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Title 40—Protection of Environment–Volume 16

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Title 40—Protection of Environment–Volume 16


Part


chapter i—Environmental Protection Agency (Continued)

63

CHAPTER I—ENVIRONMENTAL PROTECTION AGENCY (CONTINUED)

SUBCHAPTER C—AIR PROGRAMS (CONTINUED)

PART 63—NATIONAL EMISSION STANDARDS FOR HAZARDOUS AIR POLLUTANTS FOR SOURCE CATEGORIES (CONTINUED)


Authority:42 U.S.C. 7401 et seq.


Source:57 FR 61992, Dec. 29, 1992, unless otherwise noted.

Subpart NNNNN—National Emission Standards for Hazardous Air Pollutants: Hydrochloric Acid Production


Source:68 FR 19090, Apr. 17, 2003, unless otherwise noted.

What This Subpart Covers

§ 63.8980 What is the purpose of this subpart?

This subpart establishes national emission standards for hazardous air pollutants (NESHAP) and work practice standards for hazardous air pollutants (HAP) emitted from hydrochloric acid (HCl) production. This subpart also establishes requirements to demonstrate initial and continuous compliance with the emission limitations and work practice standards.


§ 63.8985 Am I subject to this subpart?

(a) You are subject to this subpart if you own or operate an HCl production facility that produces a liquid HCl product at a concentration of 30 weight percent or greater during its normal operations and is located at, or is part of, a major source of HAP. This does not include HCl production facilities that only produce occasionally liquid HCl product at a concentration of 30 weight percent or greater.


(1) An HCl production facility is the collection of unit operations and equipment associated with the production of liquid HCl product. The HCl production facility begins at the point where a gaseous stream containing HCl enters the HCl production unit. The HCl production facility includes all HCl storage tanks that contain liquid HCl product that is produced in the HCl production unit, with the exceptions noted in paragraph (a)(2) of this section. The HCl production facility also includes all HCl transfer operations that load HCl product produced in the HCl production unit into a tank truck, rail car, ship, or barge, along with the piping and other equipment in HCl service used to transfer liquid HCl product from the HCl production unit to the HCl storage tanks and/or HCl transfer operations. The HCl production facility ends at the point that the liquid HCl product produced in the HCl production unit is loaded into a tank truck, rail car, ship, or barge, at the point the HCl product enters another process on the plant site, or at the point the HCl product leaves the plant site via pipeline.


(2) Storage tanks that are dedicated feedstock tanks for another process and storage tanks that store HCl dedicated for use in wastewater treatment are not considered part of an HCl production facility.


(3) A major source of HAP emissions is any stationary source or group of stationary sources within a contiguous area under common control that emits or has the potential to emit any single HAP at a rate of 9.07 megagrams (10 tons) or more per year or any combination of HAP at a rate of 22.68 megagrams (25 tons) or more per year.


(b) An HCl production facility is not subject to this subpart if it is also subject to NESHAP under one of the subparts listed in paragraphs (b)(1) through (5) of this section.


(1) 40 CFR part 63, subpart S, National Emission Standards for Hazardous Air Pollutants from the Pulp and Paper Industry.


(2) 40 CFR part 63, subpart CCC, National Emission Standards for Hazardous Air Pollutants for Steel Pickling—HCl Process Facilities and Hydrochloric Acid Regeneration Plants.


(3) 40 CFR part 63, subpart MMM, National Emission Standards for Hazardous Air Pollutants for Pesticide Active Ingredient Production.


(4) 40 CFR part 63, section 63.994, subpart SS, National Emission Standards for Closed Vent Systems, Control Devices, Recovery Devices and Routing to a Fuel Gas System or a Process.


(5) 40 CFR part 63, subpart GGG, National Emission Standards for Pharmaceuticals Production.


(c) An HCl production facility is not subject to this subpart if it is located following the incineration of chlorinated waste gas streams, waste liquids, or solid wastes, and the emissions from the HCl production facility are subject to section 63.113(c), subpart G, National Emission Standards for Organic Hazardous Air Pollutants from the Synthetic Organic Chemical Manufacturing Industry for Process Vents, Storage Vessels, Transfer Operations, and Wastewater.


(d) An HCl production facility is not subject to this subpart if it produces HCl through the direct synthesis of hydrogen and chlorine and is part of a chlor-alkali facility.


(e) An HCl production facility is not subject to this subpart if it is a research and development facility.


(f) An HCl production facility is not subject to this subpart if all of the gaseous streams containing HCl and chlorine (Cl2) from HCl process vents, HCl storage tanks, and HCl transfer operations are recycled or routed to another process for process purpose, prior to being discharged to the atmosphere.


[68 FR 19090, Apr. 17, 2003, as amended at 71 FR 17745, Apr. 7, 2006; 85 FR 20867, Apr. 15, 2020]


§ 63.8990 What parts of my plant does this subpart cover?

(a) This subpart applies to each new, reconstructed, or existing affected source at an HCl production facility.


(b) The affected source is the group of one or more HCl production facilities at a plant site that are subject to this subpart, and all associated wastewater operations, which contain the collection of emission streams listed in paragraphs (b)(1) through (5) of this section.


(1) Each emission stream from an HCl process vent.


(2) Each emission stream from an HCl storage tank.


(3) Each emission stream from an HCl transfer operation.


(4) Each emission stream resulting from leaks from equipment in HCl service.


(5) Each emission stream from HCl wastewater operations. There are no emission limitations or other requirements in this subpart that apply to HCl wastewater operations.


(c) An affected source is a new affected source if you commenced construction of the affected source after September 18, 2001 and you met the applicability criteria of § 63.8985 at the time you commenced construction.


(d) An affected source is reconstructed if you meet the criteria as defined in § 63.2.


(e) An affected source is existing if it is not new or reconstructed.


[68 FR 19090, Apr. 17, 2003, as amended at 71 FR 17745, Apr. 7, 2006]


§ 63.8995 When do I have to comply with this subpart?

(a) If you have a new or reconstructed affected source, you must comply with this subpart according to paragraphs (a)(1) or (2) of this section.


(1) If you start up your affected source before April 17, 2003, you must comply with the emission limitations and work practice standards in this subpart no later than April 17, 2003.


(2) If you start up your affected source after April 17, 2003, you must comply with the emission limitations and work practice standards in this subpart upon startup of your affected source.


(b) If you have an existing affected source, you must comply with the emission limitations and work practice standards no later than 3 years after April 17, 2003.


(c) If you have an area source that increases its emissions or its potential to emit such that it becomes a major source of HAP, the provisions in paragraphs (c)(1) and (2) of this section apply.


(1) Any portion of the existing facility that is a new affected source or a new reconstructed source must be in compliance with this subpart upon startup.


(2) All other parts of the source must be in compliance with this subpart no later than the date 3 years after the area source becomes a major source.


(d) You must meet the notification requirements in § 63.9045 according to the schedule in § 63.9045 and in subpart A of this part. Some of the notifications must be submitted before you are required to comply with the emission limitations in this subpart.


Emission Limitations and Work Practice Standards

§ 63.9000 What emission limitations and work practice standards must I meet?

(a) With the exceptions noted in paragraphs (c) and (d) of this section, you must meet the applicable emission limit and work practice standard in table 1 to this subpart for each emission stream listed under § 63.8990(b)(1) through (4) that is part of your affected source.


(b) With the exceptions noted in paragraph (c) of this section, you must meet the applicable operating limit in Table 2 to this subpart for each emission stream listed under § 63.8990(b)(1) through (3) that is part of your affected source.


(c) The emission streams listed in paragraphs (c)(1) through (4) of this section are exempt from the emission limitations, work practice standards, and all other requirements of this subpart.


(1) Emission streams from HCl storage tanks that never store liquid HCl product with a concentration of 30 weight percent or greater.


(2) Emission streams from HCl transfer operations that never load liquid HCl product with a concentration of 30 weight percent or greater.


(3) Emission streams from HCl wastewater operations.


(4) Emission streams from HCl process vents, HCl storage tanks, and HCl transfer operations that are also subject to 40 CFR part 63, subpart EEE, National Emission Standards for Hazardous Air Pollutants for Hazardous Waste Combustors, or 40 CFR 266.107, subpart H, Burning of Hazardous Waste in Boilers and Industrial Furnaces.


(d) The emission limits for HCl storage tanks in table 1 to this subpart do not apply during periods of planned routine maintenance of HCl storage tank control devices. Periods of planned routine maintenance of each HCl storage tank control device, during which the control device does not meet the emission limits specified in table 1 to this subpart, shall not exceed 240 hours per year.


[68 FR 19090, Apr. 17, 2003, as amended at 71 FR 17745, Apr. 7, 2006]


General Compliance Requirements

§ 63.9005 What are my general requirements for complying with this subpart?

(a) Before October 13, 2020, for each existing source, and for each new or reconstructed source for which construction or reconstruction commenced after April 17, 2003, but before February 5, 2019, you must be in compliance with the emission limitations and work practice standards in this subpart at all times, except during periods of startup, shutdown, and malfunction. After October 13, 2020, for each such source you must be in compliance with the emission limitations in this subpart at all times. For new and reconstructed sources for which construction or reconstruction commenced after February 4, 2019, you must be in compliance with the emissions limitations in this subpart at all times.


(b) Before October 13, 2020, for each existing source, and for each new or reconstructed source for which construction or reconstruction commenced after April 17, 2003, but before February 5, 2019, you must always operate and maintain your affected source, including air pollution control and monitoring equipment, according to the provisions in § 63.6(e)(1)(i). After October 13, 2020 for each such source, and after April 15, 2020 for new and reconstructed sources for which construction or reconstruction commenced after February 4, 2019, at all times you must operate and maintain any affected source, including associated air pollution control equipment and monitoring equipment, in a manner consistent with safety and good air pollution control practices for minimizing emissions. The general duty to minimize emissions does not require you to make any further efforts to reduce emissions if levels required by the applicable standard have been achieved. Determination of whether a source is operating in compliance with operation and maintenance requirements will be based on information available to the Administrator which may include, but is not limited to, monitoring results, review of operation and maintenance procedures, review of operation and maintenance records, and inspection of the source.


(c) Before October 13, 2020, for each existing source, and for each new or reconstructed source for which construction or reconstruction commenced after April 17, 2003, but before February 5, 2019, you must develop a written startup, shutdown, and malfunction plan according to the provisions in § 63.6(e)(3). For each such source, a startup, shutdown, and malfunction plan is not required after October 13, 2020. No startup, shutdown, and malfunction plan is required for any new or reconstructed source for which construction or reconstruction commenced after February 4, 2019.


(d) All monitoring equipment shall be installed, calibrated, maintained, and operated according to manufacturer’s specifications or other written procedures that provide adequate assurance that the equipment would reasonably be expected to monitor accurately. For each monitoring system required in this section, you must develop, implement, and submit to the Administrator a site-specific monitoring plan that addresses the installation requirements in paragraphs (d)(1) through (3) of this section, the ongoing procedures in paragraphs (d)(4) through (6) of this section, and the requirements in § 63.9025, as applicable. You must submit the plan with your Notification of Compliance Status. Upon request of the Administrator, you must promptly correct any deficiencies in a site-specific monitoring plan and submit the revised plan.


(1) Installation of the continuous monitoring system (CMS) sampling probe or other interface at a measurement location relative to each affected process unit such that the measurement is representative of control of the exhaust emissions (e.g., on or downstream of the last control device).


(2) Performance and equipment specifications for the sample interface, the pollutant concentration or parametric signal analyzer, and the data collection and reduction system.


(3) Performance evaluation procedures and acceptance criteria (e.g., calibrations).


(4) Before October 13, 2020, for each existing source, and for each new or reconstructed source for which construction or reconstruction commenced after April 17, 2003, but before February 5, 2019, ongoing operation and maintenance (O&M) procedures in accordance with the general requirements of §§ 63.8(c)(1) and (3), (c)(4)(ii), and (c)(7) and (8), and 63.9025. After October 13, 2020 for each such source, and after April 15, 2020 for new and reconstructed sources for which construction or reconstruction commenced after February 4, 2019, ongoing operation and maintenance (O&M) procedures in accordance with the general requirements of §§ 63.8(c)(1)(ii), (c)(3), (c)(4)(ii), and (c)(7) and (8), and 63.9025.


(5) Before October 13, 2020, for each existing source, and for each new or reconstructed source for which construction or reconstruction commenced after April 17, 2003, but before February 5, 2019, ongoing data quality assurance procedures in accordance with the general requirements of § 63.8(d). After October 13, 2020 for each such source, and after April 15, 2020 for new and reconstructed sources for which construction or reconstruction commenced after February 4, 2019, ongoing data quality assurance procedures in accordance with the general requirements of § 63.8(d) except for the requirements related to startup, shutdown, and malfunction plans referenced in § 63.8(d)(3). The owner or operator shall keep these written procedures on record for the life of the affected source or until the affected source is no longer subject to the provisions of this part, to be made available for inspection, upon request, by the Administrator. If the performance evaluation plan is revised, the owner or operator shall keep previous (i.e., superseded) versions of the performance evaluation plan on record to be made available for inspection, upon request, by the Administrator, for a period of 5 years after each revision to the plan. The program of corrective action should be included in the plan required under § 63.8(d)(2).


(6) Before October 13, 2020, for each existing source, and for each new or reconstructed source for which construction or reconstruction commenced after April 17, 2003, but before February 5, 2019, ongoing recordkeeping and reporting procedures in accordance with the general requirements of § 63.10(c) and (e)(1) and (e)(2)(i). After October 13, 2020 for each such source, and after April 15, 2020 for new and reconstructed sources for which construction or reconstruction commenced after February 4, 2019, ongoing recordkeeping and reporting procedures in accordance with the general requirements of § 63.10(c)(1) through (14) and (e)(1) and (e)(2)(i).


[68 FR 19090, Apr. 17, 2003, as amended at 71 FR 20470, Apr. 20, 2006; 85 FR 20867, Apr. 15, 2020]


Testing and Initial Compliance Requirements

§ 63.9010 By what date must I conduct performance tests?

(a) If you have a new or reconstructed affected source, you must conduct performance tests within 180 calendar days after the compliance date that is specified for your source in § 63.8995(a) and according to the provisions in § 63.7(a)(2).


(b) If you have an existing affected source, you must conduct performance tests within 180 calendar days after the compliance date that is specified for your existing affected source in § 63.8995(b) and according to the provisions in § 63.7(a)(2).


(c) If you commenced construction or reconstruction between September 18, 2001 and April 17, 2003, you must demonstrate initial compliance with either the proposed emission limitation or the promulgated emission limitation no later than 180 calendar days after April 17, 2003 or within 180 calendar days after startup of the source, whichever is later, according to § 63.7(a)(2)(ix).


§ 63.9015 When must I conduct subsequent performance tests?

(a) You must conduct all applicable performance tests according to the procedures in § 63.9020 on the earlier of your title V operating permit renewal or within 5 years of issuance of your title V permit. For emission points meeting the outlet concentration limits in table 1 to this subpart without the use of a control device, all applicable performance tests must also be conducted whenever process changes are made that could reasonably be expected to increase the outlet concentration. Examples of process changes include, but are not limited to, changes in production capacity, production rate, feedstock type, or catalyst type, or whenever there is replacement, removal, or addition of recovery equipment. For purposes of this paragraph, process changes do not include: process upsets and unintentional, temporary process changes.


(b) You must report the results of subsequent performance tests within 60 days after the completion of the test. This report should also verify that the operating limits for your affected source have not changed or provide documentation of revised operating limits established as specified in Table 2 to this subpart. The reports for all subsequent performance tests should include all applicable information required in § 63.9050.


[68 FR 19090, Apr. 17, 2003, as amended at 71 FR 17745, Apr. 7, 2006]


§ 63.9020 What performance tests and other procedures must I use?

(a) You must conduct each performance test in Table 3 to this subpart that applies to you as directed in paragraphs (a)(1) through (4) of this section, except as noted in paragraphs (b) and (c) of this section.


(1) You must develop a site-specific test plan according to § 63.7(c)(2) and conduct each performance test according to the site-specific test plan.


(2) Before October 13, 2020, for each existing source, and for each new or reconstructed source for which construction or reconstruction commenced after April 17, 2003, but before February 5, 2019, you must conduct each performance test under representative conditions according to the requirements in § 63.7(e)(1) and under the specific conditions that this subpart specifies in Table 3. After October 13, 2020 for each such source, and after April 15, 2020 for new and reconstructed sources for which construction or reconstruction commenced after February 4, 2019, you must conduct each performance test under conditions representative of normal operations. The owner or operator must record the process information that is necessary to document operating conditions during the test and include in such record an explanation to support that such conditions represent normal operation. Upon request, the owner or operator shall make available to the Administrator such records as may be necessary to determine the conditions of performance tests.


(3) You may not conduct performance tests during periods of startup, shutdown, or malfunction.


(4) You must conduct at least three separate test runs for each performance test required in this section, as specified in § 63.7(e)(3). Each test run must last at least 1 hour.


(b) If you are complying with a percent reduction emission limitation, you must determine the percent reduction in accordance with paragraphs (b)(1) and (2) of this section.


(1) Calculate the mass rate of either HCl or chlorine using Equations 1 and 2 of this section:





where:

Ci, Co = Concentration of HCl or Cl2 in the gas stream at the inlet and outlet of the control device(s), respectively, dry basis, parts per million by volume.

Ei, Eo = Mass rate of HCl or Cl2 at the inlet and outlet of the control device(s), respectively, dry basis, kilogram per hour.

Mi, Mo = Molecular weight of HCl or Cl2 at the inlet and outlet of the control device(s), respectively, gram/gram-mole.

Qi, Qo = Flow rate of gas stream at the inlet and outlet of the control device(s), respectively, dry standard cubic meter per minute.

K2 = Constant, 2.494 × 10−6 (parts per million)−1 (gram-mole per standard cubic meter) (kilogram/gram) (minute/hour), where standard temperature (gram-mole per standard cubic meter) is 20 °C.

(2) Calculate the percent reduction of HCl or Cl2 using Equation 3 of this section:





where:

R = Control efficiency of control device(s).

Ei = Mass rate of HCl or Cl2 to the inlet to the control device(s), kilograms per hour.

Eo = Mass rate of HCl or Cl2 at the outlet of the control device(s), kilograms per hour.

(c) You may prepare a design evaluation in lieu of conducting a performance test for HCl storage tanks and HCl transfer operations that are not routed to a control device that also controls HCl process vent emissions or any other continuous vent stream. The design evaluation shall include documentation demonstrating that the control technique being used achieves the required control efficiency when a liquid HCl product with a concentration of 30 weight percent or greater is being loaded into the storage tank, or a tank truck, rail car, ship, or barge.


(1) If you use a caustic scrubber control device or a water scrubber control device, the design evaluation shall address the vent stream composition, constituent concentrations, liquid-to-vapor ratio, scrubbing liquid flow rate and concentration, temperature, and the reaction kinetics of the constituents with the scrubbing liquid. The design evaluation shall establish the design exhaust vent concentration level and shall include the additional information in paragraphs (c)(1)(i) and (ii) of this section for trays and a packed column scrubber.


(i) Type and total number of theoretical and actual trays.


(ii) Type and total surface area of packing for entire column and for individual packed sections, if the column contains more than one packed section.


(2) If you use any other control device, the design evaluation shall address the composition and HAP concentration of the vent stream immediately preceding the control device, as well as other parameters necessary to demonstrate that the control technique being used achieves the required control efficiency when a liquid HCl product with a concentration of 30 weight percent or greater is being loaded into the storage tank, or a tank truck, rail car, ship, or barge.


(d) You are not required to conduct a performance test for an emission point for which a performance test was conducted within the previous 5-year period, using the same test methods specified in this section and for which either no deliberate process changes have been made since the test, or the owner or operator can demonstrate that the results of the performance test, with or without adjustments, reliably demonstrate compliance despite process changes. The operating limits reported under the previous performance test shall be sufficient to meet the monitoring requirements in this subpart.


(e) You must establish all operating limits with which you will demonstrate continuous compliance with the applicable emission limits in Table 1 to this subpart as described in paragraphs (e)(1) through (3) of this section.


(1) If you use a caustic scrubber control device or water scrubber control device and you conduct a performance test, you must establish operating limits according to paragraphs (e)(1)(i) and (ii) of this section. If a series of control devices are used, you must establish separate operating limits for each device.


(i) You must establish the minimum value as the operating limit for scrubber inlet liquid or recirculating liquid flow rate, as appropriate. The minimum value shall be based on the scrubber inlet liquid or recirculating liquid flow rate, as appropriate, values measured during the performance test.


(ii) You must establish the minimum and maximum values as the operating limits for scrubber effluent pH. The minimum and maximum values shall be based on the scrubber effluent pH values measured during the performance test.


(2) If you use any other control device and you conduct a performance test, you must establish operating limits according to your site-specific test plan submitted in accordance with § 63.7(c)(2)(i). The operating limits shall be based on the operating parameter values measured during the performance test. If a series of control devices are used, you must establish separate operating limits for each device.


(3) If you do not conduct a performance test for a HCl storage tank or HCl transfer operation, you must use engineering assessments and/or manufacturer’s recommendations to establish the operating limits specified in paragraphs (e)(1)(i) and (ii), or (e)(2), of this section.


(4) As needed in applicability determinations, you must use ASTM E224 to determine the HCl concentration in liquid products.


[68 FR 19090, Apr. 17, 2003, as amended at 85 FR 20867, Apr. 15, 2020]


§ 63.9025 What are my monitoring installation, operation, and maintenance requirements?

(a) For each operating parameter that you are required by § 63.9020(e) to monitor, you must install, operate, and maintain each CMS according to the requirements in paragraphs (a)(1) through (6) of this section.


(1) You must operate your CMS and collect data at all times the process is operating.


(2) You must collect data from at least four equally spaced periods each hour.


(3) For at least 75 percent of the operating hours in a 24-hour period, you must have valid data (as defined in your site-specific monitoring plan) for at least 4 equally spaced periods each hour.


(4) For each hour that you have valid data from at least four equally spaced periods, you must calculate the hourly average value using all valid data or, where data are collected from an automated CMS, using at least one measured value per minute if measured more frequently than once per minute.


(5) You must calculate the daily average using all of the hourly averages calculated according to paragraph (a)(4) of this section for the 24-hour period.


(6) You must record the results for each inspection, calibration, and validation check as specified in your site-specific monitoring plan.


(b) For scrubber control devices, you may request approval, in accordance with § 63.8(f), to monitor parameters other than those specified in § 63.9020(e). In accordance with § 63.8(f), you must submit a monitoring plan to the Administrator and the plan must meet the requirements in paragraphs (a) and (b)(1) through (3) of this section. You must conduct monitoring in accordance with the plan submitted to the Administrator unless comments received from the Administrator require an alternate monitoring scheme.


(1) Identify the operating parameter to be monitored to ensure that the control or capture efficiency measured during the initial compliance test is maintained.


(2) Discuss why this parameter is appropriate for demonstrating ongoing compliance.


(3) Identify the specific monitoring procedures.


(c) For any other control device, you must ensure that the CMS is operated according to a monitoring plan submitted to the Administrator as required by § 63.8(f). The monitoring plan must meet the requirements in paragraphs (a) and (c)(1) through (3) of this section. You must conduct monitoring in accordance with the plan submitted to the Administrator, as amended, unless comments received from the Administrator require an alternate monitoring scheme.


(1) Identify the operating parameter to be monitored to ensure that the control or capture efficiency measured during the initial compliance test is maintained.


(2) Discuss why this parameter is appropriate for demonstrating ongoing compliance.


(3) Identify the specific monitoring procedures.


[68 FR 19090, Apr. 17, 2003, as amended at 71 FR 17745, Apr. 7, 2006; 85 FR 20868, Apr. 15, 2020]


§ 63.9030 How do I demonstrate initial compliance with the emission limitations and work practice standards?

(a) You must demonstrate initial compliance with each emission limit and work practice standard that applies to you according to Table 4 to this subpart.


(b) You must establish each site-specific operating limit in Table 2 to this subpart that applies to you according to the requirements in § 63.9020 and Table 3 to this subpart.


(c) For existing sources and for new or reconstructed sources which commenced construction or reconstruction after April 17, 2003, but before February 5, 2019, before October 13, 2020, you must submit the Notification of Compliance Status containing the results of the initial compliance demonstration according to the requirements in § 63.9045(f) and (g). After October 13, 2020 for such sources, and after April 15, 2020 for new or reconstructed sources which commence construction or reconstruction after February 4, 2019, you must submit the Notification of Compliance Status containing the results of the initial compliance demonstration according to the requirements in §§ 63.9045(f) and (g) and 63.9050(d).


[68 FR 19090, Apr. 17, 2003, as amended at 85 FR 20868, Apr. 15, 2020]


Continuous Compliance Requirements

§ 63.9035 How do I monitor and collect data to demonstrate continuous compliance?

(a) You must monitor and collect data according to this section.


(b) If you use a caustic scrubber or a water scrubber/absorber to meet the emission limits in Table 1 to this subpart, you must keep the records specified in paragraphs (b)(1) and (2) of this section to support your compliance demonstration.


(1) Records of daily average scrubber inlet liquid or recirculating liquid flow rate, as appropriate.


(2) Records of the daily average scrubber effluent pH.


(c) If you use any other control device to meet the emission limits in Table 1 to this subpart, you must keep records of the operating parameter values identified in your monitoring plan in § 63.9025(c) to support your compliance demonstration.


(d) Except for monitor malfunctions, associated repairs, and required quality assurance or control activities (including, as applicable, calibration checks and required zero and span adjustments), you must monitor continuously (or collect data at all required intervals) at all times that the affected source is operating. This includes periods of startup, shutdown, or malfunction when the affected source is operating. A monitoring malfunction includes, but is not limited to, any sudden, infrequent, not reasonably preventable failure of the monitoring equipment to provide valid data. Monitoring failures that are caused in part by poor maintenance or careless operation are not malfunctions.


(e) You may not use data recorded during monitoring malfunctions, associated repairs, and required quality assurance or control activities in data averages and calculations used to report emission or operating levels, nor may such data be used in fulfilling a minimum data availability requirement, if applicable. You must use all the data collected during all other periods in assessing the operation of the control device and associated control system.


§ 63.9040 How do I demonstrate continuous compliance with the emission limitations and work practice standards?

(a) You must demonstrate continuous compliance with each emission limit and work practice standard in Table 1 to this subpart that applies to you according to Table 4 to this subpart.


(b) You must demonstrate continuous compliance with each operating limit in Table 2 of this subpart that applies to you according to Tables 4 and 5 to this subpart.


(c) You must report each instance in which you did not meet an emission limit, work practice standard or operating limit in Table 1 or 2 to this subpart, respectively, that applies to you. This includes periods of startup, shutdown, and malfunction. These instances are deviations from the emission limitations in this subpart. These deviations must be reported according to the requirements in § 63.9050.


(d) [Reserved]


(e) For existing sources and for new or reconstructed sources which commenced construction or reconstruction after April 17, 2003, but before February 5, 2019, before October 13, 2020, consistent with §§ 63.6(e) and 63.7(e)(1), deviations that occur during a period of startup, shutdown, or malfunction are not violations if you demonstrate to the Administrator’s satisfaction that you were operating in accordance with § 63.6(e)(1). The Administrator will determine whether deviations that occur during a period of startup, shutdown, or malfunction are violations, according to the provisions in § 63.6(e). After October 13, 2020 for such sources, and after April 15, 2020 for new and reconstructed sources which commence construction or reconstruction after February 4, 2019, the exemptions for periods of startup, shutdown, and malfunction in § 63.6(e) no longer apply.


(f) An owner or operator may designate a process vent as a maintenance vent if the vent is only used as a result of startup or shutdown, of equipment where equipment is emptied, depressurized, degassed or placed into service. The owner or operator does not need to designate a maintenance vent as a HCl process vent, HCl storage tank vent, or an HCl transfer operation. The owner or operator must comply with the applicable requirements in paragraphs (f)(1) and (2) of this section for each maintenance vent by October 13, 2020 or the date of startup for new and reconstructed sources, whichever is later, unless an extension is requested in accordance with the provisions in § 63.6(i).


(1) Prior to venting to the atmosphere, process liquids must be removed from the equipment as much as practical and the equipment must be washed with water or purged with air or otherwise depressurized to a control device, fuel gas system, or back to the process to remove the HCl and Cl2 until the equipment served by the maintenance vent contains less than 20 pounds of HCl or Cl2.


(2) For maintenance vents complying with the requirements in paragraph (f)(1) of this section, the owner or operator shall demonstrate the mass of HCl or Cl2 in the equipment served by the maintenance vent is less than 20 pounds for each maintenance activity based on the equipment size and contents after considering any contents drained or purged from the equipment. Equipment size may be determined from equipment design specifications. Equipment contents may be determined using process knowledge. The owner or operator must maintain records for five years of the number of maintenance activities for which maintenance vent provisions are used during each reporting period.


[68 FR 19090, Apr. 17, 2003, as amended at 71 FR 20470, Apr. 20, 2006; 85 FR 20868, Apr. 15, 2020]


Notifications, Reports, and Records

§ 63.9045 What notifications must I submit and when?

(a) You must submit all of the notifications in §§ 63.7(b) and (c), 63.8(f)(4) and (6), and 63.9 (b) through (h) that apply to you by the dates specified.


(b) As specified in § 63.9(b)(2), if you start up your affected source before April 17, 2003, you must submit an Initial Notification not later than 120 calendar days after April 17, 2003, or no later than 120 days after the source becomes subject to this subpart, whichever is later.


(c) As specified in § 63.9(b)(4), if you start up your new or reconstructed affected source on or after April 17, 2003, you must submit the application for construction or reconstruction required by § 63.9(b)(1)(iii) in lieu of the initial notification.


(d) You must submit a notification of intent to conduct a performance test at least 60 calendar days before the performance test is scheduled to begin, as required in § 63.7(b)(1).


(e) [Reserved]


(f) You must submit the Notification of Compliance Status, including the performance test results, within 180 calendar days after the applicable compliance dates specified in § 63.8995.


(g) The Notification of Compliance Status must also include the information in paragraphs (g)(1) through (2) of this section that applies to you.


(1) Each operating parameter value averaged over the full period of the performance test (for example, average pH).


(2) Each operating parameter range within which HAP emissions are reduced to the level corresponding to meeting the applicable emission limits in Table 1 to this subpart.


[68 FR 19090, Apr. 17, 2003, as amended at 71 FR 17745, Apr. 7, 2006; 85 FR 20868, Apr. 15, 2020; 85 FR 73916, Nov. 19, 2020]


§ 63.9050 What reports must I submit and when?

(a) You must submit a compliance report that includes the information in paragraphs (c) through (e) of this section, as applicable, as specified in table 6 to this subpart.


(b) Unless the Administrator has approved a different schedule for submission of reports under § 63.10(a), you must submit each report according to paragraphs (b)(1) through (5) of this section.


(1) The first compliance report must cover the period beginning on the compliance date that is specified for your affected source in § 63.8995 and ending on June 30 or December 31, whichever date is the first date following the end of the first calendar half after the compliance date that is specified for your source in § 63.8995 (i.e., June 30, 2006, for sources existing on April 17, 2006).


(2) The first compliance report must be postmarked or delivered no later than July 31 or January 31, whichever date follows the end of the first calendar half after the compliance date that is specified for your affected source in § 63.8995 (i.e., July 31, 2006, for sources existing on April 17, 2006).


(3) Each subsequent compliance report must cover the semiannual reporting period from January 1 through June 30 or the semiannual reporting period from July 1 through December 31.


(4) Each subsequent compliance report must be postmarked or delivered no later than July 31 or January 31, whichever date is the first date following the end of the semiannual reporting period.


(5) For each affected source that is subject to permitting regulations pursuant to 40 CFR part 70 or 71, and if the permitting authority has established dates for submitting semiannual reports pursuant to 40 CFR 70.6 (a)(3)(iii)(A) or 71.6 (a)(3)(iii)(A), you may submit the first and subsequent compliance reports according to the dates the permitting authority has established instead of according to the dates in paragraphs (b)(1) through (4) of this section.


(c) The compliance report must contain the following information in paragraphs (c)(1) through (10) of this section.


(1) Company name and address.


(2) Statement by a responsible official with that official’s name, title, and signature, certifying the truth, accuracy, and completeness of the content of the report.


(3) Date of report and beginning and ending dates of the reporting period.


(4) For existing sources and for new or reconstructed sources for which construction or reconstruction commenced after April 17, 2003, but before February 5, 2019, before October 13, 2020, if you had a startup, shutdown, or malfunction during the reporting period and you took actions consistent with your startup, shutdown, and malfunction plan, the compliance report must include the information in § 63.10(d)(5)(i). A startup, shutdown, and malfunction plan and the information in § 63.10(d)(5)(i) is not required after October 13, 2020.


(5) For existing sources and for new or reconstructed sources which commenced construction or reconstruction after April 17, 2003, but before February 5, 2019, before October 13, 2020, if there are no deviations from any emission limitations that apply to you, a statement that there were no deviations from the emission limitations during the reporting period.


(6) If there were no periods during which the CMS was out-of-control in accordance with the monitoring plan, a statement that there were no periods during which the CMS was out-of-control during the reporting period.


(7) Verification that you continue to use the equipment LDAR plan and information that explains any periods when the procedures in the plan were not followed and the corrective actions were not taken.


(8) If you did not make revisions to your site-specific monitoring plan and/or LDAR plan during the reporting period, a statement that you did not make any revisions to your site-specific monitoring plan and/or LDAR plan during the reporting period. If you made revisions to your site-specific monitoring plan and/or LDAR plan during the reporting period, a copy of the revised plan.


(9) If you meet the outlet concentration limit in table 1 to this subpart without the use of a control device for any emission point, verification that you have not made any process changes that could reasonably be expected to increase the outlet concentration since your most recent performance test for that emission point.


(10) The information specified in paragraphs (c)(10)(i) and (ii) of this section for those planned routine maintenance operations that caused or may cause an HCl storage tank control device not to meet the emission limits in table 1 to this subpart, as applicable.


(i) A description of the planned routine maintenance that was performed for each HCl storage tank control device during the reporting period. This description shall include the type of maintenance performed and the total number of hours during the reporting period that the HCl storage tank control device did not meet the emission limits in table 1 to this subpart, as applicable, due to planned routine maintenance.


(ii) A description of the planned routine maintenance that is anticipated to be performed for each HCl storage tank control device during the next reporting period. This description shall include the type of maintenance necessary, planned frequency of maintenance, and lengths of maintenance periods.


(d) For each deviation from an emission limitation occurring at an affected source where you are using a continuous monitoring system (CMS) to comply with the emission limitation in this subpart, you must include the information in paragraphs (c)(1) through (6) of this section and the following information in paragraphs (d)(1) through (9) of this section and § 63.10(e)(3)(vi). This includes periods of startup, shutdown, and malfunction.


(1) The date and time that each malfunction started and stopped.


(2) The date and time that each CMS was inoperative, except for zero (low-level) and high-level checks.


(3) The date, time, and duration that each CMS was out-of-control, including the information in § 63.8(c)(8).


(4) The date and time that each deviation started and stopped, and whether each deviation occurred during a period of startup, shutdown, or malfunction or during another period.


(5) A summary of the total duration of the deviation during the reporting period and the total duration as a percent of the total source operating time during that reporting period.


(6) A breakdown of the total duration of the deviations during the reporting period into those that are due to startup, shutdown, control equipment problems, process problems, other known causes, and other unknown causes.


(7) A summary of the total duration of CMS downtime during the reporting period, and the total duration of CMS downtime as a percent of the total source operating time during that reporting period.


(8) A brief description of the process units.


(9) A description of any changes in CMS, processes, or controls since the last reporting period.


(e) Each affected source that has obtained a title V operating permit pursuant to 40 CFR part 70 or 71 must report all deviations as defined in this subpart in the semiannual monitoring report required by 40 CFR 70.6(a)(3)(iii)(A) or 71.6(a)(3)(iii)(A). If an affected source submits a compliance report pursuant to Table 6 to this subpart along with, or as part of, the semiannual monitoring report required by 40 CFR 70.6(a)(3)(iii)(A) or 71.6(a)(3)(iii)(A), and the compliance report includes all required information concerning deviations from any emission limitation in this subpart, submission of the compliance report shall be deemed to satisfy any obligation to report the same deviations in the semiannual monitoring report. However, submission of a compliance report shall not otherwise affect any obligation the affected source may have to report deviations from permit requirements to the permit authority.


(f) For existing sources and for new or reconstructed sources which commenced construction or reconstruction after April 17, 2003, but before February 5, 2019, before October 13, 2020, for each startup, shutdown, or malfunction during the reporting period that is not consistent with your startup, shutdown, and malfunction plan you must submit an immediate startup, shutdown and malfunction report. Unless the Administrator has approved a different schedule for submission of reports under § 63.10(a), you must submit each report according to paragraphs (f)(1) and (2) of this section. An immediate startup, shutdown, and malfunction report is not required after October 13, 2020.


(1) An initial report containing a description of the actions taken for the event must be submitted by fax or telephone within 2 working days after starting actions inconsistent with the plan.


(2) A follow-up report containing the information listed in § 63.10(d)(5)(ii) must be submitted within 7 working days after the end of the event unless you have made alternative reporting arrangements with the permitting authority.


(g) Within 60 days after the date of completing each performance test required by this subpart, you must submit the results of the performance test following the procedures specified in paragraphs (g)(1) through (3) of this section.


(1) Data collected using test methods supported by the EPA’s Electronic Reporting Tool (ERT) as listed on the EPA’s ERT website (https://www.epa.gov/electronic-reporting-air-emissions/electronic-reporting-tool-ert) at the time of the test. Submit the results of the performance test to the EPA via the Compliance and Emissions Data Reporting Interface (CEDRI). CEDRI can be accessed through the EPA’s Central Data Exchange (CDX) (https://cdx.epa.gov/). The data must be submitted in a file format generated through the use of the EPA’s ERT. Alternatively, you may submit an electronic file consistent with the extensible markup language (XML) schema listed on the EPA’s ERT website.


(2) Data collected using test methods that are not supported by the EPA’s ERT as listed on the EPA’s ERT website at the time of the test. Submit the results of the performance test as an attachment in the ERT.


(3) Confidential business information (CBI). If you claim some of the information submitted under paragraph (g)(1) of this section is CBI, you must submit a complete file, including information claimed to be CBI, to the EPA. The file must be generated through the use of the EPA’s ERT or an alternate electronic file consistent with the XML schema listed on the EPA’s ERT website. Submit the file on a compact disc, flash drive or other commonly used electronic storage medium and clearly mark the medium as CBI. Mail the electronic medium to U.S. EPA/OAQPS/CORE CBI Office, Attention: Group Leader, Measurement Policy Group, MD C404-02, 4930 Old Page Rd., Durham, NC 27703. The same file with the CBI omitted must be submitted to the EPA via the EPA’s CDX as described in paragraph (g)(1) of this section.


(h) Within 60 days after the date of completing each CMS performance evaluation (as defined in § 63.2), you must submit the results of the performance evaluation following the procedures specified in paragraphs (h)(1) through (3) of this section.


(1) Performance evaluations of CMS measuring relative accuracy test audit (RATA) pollutants that are supported by the EPA’s ERT as listed on the EPA’s ERT website at the time of the evaluation. Submit the results of the performance evaluation to the EPA via CEDRI, which can be accessed through the EPA’s CDX. The data must be submitted in a file format generated through the use of the EPA’s ERT. Alternatively, you may submit an electronic file consistent with the XML schema listed on the EPA’s ERT website.


(2) Performance evaluations of CMS measuring RATA pollutants that are not supported by the EPA’s ERT as listed on the EPA’s ERT website at the time of the evaluation. Submit the results of the performance evaluation as an attachment in the ERT.


(3) Confidential business information (CBI). If you claim some of the information submitted under paragraph (g)(1) of this section is CBI, you must submit a complete file, including information claimed to be CBI, to the EPA. The file must be generated through the use of the EPA’s ERT or an alternate electronic file consistent with the XML schema listed on the EPA’s ERT website. Submit the file on a compact disc, flash drive or other commonly used electronic storage medium and clearly mark the medium as CBI. Mail the electronic medium to U.S. EPA/OAQPS/CORE CBI Office, Attention: Group Leader, Measurement Policy Group, MD C404-02, 4930 Old Page Rd., Durham, NC 27703. The same file with the CBI omitted must be submitted to the EPA via the EPA’s CDX as described in paragraph (g)(1) of this section.


(i) You must submit to the Administrator compliance reports. Beginning on April 16, 2021 or 1 year after the appropriate electronic reporting template becomes available on the CEDRI website, whichever is later, submit all subsequent reports following the procedure specified in paragraph (l) of this section.


(j) You must submit to the Administrator performance evaluations. Beginning on April 16, 2021 or 1 year after the appropriate electronic reporting template becomes available on the CEDRI website, whichever is later, submit all subsequent reports following the procedure specified in paragraph (l) of this section.


(k) You must submit to the Administrator a Notification of Compliance Status. Beginning on April 16, 2021 or 1 year after the appropriate electronic reporting template becomes available on the CEDRI website, whichever is later, submit all subsequent reports following the procedure specified in paragraph (l) of this section.


(l) If you are required to submit reports following the procedure specified in this paragraph, you must submit reports to the EPA via CEDRI. CEDRI can be accessed through the EPA’s CDX (https://cdx.epa.gov/). You must use the appropriate electronic report template on the CEDRI website (https://www.epa.gov/electronic-reporting-air-emissions/compliance-and-emissions-data-reporting-interface-cedri) for this subpart. The date report templates become available will be listed on the CEDRI website. The report must be submitted by the deadline specified in this subpart, regardless of the method in which the report is submitted. If you claim some of the information required to be submitted via CEDRI is CBI, submit a complete report, including information claimed to be CBI, to the EPA. The report must be generated using the appropriate form on the CEDRI website. Submit the file on a compact disc, flash drive, or other commonly used electronic storage medium and clearly mark the medium as CBI. Mail the electronic medium to U.S. EPA/OAQPS/CORE CBI Office, Attention: Group Leader, Measurement Policy Group, MD C404-02, 4930 Old Page Rd., Durham, NC 27703. The same file with the CBI omitted must be submitted to the EPA via the EPA’s CDX as described earlier in this paragraph.


(m) If you are required to electronically submit a report through CEDRI in the EPA’s CDX, you may assert a claim of EPA system outage for failure to timely comply with the reporting requirement. To assert a claim of EPA system outage, you must meet the requirements outlined in paragraphs (m)(1) through (7) of this section.


(1) You must have been or will be precluded from accessing CEDRI and submitting a required report within the time prescribed due to an outage of either the EPA’s CEDRI or CDX systems.


(2) The outage must have occurred within the period of time beginning 5 business days prior to the date that the submission is due.


(3) The outage may be planned or unplanned.


(4) You must submit notification to the Administrator in writing as soon as possible following the date you first knew, or through due diligence should have known, that the event may cause or caused a delay in reporting.


(5) You must provide to the Administrator a written description identifying:


(i) The date, time and length of the outage;


(ii) A rationale for attributing the delay in reporting beyond the regulatory deadline to EPA system outage;


(iii) Measures taken or to be taken to minimize the delay in reporting; and


(iv) The date by which you propose to report, or if you have already met the reporting requirement at the time of the notification, the date you reported.


(6) The decision to accept the claim of EPA system outage and allow an extension to the reporting deadline is solely within the discretion of the Administrator.


(7) In any circumstance, the report must be submitted electronically as soon as possible after the outage is resolved.


(n) If you are required to electronically submit a report through CEDRI in the EPA’s CDX, you may assert a claim of force majeure for failure to timely comply with the reporting requirement. To assert a claim of force majeure, you must meet the requirements outlined in paragraphs (n)(1) through (5) of this section.


(1) You may submit a claim if a force majeure event is about to occur, occurs, or has occurred or there are lingering effects from such an event within the period of time beginning 5 business days prior to the date the submission is due. For the purposes of this section, a force majeure event is defined as an event that will be or has been caused by circumstances beyond the control of the affected facility, its contractors, or any entity controlled by the affected facility that prevents you from complying with the requirement to submit a report electronically within the time period prescribed. Examples of such events are acts of nature (e.g., hurricanes, earthquakes, or floods), acts of war or terrorism, or equipment failure or safety hazard beyond the control of the affected facility (e.g., large scale power outage).


(2) You must submit notification to the Administrator in writing as soon as possible following the date you first knew, or through due diligence should have known, that the event may cause or caused a delay in reporting.


(3) You must provide to the Administrator:


(i) A written description of the force majeure event;


(ii) A rationale for attributing the delay in reporting beyond the regulatory deadline to the force majeure event;


(iii) Measures taken or to be taken to minimize the delay in reporting; and


(iv) The date by which you propose to report, or if you have already met the reporting requirement at the time of the notification, the date you reported.


(4) The decision to accept the claim of force majeure and allow an extension to the reporting deadline is solely within the discretion of the Administrator.


(5) In any circumstance, the reporting must occur as soon as possible after the force majeure event occurs.


[68 FR 19090, Apr. 17, 2003, as amended at 71 FR 17745, Apr. 7, 2006; 85 FR 20868, Apr. 15, 2020]


§ 63.9055 What records must I keep?

(a) You must keep a copy of each notification and report that you submitted to comply with this subpart, including all documentation supporting any Initial Notification or Notification of Compliance Status that you submitted, as required in § 63.10(b)(2)(xiv).


(b) You must also keep the following records specified in paragraphs (b)(1) through (5) of this section.


(1) For existing sources and for new or reconstructed sources which commenced construction or reconstruction after April 17, 2003, but before February 5, 2019, before October 13, 2020, the records in § 63.6(e)(3)(iii) through (v) related to startup, shutdown, and malfunction for a period of 5 years. A startup, shutdown, and malfunction plan is not required after October 13, 2020.


(2) Records of performance tests as required in § 63.10(b)(2)(viii).


(3) Records of operating parameter values that are consistent with your monitoring plan.


(4) Records of the date and time that each deviation started and stopped and whether the deviation occurred during a period of startup, shutdown, or malfunction or during another period.


(5) Copies of the current versions of the site-specific monitoring plan and the equipment LDAR plan. You also must submit copies of these plans and any revisions or updates to the Administrator for comment only (not for approval).


(6) Records of the planned routine maintenance performed on each HCl storage tank control device including the duration of each time the control device does not meet the emission limits in table 1 to this subpart, as applicable, due to planned routine maintenance. Such a record shall include the information specified in paragraphs (b)(6)(i) and (ii) of this section.


(i) The first time of day and date the emission limits in table 1 to this subpart, as applicable, were not met at the beginning of the planned routine maintenance, and


(ii) The first time of day and date the emission limits in table 1 to this subpart, as applicable, were met at the conclusion of the planned routine maintenance.


(c) After October 13, 2020, you must keep records of each deviation specified in paragraphs (c)(1) through (3) of this section.


(1) For each deviation record the date, time, and duration of each deviation.


(2) For each deviation, record and retain a list of the affected sources or equipment, an estimate of the quantity of each regulated pollutant emitted over any emission limit and a description of the method used to estimate the emissions.


(3) Record actions taken to minimize emissions in accordance with § 63.9005(b), and any corrective actions taken to return the affected unit to its normal or usual manner of operation.


(d) Any records required to be maintained by this part that are submitted electronically via the EPA’s CEDRI may be maintained in electronic format. This ability to maintain electronic copies does not affect the requirement for facilities to make records, data, and reports available upon request to a delegated air agency or the EPA as part of an on-site compliance evaluation.


[68 FR 19090, Apr. 17, 2003, as amended at 71 FR 17746, Apr. 7, 2006; 85 FR 20870, Apr. 15, 2020]


§ 63.9060 In what form and how long must I keep my records?

(a) Your records must be in a form suitable and readily available for expeditious inspection and review, according to § 63.10(b)(1).


(b) As specified in § 63.10(b)(1), you must keep each record for 5 years following the date of each occurrence, measurement, maintenance, corrective action, report, or record.


(c) You must keep each record on site, or readily accessible from on site through a computer or other means, for at least 2 years after the date of each occurrence, measurement, maintenance, corrective action, report, or record, according to § 63.10(b)(1). You can keep the records off site for the remaining 3 years. Records may be maintained in hard copy or computer-readable format including, but not limited to, on paper, microfilm, hard disk drive, floppy disk, compact disk, magnetic tape, or microfiche.


(d) You must keep each previous (i.e., superseded) version of the site-specific monitoring plan and the LDAR plan for a period of 5 years after revision of the plan. If, at any time after adoption of a site-specific monitoring plan or an LDAR plan, your affected source ceases operation or is otherwise no longer subject to the provisions of this subpart, you must retain a copy of the most recent plan for 5 years from the date your source ceases operation or is no longer subject to this subpart.


Other Requirements and Information

§ 63.9065 What parts of the General Provisions apply to me?

(a) Table 7 to this subpart shows which parts of the General Provisions in §§ 63.1 through 63.15 apply to you.


§ 63.9070 Who implements and enforces this subpart?

(a) This subpart can be implemented and enforced by us, the U.S. EPA, or a delegated authority such as your State, local, or tribal agency. If the U.S. EPA Administrator has delegated authority to your State, local, or tribal agency, then that agency, as well as U.S. EPA, has the authority to implement and enforce this subpart. You should contact your U.S. EPA Regional Office to find out if this subpart is delegated to your State, local, or tribal agency.


(b) In delegating implementation and enforcement authority of this subpart to a State, local, or tribal agency under section 40 CFR part 63, subpart E, the authorities contained in paragraph (c) of this section are retained by the Administrator of U.S. EPA and are not transferred to the State, local, or tribal agency.


(c) The authorities in paragraphs (c)(1) through (4) of this section that cannot be delegated to State, local, or tribal agencies are as follows.


(1) Approval of alternatives to requirements in §§ 63.8980, 63.8985, 63.8990, 63.8995, and 63.9000.


(2) Approval of major changes to test methods under § 63.7(e)(2)(ii) and (f) and as defined in § 63.90.


(3) Approval of major changes to monitoring under § 63.8(f) and as defined in § 63.90.


(4) Approval of major changes to recordkeeping and reporting under § 63.10(f) and as defined in § 63.90.


§ 63.9075 What definitions apply to this subpart?

Terms used in this subpart are defined in the Clean Air Act in 40 CFR 63.2 and in this section as follows:


Caustic scrubber control device means any add-on device that mixes an aqueous stream or slurry containing a caustic substance with the exhaust gases from an HCl process vent, HCl storage tank, or HCl transfer operation to control emissions of HCl and/or Cl2.


Chlor-alkali facility means a facility where chlorine and sodium or potassium hydroxide are produced as co-products and hydrogen is produced as a by-product in an electrolytic process using either mercury cells, diaphragm cells, or membrane cells.


Continuous monitoring system, for purposes of the final rule, means liquid flow monitoring devices that meet the performance specifications given in § 63.9025(a); or pH monitoring devices that meet the performance specifications given in § 63.9025(a); or other control devices as mentioned in 63.9025(a) and (b) or § 63.9025(a) and (c).


Control device means an add-on device used to reduce HCl and/or Cl2 emissions from an HCl process vent, HCl storage tank, or HCl transfer operation at an HCl production facility. An HCl production unit is not a control device.


Deviation means any instance in which an affected source subject to this subpart, or an owner or operator of such a source:


(1) Fails to meet any requirement or obligation established by this subpart, including but not limited to any emission limitation or work practice standard;


(2) Fails to meet any term or condition that is adopted to implement an applicable requirement in this subpart and that is included in the operating permit for any affected source required to obtain such a permit; or


(3) Fails to meet any emission limitation or work practice standard in this subpart during startup, shutdown, or malfunction, regardless of whether or not such failure is permitted by this subpart.


Emission limitation means any emission limit or operating limit.


Emission stream means a gaseous stream from an HCl process vent, an HCl storage tank, an HCl transfer operation, leaking equipment in HCl service, or HCl wastewater operations that is discharged to the atmosphere. Gaseous streams from HCl process vents, HCl storage tanks, and HCl transfer operations that are routed to another process or recycled for reaction or other use (i.e., for pH control) of the HCl and/or Cl2 are not emission streams. Gaseous streams from HCl transfer operations that are vapor balanced to an HCl storage tank subject to this subpart are not emission streams.


Equipment in HCl service means each pump, compressor, agitator, pressure relief device, sampling connection system, open-ended valve or line, valve, connector, and instrumentation system in an HCl production facility that contains 30 weight percent or greater of liquid HCl or 5 weight percent or greater of gaseous HCl at any time.


HCl process vent means the point of discharge to the atmosphere, or point of entry into a control device, of a gaseous stream that originates from an HCl production unit. The following points of discharge are not HCl process vents:


(1) A leak from equipment in HCl service subject to this subpart.


(2) An exit from a control device used to comply with this subpart.


(3) An HCl storage tank vent or HCl transfer operation vent subject to this subpart.


(4) A HCl wastewater operation vent subject to this subpart.


(5) A point of discharge from a relief valve.


(6) A point of discharge from an analyzer.


HCl production facility is defined in § 63.8985(a)(1).


HCl production unit means an absorber or other vessel in which a liquid HCl product is manufactured by absorbing gaseous HCl into either water or an aqueous HCl solution.


HCl storage tank means a tank or other vessel that is used to store liquid HCl product. Tanks or vessels permanently attached to motor vehicles (such as trucks, railcars, barges, or ships) are not HCl storage tanks.


HCl transfer operation means the loading, into a tank truck, railcar, ship, or barge, of liquid HCl from a transfer (or loading) rack (as defined in this section) for which the predominant use is liquid HCl. The predominant use of a transfer (or loading) rack is the material that is loaded by the transfer (or loading) rack in the greatest amount.


HCl wastewater operation means an operation that handles and processes water containing HCl that is discarded from an HCl production facility.


Plant site means all contiguous or adjoining property that is under common control, including properties that are separated only by a road or other public right-of-way. Common control includes properties that are owned, leased, or operated by the same entity, parent entity, subsidiary, or any combination thereof.


Research and development facility means laboratory and pilot plant operations whose primary purpose is to conduct research and development into new processes and products, where the operations are under close supervision of technically trained personnel, and the operations are not engaged in the manufacture of products for commercial sale, except in a de minimis manner.


Responsible official means responsible official as defined in 40 CFR 70.2 of this chapter.


Transfer (or loading) rack means the collection of loading arms and loading hoses, at a single loading rack, that are used to fill tank trucks, railcars, ships, and/or barges. Transfer rack includes the associated pumps, meters, shutoff valves, relief valves, and other piping and valves.


Vapor balanced means connected to a piping system that is designed to collect vapors displaced from tank trucks, rail cars, ships, or barges during loading, and to route the collected vapors to the storage vessel from which the liquid being loaded originated, or to another storage vessel connected by a common header.


Vent means the point of discharge to the atmosphere or to a control device from either an HCl process vent, an HCl storage tank, or an HCl transfer operation.


Water scrubber control device means any add-on device that mixes an aqueous stream not containing a caustic substance with the exhaust gases from an HCl process vent, HCl storage tank, or HCl transfer operation to control emissions of HCl and/or Cl2.


[68 FR 19090, Apr. 17, 2003, as amended at 71 FR 17746, Apr. 7, 2006]


Table 1 to Subpart NNNNN of Part 63—Emission Limits and Work Practice Standards

As stated in § 63.9000(a), you must comply with the following emission limits and work practice standards for each emission stream that is part of an affected source.


For each . . .
You must meet the following emission limit and work practice standard
1. Emission stream from an HCl process vent at an existing sourcea. Reduce HCl emissions by 99 percent or greater or achieve an outlet concentration of 20 ppm by volume or less; and
b. Reduce Cl2 emissions by 99 percent or greater or achieve an outlet concentration of 100 ppm by volume or less.
2. Emission stream from an HCl storage tank at an existing sourceReduce HCl emissions by 99 percent or greater or achieve an outlet concentration of 120 ppm by volume or less.
3. Emission stream from an HCl transfer operation at an existing sourceReduce HCl emissions by 99 percent or greater or achieve an outlet concentration of 120 ppm by volume or less.
4. Emission stream from leaking equipment in HCl service at existing and new sourcesa. Prepare and operate at all times according to an equipment LDAR plan that describes in detail the measures that will be put in place to detect leaks and repair them in a timely fashion; and
b. Submit the plan to the Administrator for comment only with your Notification of Compliance Status; and
c. You may incorporate by reference in such plan existing manuals that describe the measures in place to control leaking equipment emissions required as part of other federally enforceable requirements, provided that all manuals that are incorporated by reference are submitted to the Administrator.
5. Emission stream from an HCl process vent at a new sourcea. Reduce HCl emissions by 99.4 percent or greater or achieve an outlet concentration of 12 ppm by volume or less; and
b. Reduce Cl2 emissions by 99.8 percent or greater or achieve an outlet concentration of 20 ppm by volume or less.
6. Emission stream from an HCl storage tank at a new sourceReduce HCl emissions by 99.9 percent or greater or achieve an outlet concentration of 12 ppm by volume or less.
7. Emission stream from an HCl transfer operation at a new sourceReduce HCl emissions by 99 percent or greater or achieve an outlet concentration of 120 ppm by volume or less.

[68 FR 19090, Apr. 17, 2003, as amended at 71 FR 17746, Apr. 7, 2006; 85 FR 20870, Apr. 15, 2020]


Table 2 to Subpart NNNNN of Part 63—Operating Limits

As stated in § 63.9000(b), you must comply with the following operating limits for each emission stream that is part of an affected source that is vented to a control device.


For each . . .
You must . . .
1. Caustic scrubber or water scrubber/absorbera. Maintain the daily average scrubber inlet liquid or recirculating liquid flow rate, as appropriate, above the operating limit; and

b. Maintain the daily average scrubber effluent pH within the operating limits; or

c. Instead of a. and b., maintain your operating parameter(s) within the operating limits established according to your monitoring plan established under § 63.8(f).
2. Other type of control device to which HCl emissions are ductedMaintain your operating parameter(s) within the limits established during the performance test and according to your monitoring plan.

Table 3 to Subpart NNNNN of Part 63—Performance Test Requirements for HCl Production Affected Sources

As stated in § 63.9020, you must comply with the following requirements for performance tests for HCl production for each affected source.


For each HCl process vent and each HCl storage tank and HCl transfer operation for which you are conducting a performance test, you must . . .
Using . . .
Additional Information . . .
1. Select sampling port location(s) and the number of traverse pointsa. Method 1 or 1A in appendix A to 40 CFR part 60 of this chapteri. If complying with a percent reduction emission limitation, sampling sites must located at the inlet and outlet of the control device prior to any releases to the atmosphere (or, if a series of control devices are used, at the inlet of the first control device and at the outlet of the final control device prior to any releases to the atmosphere); or
ii. If complying with an outlet concentration emission limitation, the sampling site must be located at the outlet of the final control device and prior to any releases to the atmosphere or, if no control device is used, prior to any releases to the atmosphere.
2. Determine velocity and volumetric flow rateMethod 2, 2A, 2C, 2D, 2F, or 2G in appendix A to 40 CFR part 60 of this chapter.
3. Determine gas molecular weighta. Not applicablei. Assume a molecular weight of 29 (after moisture correction) for calculation purposes.
4. Measure moisture content of the stack gasMethod 4 in appendix A to 40 CFR part 60 of this chapter.
5. Measure HCl concentration and Cl2 concentration from HCl process ventsa. Method 26A in appendix A to 40 CFR part 60 of this chapteri. An owner or operator may be exempted from measuring the Cl2 concentration from an HCl process vent provided that a demonstration that Cl2 is not likely to be present in the stream is submitted as part of the site-specific test plan required by § 63.9020(a)(2). This demonstration may be based on process knowledge, engineering judgment, or previous test results.
6. Establish operating limits with which you will demonstrate continuous compliance with the emission limits in Table 1 to this subpart, in accordance with § 63.9020(e)(1) or (2).

[68 FR 19090, Apr. 17, 2003, as amended at 71 FR 17747, Apr. 7, 2006]


Table 4 to Subpart NNNNN of Part 63—Initial Compliance With Emission Limitations and Work Practice Standards

As stated in § 63.9030, you must comply with the following requirements to demonstrate initial compliance with the applicable emission limits for each affected source vented to a control device and each work practice standard.


For each . . .
For the following emission limit or work practice standard . . .
You have demonstrated initial compliance if . . .
1. HCl process vent and each HCl storage tank and HCl transfer operation for which you are conducting a performance testa. In Table 1 to this subparti. The average percent reduction of HCl and Cl2 (if applicable), measured over the period of the performance test conducted according to Table 3 of this subpart and determined in accordance with § 63.9020(b), is greater than or equal to the applicable percent reduction emission limitation specified in Table 1 of this subpart; or
ii. The average HCl and Cl2 (if applicable) concentration, measured over the period of the performance test conducted according to Table 3 of this subpart, is less than or equal to the applicable concentration emission limitation specified in Table 1 of this subpart.
2. HCl storage tank and HCl transfer operation for which you are preparing a design evaluation in lieu of conducting a performance testa. In Table 1 to this subparti. The percent reduction of HCl, demonstrated by a design evaluation prepared in accordance with § 63.9020(c), is greater than or equal to the applicable percent reduction emission limitation specified in Table 1 of this subpart; or
ii. The HCl concentration, demonstrated by a design evaluation prepared in accordance with § 63.9020(c), is less than or equal to the applicable concentration emission limitation specified in Table 1 of this subpart.
3. Leaking equipmenta. In Table 1 to this subparti. You certify in your Notification of Compliance Status that you have developed and implemented your LDAR plan and submitted it to the Administrator for comment only.

Table 5 to Subpart NNNNN of Part 63—Continuous Compliance With Emission Limitations and Work Practice Standards

As stated in § 63.9040, you must comply with the following requirements to demonstrate continuous compliance with the applicable emission limitations for each affected source vented to a control device and each work practice standard.


For each . . .
For the following emission limitation and work practice standard . . .
You must demonstrate continuous compliance by . . .
1. Affected source using a caustic scrubber or water scrubber/adsorbera. In Tables 1 and 2 to this subparti. Collecting the scrubber inlet liquid or recirculating liquid flow rate, as appropriate, and effluent pH monitoring data according to § 63.9025, consistent with your monitoring plan; and
ii. Reducing the data to 1-hour and daily block averages according to the requirements in § 63.9025; and
iii. Maintaining the daily average scrubber inlet liquid or recirculating liquid flow rate, as appropriate, above the operating limit; and
iv. Maintaining the daily average scrubber effluent pH within the operating limits.
2. Affected source using any other control devicea. In Tables 1 and 2 to this subparti. Conducting monitoring according to your monitoring plan established under § 63.8(f) in accordance with § 63.9025(c); and
ii. Collecting the parameter data according to your monitoring plan established under § 63.8(f); and
iii. Reducing the data to 1-hour and daily block averages according to the requirements in § 63.9025; and
iv. Maintaining the daily average parameter values within the operating limits established according to your monitoring plan established under § 63.8(f).
3. Affected source using no control devicea. In Tables 1 and 2 to this subpart.i. Verifying that you have not made any process changes that could reasonably be expected to change the outlet concentration since your most recent performance test for an emission point.
4. Leaking equipment affected sourcea. In Table 1 to this subparti. Verifying that you continue to use a LDAR plan; and
ii. Reporting any instances where you deviated from the plan and the corrective actions taken.

[68 FR 19090, Apr. 17, 2003, as amended at 71 FR 17747, Apr. 7, 2006]


Table 6 to Subpart NNNNN of Part 63—Requirements for Reports

As stated in § 63.9050(a), you must submit a compliance report that includes the information in § 63.9050(c) through (e) as well as the information in the following table. For existing sources and for new or reconstructed sources which commenced construction or reconstruction after April 17, 2003, but before February 5, 2019, before October 13, 2020, you must also submit startup, shutdown, and malfunction reports according to the requirements in § 63.9050(f) and the following table. A startup, shutdown, and malfunction plan is not required after October 13, 2020.


Table 6 to Subpart NNNNN of Part 63—Requirements for Reports

If . . .
Then you must submit a report or statement that:
1. There are no deviations from any emission limitations that apply to youThere were no deviations from any emission limitations that apply to you during the reporting period. Include this statement in the compliance report.
2. There were no periods during which the operating parameter monitoring systems were out-of-control in accordance with the monitoring planThere were no periods during which the CMS were out-of-control during the reporting period. Include this statement in the compliance report.
3. There was a deviation from any emission limitation during the reporting periodContains the information in § 63.9050(d). Include this statement in the compliance report.
4. There were periods during which the operating parameter monitoring systems were out-of-control in accordance with the monitoring planContains the information in § 63.9050(d). Include this statement in the compliance report.
5. There was a startup, shutdown, and malfunction during the reporting period that is not consistent with your startup, shutdown, and malfunction planFor existing sources and for new or reconstructed sources which commenced construction or reconstruction after April 17, 2003, but before February 5, 2019, before October 13, 2020, contains the information in § 63.9050(f). Include this statement in the compliance report. A startup, shutdown, and malfunction plan is not required after October 13, 2020.
6. There were periods when the procedures in the LDAR plan were not followedContains the information in § 63.9050(c)(7). Include this statement in the compliance report.

[85 FR 20870, Apr. 15, 2020]


Table 7 to Subpart NNNNN of Part 63—Applicability of General Provisions to Subpart NNNNN

As stated in § 63.9065, you must comply with the applicable General Provisions requirements according to the following:


Citation
Requirement
Applies to subpart NNNNN
Explanation
§ 63.1Initial applicability determination; applicability after standard established; permit requirements; extensions; notificationsYes.
§ 63.2DefinitionsYesAdditional definitions are found in § 63.9075.
§ 63.3Units and abbreviationsYes.
§ 63.4Prohibited activities; compliance date; circumvention, severabilityYes.
§ 63.5Construction/reconstruction applicability; applications; approvalsYes.
§ 63.6(a)Compliance with standards and maintenance requirements-applicabilityYes.
§ 63.6(b)(1)-(4)Compliance dates for new or reconstructed sourcesYes§ 63.8995 specifies compliance dates.
§ 63.6(b)(5)Notification if commenced construction or reconstruction after proposalYes.
§ 63.6(b)(6)[Reserved]Yes.
§ 63.6(b)(7)Compliance dates for new or reconstructed area sources that become majorYes§ 63.8995 specifies compliance dates.
§ 63.6(c)(1)-(2)Compliance dates for existing sourcesYes§ 63.8995 specifies compliance dates.
§ 63.6(c)(3)-(4)[Reserved]Yes.
§ 63.6(c)(5)Compliance dates for existing area sources that become majorYes§ 63.8995 specifies compliance dates.
§ 63.6(d)[Reserved]Yes.
§ 63.6(e)(1)(i)General Duty to minimize emissionsNo, for new or reconstructed sources which commenced construction or reconstruction after February 4, 2019. Yes, for all other affected sources before October 13, 2020, and No thereafterSubpart NNNNN requires affected units to meet emissions standards at all times. See § 63.9005(b) for general duty requirement.
§ 63.6(e)(1)(ii)Requirement to correct malfunctions ASAPNo, for new or reconstructed sources which commenced construction or reconstruction after February 4, 2019. Yes, for all other affected sources before October 13, 2020, and No thereafter
§ 63.6(e)(1)(iii)-(e)(2)Operation and maintenance requirementsYes
§ 63.6(e)(3)Startup, Shutdown, and Malfunction PlansNo, for new or reconstructed sources which commenced construction or reconstruction after February 4, 2019. Yes, for all other affected sources before October 13, 2020, and No thereafter
§ 63.6(f)(1)Compliance except during startup, shutdown, and malfunctionNo, for new or reconstructed sources which commenced construction or reconstruction after February 4, 2019. Yes, for all other affected sources before October 13, 2020, and No thereafter
§ 63.6(f)(2)-(3)Methods for determining complianceYes.
§ 63.6(g)Use of an alternative non-opacity emission standardYes.
§ 63.6(h)Compliance with opacity/visible emission standardsNoSubpart NNNNN does not specify opacity or visible emission standards.
§ 63.6(i)Extension of compliance with emission standardsYes.
§ 63.6(j)Presidential compliance exemptionYes.
§ 63.7(a)(1)-(2)Performance test datesYesExcept for existing affected sources as specified in § 63.9010(b).
§ 63.7(a)(3)Administrator’s Clean Air Act section 114 authority to require a performance testYes.
§ 63.7(b)Notification of performance test and reschedulingYes.
§ 63.7(c)Quality assurance program and site-specific test plansYes.
§ 63.7(d)Performance testing facilitiesYes.
§ 63.7(e)(1)Conditions for conducting performance testsNo, for new or reconstructed sources which commenced construction or reconstruction after February 4, 2019. Yes, for all other affected sources before October 13, 2020, and No thereafterSee § 63.9020(a) for performance testing requirements.
§ 63.7(f)Use of an alternative test methodYes.
§ 63.7(g)Performance test data analysis, recordkeeping, and reportingYes.
§ 63.7(h)Waiver of performance testsYes.
§ 63.8(a)(1)-(3)Applicability of monitoring requirementsYesAdditional monitoring requirements are found in § 63.9005(d) and 63.9035.
63.8(a)(4)Monitoring with flaresNoSubpart NNNNN does not refer directly or indirectly to § 63.11.
§ 63.8(b)Conduct of monitoring and procedures when there are multiple effluents and multiple monitoring systemsYes.
§ 63.8(c)(1)(i)General duty to minimize emissions and CMS operationNo, for new or reconstructed sources which commenced construction or reconstruction after February 4, 2019. Yes, for all other affected sources before October 13, 2020, and No thereafter
§ 63.8(c)(1)(ii)Continuous monitoring system O&MYesApplies as modified by § 63.9005(d).
§ 63.8(c)(1)(iii)Requirement to develop Startup, Shutdown, and Malfunction Plan for CMSNo, for new or reconstructed sources which commenced construction or reconstruction after February 4, 2019. Yes, for all other affected sources before October 13, 2020, and No thereafter
§ 63.8(c)(2)-(3)Continuous monitoring system O&MYesApplies as modified by § 63.9005(d)
§ 63.8(c)(4)Continuous monitoring system requirements during breakdown, out-of-control, repair, maintenance, and high-level calibration driftsYesApplies as modified by § 63.9005(d).
§ 63.8(c)(5)Continuous opacity monitoring system (COMS) minimum proceduresNoSubpart NNNNN does not have opacity or visible emission standards.
§ 63.8(c)(6)Zero and high level calibration checksYesApplies as modified by § 63.9005(d).
§ 63.8(c)(7)-(8)Out-of-control periods, including reportingYes.
§ 63.8(d)(1)-(2)Quality control program and CMS performance evaluationYesApplies as modified by § 63.9005(d).
§ 63.8(d)(3)Written procedures for CMSNo, for new or reconstructed sources which commenced construction or reconstruction after February 4, 2019. Yes, for all other affected sources before October 13, 2020, and No thereafterSee § 63.9005(d)(5) for written procedures for CMS.
§ 63.8(e)Performance evaluation of CMSYesApplies as modified by § 63.9005(d).
§ 63.8(f)(1)-(5)Use of an alternative monitoring methodYes.
§ 63.8(f)(6)Alternative to relative accuracy testNoOnly applies to sources that use continuous emissions monitoring systems (CEMS).
§ 63.8(g)Data reductionYesApplies as modified by § 63.9005(d).
§ 63.9(a)Notification requirements—applicabilityYes.
§ 63.9(b)Initial notificationsYesExcept § 63.9045(c) requires new or reconstructed affected sources to submit the application for construction or reconstruction required by § 63.9(b)(1)(iii) in lieu of the initial notification.
§ 63.9(c)Request for compliance extensionYes.
§ 63.9(d)Notification that a new source is subject to special compliance requirementsYes.
§ 63.9(e)Notification of performance testYes.
§ 63.9(f)Notification of visible emissions/opacity testNoSubpart NNNNN does not have opacity or visible emission standards.
§ 63.9(g)(1)Additional CMS notifications—date of CMS performance evaluationYes.
§ 63.9(g)(2)Use of COMS dataNoSubpart NNNNN does not require the use of COMS.
§ 63.9(g)(3)Alternative to relative accuracy testingNoApplies only to sources with CEMS.
§ 63.9(h)Notification of compliance statusYesExcept the submission date specified in § 63.9(h)(2)(ii) is superseded by the date specified in § 63.9045(f).
§ 63.9(i)Adjustment of submittal deadlinesYes.
§ 63.9(j)Change in previous informationYes.
§ 63.9(k)Electronic reporting proceduresYesOnly as specified in § 63.9(j).
§ 63.10(a)Recordkeeping/reporting applicabilityYes.
§ 63.10(b)(1)General recordkeeping requirementsYes§§ 63.9055 and 63.9060 specify additional recordkeeping requirements.
§ 63.10(b)(2)(i)-(ii)Records related to startup, shutdown, and malfunction periodsNo, for new or reconstructed sources which commenced construction or reconstruction after February 4, 2019. Yes, for all other affected sources before October 13, 2020, and No thereafterSee 63.9055 for recordkeeping of (1) date, time and duration; (2) listing of affected source or equipment, and an estimate of the quantity of each regulated pollutant emitted over the standard; and (3) actions to minimize emissions and correct the failure.
§ 63.10(b)(2)(iii)Maintenance RecordsYes
§ 63.10(b)(2)(iv)Actions taken to minimize emissions during startup, shutdown, and malfunctionNo, for new or reconstructed sources which commenced construction or reconstruction after February 4, 2019. Yes, for all other affected sources before October 13, 2020, and No thereafter
§ 63.10(b)(2)(v)Actions taken to minimize emissions during startup, shutdown, and malfunctionNo, for new or reconstructed sources which commenced construction or reconstruction after February 4, 2019. Yes, for all other affected sources before October 13, 2020, and No thereafter
§ 63.10(b)(2)(vi)Recordkeeping for CMS malfunctionsYes
§ 63.10(b)(2)(vii)-(xi)Records for performance tests and CMSYes
§ 63.10(b)(2)(xii)Records when under waiverYes.
§ 63.10(b)(2)(xiii)Records when using alternative to relative accuracy testNoApplies only to sources with CEMS.
§ 63.10(b)(2)(xiv)All documentation supporting initial notification and notification of compliance statusYes.
§ 63.10(b)(3)Recordkeeping requirements for applicability determinationsYes.
§ 63.10(c)(1)-(14)Additional recordkeeping requirements for sources with CMSYesApplies as modified by § 63.9005 (d).
§ 63.10(c)(15)Use of Startup, Shutdown, and Malfunction PlanNo, for new or reconstructed sources which commenced construction or reconstruction after February 4, 2019. Yes, for all other affected sources before October 13, 2020, and No thereafter
§ 63.10(d)(1)General reporting requirementsYes§ 63.9050 specifies additional reporting requirements.
§ 63.10(d)(2)Performance test resultsYes§ 63.9045(f) specifies submission date.
§ 63.10(d)(3)Opacity or visible emissions observationsNoSubpart NNNNN does not specify opacity or visible emission standards.
§ 63.10(d)(4)Progress reports for sources with compliance extensionsYes.
§ 63.10(d)(5)Startup, shutdown, and malfunction reportsNo, for new or reconstructed sources which commenced construction or reconstruction after February 4, 2019. Yes, for all other affected sources before October 13, 2020, and No thereafterSee § 63.9050(c)(5) for malfunction reporting requirements.
§ 63.10(e)(1)Additional CMS reports—generalYesApplies as modified by § 63.9005(d).
§ 63.10(e)(2)(i)Results of CMS performance evaluationsYesApplies as modified by § 63.9005(d).
§ 63.10(e)(2)Results of COMS performance evaluationsNoSubpart NNNNN does not require the use of COMS.
§ 63.10(e)(3)Excess emissions/CMS performance reportsYes.
§ 63.10(e)(4)Continuous opacity monitoring system data reportsNoSubpart NNNNN does not require the use of COMS.
§ 63.10(f)Recordkeeping/reporting waiverYes.
§ 63.11Control device requirements—applicabilityNoFacilities subject to subpart NNNNN do not use flares as control devices.
§ 63.12State authority and delegationsYes§ 63.9070 lists those sections of subparts NNNNN and A that are not delegated.
§ 63.13AddressesYes.
§ 63.14Incorporation by referenceYesSubpart NNNNN does not incorporate any material by reference.
§ 63.15Availability of information/confidentialityYes.

[68 FR 19090, Apr. 17, 2003, as amended at 71 FR 17748, Apr. 7, 2006; 85 FR 20871, Apr. 15, 2020; 85 FR 73916, Nov. 19, 2020]


Subpart OOOOO [Reserved]

Subpart PPPPP—National Emission Standards for Hazardous Air Pollutants for Engine Test Cells/Stands


Source:68 FR 28785, May 27, 2003, unless otherwise noted.

What This Subpart Covers

§ 63.9280 What is the purpose of subpart PPPPP?

This subpart PPPPP establishes national emission standards for hazardous air pollutants (NESHAP) for engine test cells/stands located at major sources of hazardous air pollutants (HAP) emissions. This subpart also establishes requirements to demonstrate initial and continuous compliance with the emission limitations contained in this NESHAP.


§ 63.9285 Am I subject to this subpart?

You are subject to this subpart if you own or operate an engine test cell/stand that is located at a major source of HAP emissions.


(a) An engine test cell/stand is any apparatus used for testing uninstalled stationary or uninstalled mobile (motive) engines.


(b) An uninstalled engine is an engine that is not installed in, or an integrated part of, the final product.


(c) A major source of HAP emissions is a plant site that emits or has the potential to emit any single HAP at a rate of 10 tons (9.07 megagrams) or more per year or any combination of HAP at a rate of 25 tons (22.68 megagrams) or more per year.


§ 63.9290 What parts of my plant does this subpart cover?

This subpart applies to each new, reconstructed, or existing affected source.


(a) Affected source. An affected source is the collection of all equipment and activities associated with engine test cells/stands used for testing uninstalled stationary or uninstalled mobile (motive) engines located at a major source of HAP emissions.


(1) Existing affected source. An affected source is existing if you commenced construction or reconstruction of the affected source on or before May 14, 2002. A change in ownership of an existing affected source does not make that affected source a new or reconstructed affected source.


(2) New affected source. An affected source is new if you commenced construction of the affected source after May 14, 2002.


(3) Reconstructed affected source. An affected source is reconstructed if you meet the definition of reconstruction in § 63.2 of subpart A of this part and reconstruction is commenced after May 14, 2002. Changes made to an existing affected source primarily for the purpose of complying with revisions to engine testing requirements under 40 CFR parts 80, 86, 89, 90, 91, or 92 are not considered a modification or reconstruction. In addition, passive measurement and control instrumentation and electronics are not included as part of any affected source reconstruction evaluation.


(b) Existing affected sources do not have to meet the requirements of this subpart and of subpart A of this part.


(c) Any portion of a new or reconstructed affected source located at a major source that is used exclusively for testing internal combustion engines with rated power of less than 25 horsepower (hp) (19 kilowatts(kW)) does not have to meet the requirements of this subpart and of subpart A of this part except for the initial notification requirements of § 63.9345(b).


(d) Any portion of a new or reconstructed affected source located at a major source that meets any of the criteria specified in paragraphs (d)(1) through (4) of this section does not have to meet the requirements of this subpart and of subpart A of this part.


(1) Any portion of the affected source used exclusively for testing combustion turbine engines.


(2) Any portion of the affected source used exclusively for testing rocket engines.


(3) Any portion of the affected source used in research and teaching activities at facilities that are not engaged in the development of engines or engine test services for commercial purposes.


(4) Any portion of the affected source operated to test or evaluate fuels (such as knock engines), transmissions, or electronics.


§ 63.9295 When do I have to comply with this subpart?

(a) Affected sources. (1) If you start up your new or reconstructed affected source before May 27, 2003, you must comply with the emission limitations in this subpart no later than May 27, 2003; except that the compliance date for the requirements promulgated at §§ 63.9295, 63.9305, 63.9340, 63.9350, 63.9355, 63.9375, and Table 7 of 40 CFR part 63, subpart PPPPP, revised on June 3, 2020 is December 1, 2020.


(2) If you start up your new or reconstructed affected source on or after May 27, 2003, you must comply with the emission limitations in this subpart upon startup; except that if the initial startup of your new or reconstructed affected source occurs after May 27, 2003, but on or before May 8, 2019, the compliance date for the requirements promulgated at §§ 63.9295, 63.9305, 63.9340, 63.9350, 63.9355, 63.9375, and Table 7 of this subpart as revised on June 3, 2020 is December 1, 2020.


(3) If the initial startup of your new or reconstructed affected source occurs after May 8, 2019, the compliance date is June 3, 2020 or the date of startup, whichever is later.


(b) Area sources that become major sources. If your new or reconstructed affected source is located at an area source that increases its emissions or its potential to emit such that it becomes a major source of HAP, your new or reconstructed affected source must be in compliance with this subpart when the area source becomes a major source.


(c) You must meet the notification requirements in § 63.9345 and in 40 CFR part 63, subpart A.


[68 FR 28785, May 27, 2003, as amended at 85 FR 34345, June 3, 2020]


Emission Limitations

§ 63.9300 What emission limitations must I meet?

For each new or reconstructed affected source that is used in whole or in part for testing internal combustion engines with rated power of 25 hp (19 kW) or more and that is located at a major source, you must comply with the emission limitations in Table 1 to this subpart. (Tables are found at the end of this subpart.)


§ 63.9301 What are my options for meeting the emission limits?

You may use either a continuous parameter monitoring system (CPMS) or a continuous emission monitoring system (CEMS) to demonstrate compliance with the emission limitations. Continuous monitoring systems must meet the requirements in § 63.9306 (CPMS) and § 63.9307 (CEMS).


§ 63.9302 What operating limits must I meet?

(a) For any new or reconstructed affected source on which you use add-on controls, you must meet the operating limits specified in Table 2 to this subpart. These operating limits must be established during the performance test according to the requirements in § 63.9324. You must meet the operating limits at all times after you establish them.


(b) If you use an add-on control device other than those listed in Table 2 to this subpart, or wish to monitor an alternative parameter and comply with a different operating limit, you must apply to the Administrator for approval of alternative monitoring under § 63.8(f).


General Compliane Requirements

§ 63.9305 What are my general requirements for complying with this subpart?

(a) Prior to December 1, 2020, you must be in compliance with the emission limitation that applies to you at all times, except during periods of startup, shutdown, or malfunction (SSM) of your control device or associated monitoring equipment. On and after December 1, 2020, you must be in compliance with the applicable emission limitation at all times.


(b) If you must comply with the emission limitation, you must operate and maintain your engine test cell/stand, air pollution control equipment, and monitoring equipment in a manner consistent with safety and good air pollution control practices for minimizing emissions at all times. The general duty to minimize emissions does not require the owner or operator to make any further efforts to reduce emissions if levels required by the applicable standard have been achieved. Determination of whether a source is operating in compliance with operation and maintenance requirements will be based on information available to the Administrator that may include, but is not limited to, monitoring results, review of operation and maintenance procedures, review of operation and maintenance records, and inspection of the affected source.


(c) For affected sources prior to December 1, 2020, you must develop a written SSM plan (SSMP) for emission control devices and associated monitoring equipment according to the provisions in § 63.6(e)(3). The plan will apply only to emission control devices, and not to engine test cells/stands.


[85 FR 34345, June 3, 2020]


§ 63.9306 What are my continuous parameter monitoring system (CPMS) installation, operation, and maintenance requirements?

(a) General. You must install, operate, and maintain each CPMS specified in paragraphs (c) and (d) of this section according to paragraphs (a)(1) through (7) of this section. You must install, operate, and maintain each CPMS specified in paragraph (b) of this section according to paragraphs (a)(3) through (5) of this section.


(1) The CPMS must complete a minimum of one cycle of operation for each successive 15-minute period. You must have a minimum of four equally spaced successive cycles of CPMS operation in 1 hour.


(2) You must determine the average of all recorded readings for each successive 3-hour period of the emission capture system and add-on control device operation.


(3) You must record the results of each inspection, calibration, and validation check of the CPMS.


(4) You must maintain the CPMS at all times and have available necessary parts for routine repairs of the monitoring equipment.


(5) You must operate the CPMS and collect emission capture system and add-on control device parameter data at all times that an engine test cell/stand is operating, except during monitoring malfunctions, associated repairs, and required quality assurance or control activities (including, if applicable, calibration checks and required zero and span adjustments).


(6) You must not use emission capture system or add-on control device parameter data recorded during monitoring malfunctions, associated repairs, out-of-control periods, or required quality assurance or control activities when calculating data averages. You must use all the data collected during all other periods in calculating the data averages for determining compliance with the emission capture system and add-on control device operating limits.


(7) A monitoring malfunction is any sudden, infrequent, not reasonably preventable failure of the CPMS to provide valid data. Monitoring failures that are caused in part by poor maintenance or careless operation are not malfunctions. Any period for which the monitoring system is out-of-control and data are not available for required calculations is a deviation from the monitoring requirements.


(b) Capture system bypass line. You must meet the requirements of paragraphs (b)(1) and (2) of this section for each emission capture system that contains bypass lines that could divert emissions away from the add-on control device to the atmosphere.


(1) You must monitor or secure the valve or closure mechanism controlling the bypass line in a nondiverting position in such a way that the valve or closure mechanism cannot be opened without creating a record that the valve was opened. The method used to monitor or secure the valve or closure mechanism must meet one of the requirements specified in paragraphs (b)(1)(i) through (iv) of this section.


(i) Flow control position indicator. Install, calibrate, maintain, and operate according to the manufacturer’s specifications a flow control position indicator that takes a reading at least once every 15 minutes and provides a record indicating whether the emissions are directed to the add-on control device or diverted from the add-on control device. The time of occurrence and flow control position must be recorded, as well as every time the flow direction is changed. The flow control position indicator must be installed at the entrance to any bypass line that could divert the emissions away from the add-on control device to the atmosphere.


(ii) Car-seal or lock-and-key valve closures. Secure any bypass line valve in the closed position with a car-seal or a lock-and-key type configuration. You must visually inspect the seal or closure mechanism at least once every month to ensure that the valve is maintained in the closed position, and the emissions are not diverted away from the add-on control device to the atmosphere.


(iii) Valve closure monitoring. Ensure that any bypass line valve is in the closed (nondiverting) position through monitoring of valve position at least once every 15 minutes. You must inspect the monitoring system at least once every month to verify that the monitor will indicate valve position.


(iv) Automatic shutdown system. Use an automatic shutdown system in which the engine testing operation is stopped when flow is diverted by the bypass line away from the add-on control device to the atmosphere when an engine test cell/stand is operating. You must inspect the automatic shutdown system at least once every month to verify that it will detect diversions of flow and shut down the engine test cell/stand in operation.


(2) If any bypass line is opened, you must include a description of why the bypass line was opened and the length of time it remained open in the semiannual compliance reports required in § 63.9350.


(c) Thermal oxidizers and catalytic oxidizers. If you are using a thermal oxidizer or catalytic oxidizer as an add-on control device, you must comply with the requirements in paragraphs (c)(1) through (3) of this section.


(1) For a thermal oxidizer, install a gas temperature monitor in the firebox of the thermal oxidizer or in the duct immediately downstream of the firebox before any substantial heat exchange occurs.


(2) For a catalytic oxidizer, you must install a gas temperature monitor in the gas stream immediately before the catalyst bed, and if you established operating limits according to § 63.9324(b)(1) and (2), also install a gas temperature monitor in the gas stream immediately after the catalyst bed.


(i) If you establish operating limits according to § 63.9324(b)(1) and (2), then you must install the gas temperature monitors both upstream and downstream of the catalyst bed. The temperature monitors must be in the gas stream immediately before and after the catalyst bed to measure the temperature difference across the bed.


(ii) If you establish operating limits according to § 63.9324(b)(3) and (4), then you must install a gas temperature monitor upstream of the catalyst bed. The temperature monitor must be in the gas stream immediately before the catalyst bed to measure the temperature.


(3) For all thermal oxidizers and catalytic oxidizers, you must meet the requirements in paragraphs (a) and (c)(3)(i) through (vii) of this section for each gas temperature monitoring device.


(i) Locate the temperature sensor in a position that provides a representative temperature.


(ii) Use a temperature sensor with a measurement sensitivity of 4 degrees Fahrenheit or 0.75 percent of the temperature value, whichever is larger.


(iii) Shield the temperature sensor system from electromagnetic interference and chemical contaminants.


(iv) If a gas temperature chart recorder is used, it must have a measurement sensitivity in the minor division of at least 20 degrees Fahrenheit.


(v) Perform an electronic calibration at least semiannually according to the procedures in the manufacturer’s owner’s manual. Following the electronic calibration, you must conduct a temperature sensor validation check in which a second or redundant temperature sensor placed near the process temperature sensor must yield a reading within 30 degrees Fahrenheit of the process temperature sensor reading.


(vi) Conduct calibration and validation checks anytime the sensor exceeds the manufacturer’s specified maximum operating temperature range or install a new temperature sensor.


(vii) At least monthly, inspect components for integrity and electrical connections for continuity, oxidation, and galvanic corrosion.


(d) Emission capture systems. The capture system monitoring system must comply with the applicable requirements in paragraphs (d)(1) and (2) of this section.


(1) For each flow measurement device, you must meet the requirements in paragraphs (a) and (d)(1)(i) through (iv) of this section.


(i) Locate a flow sensor in a position that provides a representative flow measurement in the duct from each capture device in the emission capture system to the add-on control device.


(ii) Reduce swirling flow or abnormal velocity distributions due to upstream and downstream disturbances.


(iii) Conduct a flow sensor calibration check at least semiannually.


(iv) At least monthly, inspect components for integrity, electrical connections for continuity, and mechanical connections for leakage.


(2) For each pressure drop measurement device, you must comply with the requirements in paragraphs (a) and (d)(2)(i) through (vi) of this section.


(i) Locate the pressure sensor(s) in or as close to a position that provides a representative measurement of the pressure drop across each opening you are monitoring.


(ii) Minimize or eliminate pulsating pressure, vibration, and internal and external corrosion.


(iii) Check pressure tap pluggage daily.


(iv) Using a pressure sensor with measurement sensitivity of 0.002 inch water, check gauge calibration quarterly and transducer calibration monthly.


(v) Conduct calibration checks any time the sensor exceeds the manufacturer’s specified maximum operating pressure range or install a new pressure sensor.


(vi) At least monthly, inspect components for integrity, electrical connections for continuity, and mechanical connections for leakage.


[68 FR 28785, May 27, 2003, as amended at 88 FR 18415, Mar, 29, 2023]


§ 63.9307 What are my continuous emissions monitoring system installation, operation, and maintenance requirements?

(a) You must install, operate, and maintain each CEMS to monitor carbon monoxide (CO) or total hydrocarbons (THC) and oxygen (O2) at the outlet of the exhaust system of the engine test cell/stand or at the outlet of the emission control device.


(b) To comply with the CO or THC percent reduction emission limitation, you may install, operate, and maintain a CEMS to monitor CO or THC and O2 at both the inlet and the outlet of the emission control device.


(c) To comply with either emission limitations, the CEMS must be installed and operated according to the requirements described in paragraphs (c)(1) through (4) of this section.


(1) You must install, operate, and maintain each CEMS according to the applicable Performance Specification (PS) of 40 CFR part 60, appendix B (PS- 3, PS-4A, or PS-8).


(2) You must conduct a performance evaluation of each CEMS according to the requirements in 40 CFR 63.8 and according to PS-3 of 40 CFR part 60, appendix B, using Reference Method 3A or 3B for the O2 CEMS, and according to PS-4A of 40 CFR part 60, appendix B, using Reference Method 10 or 10B for the CO CEMS, and according to PS-8 of CFR part 60, appendix B, using Reference Method 25A for the THC CEMS. If the fuel used in the engines being tested is natural gas, you may use ASTM D 6522-00, Standard Test Method for Determination of Nitrogen Oxides, Carbon Monoxide and Oxygen Concentrations in Emissions from Natural Gas Fired Reciprocating Engines, Combustion Turbines, Boilers, and Process Heaters Using Portable Analyzers (incorporated by reference, see § 63.14). As an alternative to Method 3B, you may use ANSI/ASME PTC 19.10-1981, “Flue and Exhaust Gas Analyses [Part 10, Instruments and Apparatus],” (incorporated by reference, see § 63.14).


(3) As specified in § 63.8(c)(4)(ii), each CEMS must complete a minimum of one cycle of operation (sampling, analyzing, and data recording) for each successive 15-minute period. You must have at least two data points, each representing a different 15-minute period within the same hour, to have a valid hour of data.


(4) All CEMS data must be reduced as specified in § 63.8(g)(2) and recorded as CO or THC as carbon concentration in parts per million by volume, dry basis (ppmvd), corrected to 15 percent O2 content.


(d) If you have CEMS that are subject to paragraph (a) or (b) of this section, you must properly maintain and operate the monitors continuously according to the requirements described in paragraphs (d)(1) and (2) of this section.


(1) Proper maintenance. You must maintain the monitoring equipment at all times that the engine test cell/stand is operating, including but not limited to, maintaining necessary parts for routine repairs of the monitoring equipment.


(2) Continued operation. You must operate your CEMS according to paragraphs (d)(2)(i) and (ii) of this section.


(i) You must conduct all monitoring in continuous operation at all times that the engine test cell/stand is operating, except for, as applicable, monitoring malfunctions, associated repairs, and required quality assurance or control activities (including, as applicable, calibration drift checks and required zero and high-level adjustments). Quality assurance or control activities must be performed according to procedure 1 of 40 CFR part 60, appendix F.


(ii) Data recorded during monitoring malfunctions, associated repairs, out-of-control periods, and required quality assurance or control activities must not be used for purposes of calculating data averages. You must use all of the data collected from all other periods in assessing compliance. A monitoring malfunction is any sudden, infrequent, not reasonably preventable failure of the monitoring equipment to provide valid data. Monitoring failures that are caused in part by poor maintenance or careless operation are not malfunctions. Any period for which the monitoring system is out-of-control and data are not available for required calculations constitutes a deviation from the monitoring requirements.


[68 FR 28785, May 27, 2003, as amended at 85 FR 34345, June 3, 2020]


Testing and Initial Compliance Requirements

§ 63.9310 By what date must I conduct the initial compliance demonstrations?

You must conduct the initial compliance demonstrations that apply to you in Table 3 to this subpart within 180 calendar days after the compliance date that is specified for your new or reconstructed affected source in § 63.9295 and according to the provisions in § 63.7(a)(2).


§ 63.9320 What procedures must I use?

(a) You must conduct each initial compliance demonstration that applies to you in Table 3 to this subpart.


(b) You must conduct an initial performance evaluation of each capture and control system according to §§ 63.9321, 63.9322, 63.9323 and 63.9324, and each CEMS according to the requirements in 40 CFR 63.8 and according to the applicable Performance Specification of 40 CFR part 60, appendix B (PS-3, PS-4A, or PS-8).


(c) The initial demonstration of compliance with the carbon monoxide (CO) or THC concentration limitation consists of either the first 4-hour rolling average CO or THC concentration recorded after completion of the CEMS performance evaluation if CEMS are installed or the average of the test run averages during the initial performance test. You must correct the CO or THC concentration at the outlet of the engine test cell/stand or the emission control device to a dry basis and to 15 percent O2 content according to Equation 1 of this section:




Where:

Cc = concentration of CO or THC, corrected to 15 percent oxygen, ppmvd

Cunc = total uncorrected concentration of CO or THC, ppmvd

%O2d = concentration of oxygen measured in gas stream, dry basis, percent by volume

(d) The initial demonstration of compliance with the CO or THC percent reduction emission limitation consists of the first 4-hour rolling average percent reduction in CO or THC recorded after completion of the performance evaluation of the capture/control system and/or CEMS. You must complete the actions described in paragraphs (d)(1) through (2) of this section.


(1) Correct the CO or THC concentrations at the inlet and outlet of the emission control device to a dry basis and to 15 percent O2 content using Equation 1 of this section.


(2) Calculate the percent reduction in CO or THC using Equation 2 of this section:





Where:

R = percent reduction in CO or THC

Ci = corrected CO or THC concentration at inlet of the emission control device

Co = corrected CO or THC concentration at the outlet of the emission control device.

[68 FR 28785, May 27, 2003, as amended at 85 FR 34346, June 3, 2020]


§ 63.9321 What are the general requirements for performance tests?

(a) You must conduct each performance test required by § 63.9310 under the conditions in this section unless you obtain a waiver of the performance test according to the provisions in § 63.7(h). Prior to December 1, 2020, the performance test must also be conducted according to the requirements in § 63.7(e)(1).


(1) Representative engine testing conditions. You must conduct the performance test under representative operating conditions for the test cell/stand. Operations during periods of SSM, and during periods of nonoperation do not constitute representative conditions. You must record the process information that is necessary to document operating conditions during the test and explain why the conditions represent normal operation.


(2) Representative emission capture system and add-on control device operating conditions. You must conduct the performance test when the emission capture system and add-on control device are operating at a representative flow rate, and the add-on control device is operating at a representative inlet concentration. You must record information that is necessary to document emission capture system and add-on control device operating conditions during the test and explain why the conditions represent normal operation.


(b) You must conduct each performance test of an emission capture system according to the requirements in § 63.9322. You must conduct each performance test of an add-on control device according to the requirements in § 63.9323.


[68 FR 28785, May 27, 2003, as amended at 85 FR 34346, June 3, 2020]


§ 63.9322 How do I determine the emission capture system efficiency?

You must use the procedures and test methods in this section to determine capture efficiency as part of the performance test required by § 63.9310.


(a) Assuming 100 percent capture efficiency. You may assume the capture system efficiency is 100 percent if both conditions in paragraphs (a)(1) and (2) of this section are met:


(1) The capture system meets the criteria in method 204 of appendix M to 40 CFR part 51 for a permanent total enclosure (PE) and directs all the exhaust gases from the enclosure to an add-on control device.


(2) All engine test operations creating exhaust gases for which the test is applicable are conducted within the capture system.


(b) Measuring capture efficiency. If the capture system does not meet the criteria in paragraphs (a)(1) and (2) of this section, then you must use one of the two protocols described in paragraphs (c) and (d) of this section to measure capture efficiency. The capture efficiency measurements use total volatile hydrocarbon (TVH) capture efficiency as a surrogate for organic HAP capture efficiency. For the protocol in paragraph (c) of this section, the capture efficiency measurement must consist of three test runs. Each test run must be at least 3 hours in duration or the length of a production run, whichever is longer, up to 8 hours. For the purposes of this test, a production run means the time required for a single engine test to go from the beginning to the end.


(c) Gas-to-gas protocol using a temporary total enclosure or a building enclosure. The gas-to-gas protocol compares the mass of TVH emissions captured by the emission capture system to the mass of TVH emissions not captured. Use a temporary total enclosure or a building enclosure and the procedures in paragraphs (c)(1) through (5) of this section to measure emission capture system efficiency using the gas-to-gas protocol.


(1) Either use a building enclosure or construct an enclosure around the engine test cell/stand and all areas where emissions from the engine testing subsequently occur. The enclosure must meet the applicable definition of a temporary total enclosure or building enclosure in Method 204 of appendix M to 40 CFR part 51.


(2) Use Method 204B or 204C of appendix M to 40 CFR part 51 to measure the total mass, kg, of TVH emissions captured by the emission capture system during each capture efficiency test run as measured at the inlet to the add-on control device. To make the measurement, substitute TVH for each occurrence of the term VOC in the methods.


(i) The sampling points for the Method 204B or 204C of appendix M to 40 CFR part 51 measurement must be upstream from the add-on control device and must represent total emissions routed from the capture system and entering the add-on control device.


(ii) If multiple emission streams from the capture system enter the add-on control device without a single common duct, then the emissions entering the add-on control device must be simultaneously measured in each duct, and the total emissions entering the add-on control device must be determined.


(3) Use Method 204D or 204E of appendix M to 40 CFR part 51 to measure the total mass, kg, of TVH emissions that are not captured by the emission capture system; they are measured as they exit the temporary total enclosure or building enclosure during each capture efficiency test run. To make the measurement, substitute TVH for each occurrence of the term VOC in the methods.


(i) Use Method 204D of appendix M to 40 CFR part 51 if the enclosure is a temporary total enclosure.


(ii) Use Method 204E of appendix M to 40 CFR part 51 if the enclosure is a building enclosure. During the capture efficiency measurement, all organic compound emitting operations inside the building enclosure, other than the engine test cell/stand operation for which capture efficiency is being determined, must be shut down, but all fans and blowers must be operating normally.


(4) For each capture efficiency test run, determine the percent capture efficiency of the emission capture system using Equation 1 of this section:





Where:

CE = capture efficiency of the emission capture system vented to the add-on control device, percent

TVHcaptured = total mass of TVH captured by the emission capture system as measured at the inlet to the add-on control device during the emission capture efficiency test run, kg, determined according to paragraph (c)(2) of this section

TVHuncaptured = total mass of TVH that is not captured by the emission capture system and that exits from the temporary total enclosure or building enclosure during the capture efficiency test run, kg, determined according to paragraph (c)(3) of this section.

(5) Determine the capture efficiency the emission capture system as the average of the capture efficiencies measured in the three test runs.


(d) Alternative capture efficiency protocol. As an alternative to the procedure specified in paragraph (c) of this section, you may determine capture efficiency using any other capture efficiency protocol and test methods that satisfy the criteria of either the data quality objective or lower control limit approach as described in appendix A to subpart KK of this part.


[68 FR 28785, May 27, 2003, as amended at 88 FR 18415, Mar. 29, 2023]


§ 63.9323 How do I determine the add-on control device emission destruction or removal efficiency?

You must use the procedures and test methods in this section to determine the add-on control device emission destruction or removal efficiency as part of the performance test required by § 63.9310. You must conduct three test runs as specified in § 63.7(e)(3), and each test run must last at least 1 hour.


(a) For all types of add-on control devices, use the test methods specified in paragraphs (a)(1) through (5) of this section.


(1) Use Method 1 or 1A of appendix A to 40 CFR part 60, as appropriate, to select sampling sites and velocity traverse points.


(2) Use Method 2, 2A, 2C, 2D, 2F, or 2G of appendix A to 40 CFR part 60, as appropriate, to measure gas volumetric flow rate.


(3) Use Method 3, 3A, or 3B of appendix A to 40 CFR part 60, as appropriate, for gas analysis to determine dry molecular weight. The ANSI/ASME PTC 19.10-1981 Part 10 is an acceptable alternative to Method 3B (incorporated by reference, see § 63.14).


(4) Use Method 4 of appendix A to 40 CFR part 60, to determine stack gas moisture.


(5) Methods for determining gas volumetric flow rate, dry molecular weight, and stack gas moisture must be performed, as applicable, during each test run.


(b) Measure total gaseous organic mass emissions as carbon at the inlet and outlet of the add-on control device simultaneously, using either Method 25 or 25A of appendix A to 40 CFR part 60, as specified in paragraphs (b)(1) through (3) of this section. You must use the same method for both the inlet and outlet measurements.


(1) Use Method 25 of appendix A to 40 CFR part 60 if the add-on control device is an oxidizer, and you expect the total gaseous organic concentration as carbon to be more than 50 parts per million at the control device outlet.


(2) Use Method 25A of appendix A to 40 CFR part 60 if the add-on control device is an oxidizer, and you expect the total gaseous organic concentration as carbon to be 50 ppm or less at the control device outlet.


(c) For each test run, determine the total gaseous organic emissions mass flow rates for the inlet and the outlet of the add-on control device, using Equation 1 of this section. If there is more than one inlet or outlet to the add-on control device, you must calculate the total gaseous organic mass flow rate using Equation 1 of this section for each inlet and each outlet and then total all of the inlet emissions and total all of the outlet emissions.





Where:

Mf = total gaseous organic emissions mass flow rate, kg/hour (kg/h)

Cc = concentration of organic compounds as carbon in the vent gas, as determined by Method 25 or Method 25A, parts per million by volume (ppmv), dry basis

Qsd = volumetric flow rate of gases entering or exiting the add-on control device, as determined by Method 2, 2A, 2C, 2D, 2F, or 2G, dry standard cubic meters/hour (dscm/h)

0.0416 = conversion factor for molar volume, kg-moles per cubic meter (mol/m
3) (@ 293 Kelvin [K] and 760 millimeters of mercury [mmHg]).

(d) For each test run, determine the add-on control device organic emissions destruction or removal efficiency, using Equation 2 of this section:





Where:

DRE = organic emissions destruction or removal efficiency of the add-on control device, percent

Mfi = total gaseous organic emissions mass flow rate at the inlet(s) to the add-on control device, using Equation 1 of this section, kg/h

Mfo = total gaseous organic emissions mass flow rate at the outlet(s) of the add-on control device, using Equation 1 of this section, kg/h.

(e) Determine the emission destruction or removal efficiency of the add-on control device as the average of the efficiencies determined in the three test runs and calculated in Equation 2 of this section.


§ 63.9324 How do I establish the emission capture system and add-on control device operating limits during the performance test?

During the performance test required by § 63.9310, you must establish the operating limits required by § 63.9302 according to this section, unless you have received approval for alternative monitoring and operating limits under § 63.8(f) as specified in § 63.9302.


(a) Thermal oxidizers. If your add-on control device is a thermal oxidizer, establish the operating limits according to paragraphs (a)(1) and (2) of this section.


(1) During the performance test, you must monitor and record the combustion temperature at least once every 15 minutes during each of the three test runs. You must monitor the temperature in the firebox of the thermal oxidizer or immediately downstream of the firebox before any substantial heat exchange occurs.


(2) Use the data collected during the performance test to calculate and record the average combustion temperature maintained during the performance test. This average combustion temperature is the minimum operating limit for your thermal oxidizer.


(b) Catalytic oxidizers. If your add-on control device is a catalytic oxidizer, establish the operating limits according to either paragraphs (b)(1) and (2) or paragraphs (b)(3) and (4) of this section.


(1) During the performance test, you must monitor and record the temperature just before the catalyst bed and the temperature difference across the catalyst bed at least once every 15 minutes during each of the three test runs.


(2) Use the data collected during the performance test to calculate and record the average temperature just before the catalyst bed and the average temperature difference across the catalyst bed maintained during the performance test. These are the minimum operating limits for your catalytic oxidizer.


(3) As an alternative to monitoring the temperature difference across the catalyst bed, you may monitor the temperature at the inlet to the catalyst bed and implement a site-specific inspection and maintenance plan for your catalytic oxidizer as specified in paragraph (b)(4) of this section. During the performance test, you must monitor and record the temperature just before the catalyst bed at least once every 15 minutes during each of the three test runs. Use the data collected during the performance test to calculate and record the average temperature just before the catalyst bed during the performance test. This is the minimum operating limit for your catalytic oxidizer.


(4) You must develop and implement an inspection and maintenance plan for your catalytic oxidizer(s) for which you elect to monitor according to paragraph (b)(3) of this section. The plan must address, at a minimum, the elements specified in paragraphs (b)(4)(i) through (iii) of this section.


(i) Annual sampling and analysis of the catalyst activity (i.e., conversion efficiency) following the manufacturer’s or catalyst supplier’s recommended procedures.


(ii) Monthly inspection of the oxidizer system, including the burner assembly and fuel supply lines for problems and, as necessary, adjust the equipment to assure proper air-to-fuel mixtures.


(iii) Annual internal and monthly external visual inspection of the catalyst bed to check for channeling, abrasion, and settling. If problems are found, you must take corrective action consistent with the manufacturer’s recommendation and conduct a new performance test to determine destruction efficiency according to § 63.9323.


(c) Emission capture system. For each capture device that is not part of a PTE that meets the criteria of § 63.9322(a), establish an operating limit for either the gas volumetric flow rate or duct static pressure, as specified in paragraphs (c)(1) and (2) of this section. The operating limit for a PTE is specified in Table 3 to this subpart.


(1) During the capture efficiency determination required by § 63.9310, you must monitor and record either the gas volumetric flow rate or the duct static pressure for each separate capture device in your emission capture system at least once every 15 minutes during each of the three test runs at a point in the duct between the capture device and the add-on control device inlet.


(2) Calculate and record the average gas volumetric flow rate or duct static pressure for the three test runs for each capture device. This average gas volumetric flow rate or duct static pressure is the minimum operating limit for that specific capture device.


§ 63.9330 How do I demonstrate initial compliance with the emission limitation?

(a) You must demonstrate initial compliance with the emission limitation that applies to you according to Table 4 to this subpart.


(b) You must submit the Notification of Compliance Status containing results of the initial compliance demonstration according to the requirements in § 63.9345(c).


[68 FR 28785, May 27, 2003, as amended at 85 FR 34346, June 3, 2020]


Continuous Compliance Requirements

§ 63.9335 How do I monitor and collect data to demonstrate continuous compliance?

(a) Except for monitor malfunctions, associated repairs, and required quality assurance or quality control activities (including, as applicable, calibration drift checks and required zero and high-level adjustments of the monitoring system), you must conduct all monitoring in continuous operation at all times the engine test cell/stand is operating.


(b) Do not use data recorded during monitor malfunctions, associated repairs, and required quality assurance or quality control activities for meeting the requirements of this subpart, including data averages and calculations. You must use all the data collected during all other periods in assessing the performance of the emission control device or in assessing emissions from the new or reconstructed affected source.


§ 63.9340 How do I demonstrate continuous compliance with the emission limitations?

(a) You must demonstrate continuous compliance with the emission limitation in Table 1 to this subpart that applies to you according to methods specified in Table 5 to this subpart.


(b) You must report each instance in paragraphs (b)(1) and (2) of this section. These instances are deviations from the emission limitation in this subpart and must be reported according to the requirements in § 63.9350.


(1) You must report each instance in which you did not meet the emission limitation that applies to you.


(2) You must report each instance in which you did not meet the requirements in Table 7 to this subpart that apply to you.


(c) Startups, shutdowns, and malfunctions:


(1) For affected sources prior to December 1, 2020, consistent with §§ 63.6(e) and 63.7(e)(1), deviations that occur during a period of SSM of control devices and associated monitoring equipment are not violations if you demonstrate to the Administrator’s satisfaction that you were operating in accordance with § 63.6(e)(1).


(2) The Administrator will determine whether deviations that occur during a period you identify as an SSM of control devices and associated monitoring equipment are violations, according to the provisions in § 63.6(e).


[68 FR 28785, May 27, 2003, as amended at 71 FR 20470, Apr. 20, 2006; 85 FR 34346, June 3, 2020]


Notifications, Reports, and Records

§ 63.9345 What notifications must I submit and when?

(a) You must submit all of the notifications in §§ 63.8(e), 63.8(f)(4) and (6), and 63.9(b), (g)(1), (g)(2) and (h) that apply to you by the dates specified.


(b) If you own or operate a new or reconstructed test cell/stand used for testing internal combustion engines, you are required to submit an Initial Notification as specified in paragraphs (b)(1) through (3) of this section.


(1) As specified in § 63.9(b)(2), if you start up your new or reconstructed affected source before the effective date of this subpart, you must submit an Initial Notification not later than 120 calendar days after May 27, 2003, or no later than 120 days after the source becomes subject to this subpart, whichever is later.


(2) As specified in § 63.9(b), if you start up your new or reconstructed affected source on or after the effective date of this subpart, you must submit an Initial Notification not later than 120 calendar days after you become subject to this subpart.


(3) If you are required to submit an Initial Notification but are otherwise not affected by the requirements of this subpart, in accordance with § 63.9290(c), your notification should include the information in § 63.9(b)(2)(i) through (v) and a statement that your new or reconstructed engine test cell/stand has no additional requirements and explain the basis of the exclusion (for example, that the test cell/stand is used exclusively for testing internal combustion engines with rated power of less than 25 hp (19 kW)).


(c) If you are required to comply with the emission limitations in Table 1 to this subpart, you must submit a Notification of Compliance Status according to § 63.9(h)(2)(ii). For each initial compliance demonstration with the emission limitation, you must submit the Notification of Compliance Status before the close of business on the 30th calendar day following the completion of the initial compliance demonstration.


(d) You must submit a notification of initial performance evaluation of your CEMS or performance testing of your control device at least 60 calendar days before the performance testing/evaluation is scheduled to begin as required in § 63.8(e)(2).


[68 FR 28785, May 27, 2003, as amended 85 FR 73916, Nov. 19, 2020]


§ 63.9350 What reports must I submit and when?

(a) If you own or operate a new or reconstructed affected source that must meet the emission limitation, you must submit a semiannual compliance report according to Table 6 to this subpart by the applicable dates specified in paragraphs (a)(1) through (6) of this section, unless the Administrator has approved a different schedule.


(1) The first semiannual compliance report must cover the period beginning on the compliance date specified in § 63.9295 and ending on June 30 or December 31, whichever date is the first date following the end of the first calendar half after the compliance date specified in § 63.9295.


(2) The first semiannual compliance report must be postmarked or delivered no later than July 31 or January 31, whichever date follows the end of the first calendar half after the compliance date that is specified in § 63.9295.


(3) Each subsequent semiannual compliance report must cover the semiannual reporting period from January 1 through June 30 or the semiannual reporting period from July 1 through December 31.


(4) Each subsequent semiannual compliance report must be postmarked or delivered no later than July 31 or January 31, whichever date is the first date following the end of the semiannual reporting period.


(5) For each new or reconstructed engine test cell/stand that is subject to permitting regulations pursuant to 40 CFR part 70 or 71, and if the permitting authority has established the date for submitting semiannual reports pursuant to 40 CFR 70.6(a)(3)(iii)(A) or 40 CFR 71.6(a)(3)(iii)(A), you may submit the first and subsequent compliance reports according to the dates the permitting authority has established instead of according to the dates in paragraphs (a)(1) through (4) of this section.


(6) For affected sources prior to December 1, 2020, if you had an SSM of a control device or associated monitoring equipment during the reporting period and you took actions consistent with your SSMP, the compliance report must include the information in paragraphs § 63.10(d)(5)(i).


(7) Beginning on December 1, 2020, submit all semiannual compliance reports following the procedure specified in paragraph (g) of this section.


(b) If there is no deviation from the applicable emission limitation and the CEMS or CPMS was not out-of-control, according to § 63.8(c)(7), the semiannual compliance report must contain the information described in paragraphs (b)(1) through (4) of this section.


(1) Company name and address.


(2) Statement by a responsible official, with that official’s name, title, and signature, certifying the truth, accuracy, and completeness of the content of the report.


(3) Date of report and beginning and ending dates of the reporting period.


(4) A statement that no deviation from the emission limit occurred during the reporting period and that no CEMS or CPMS was out-of-control, according to § 63.8(c)(7).


(c) For each deviation from an emission limit, the semiannual compliance report must include the information in paragraphs (b)(1) through (3) of this section and the information included in paragraphs (c)(1) through (4) of this section, except that on and after December 1, 2020 the semiannual compliance report must also include the information included in paragraph (c)(5) of this section.


(1) The date and time that each deviation started and stopped.


(2) The total operating time of each new or reconstructed engine test cell/stand during the reporting period.


(3) A summary of the total duration of the deviation during the reporting period (recorded in 4-hour periods), and the total duration as a percent of the total operating time during that reporting period.


(4) A breakdown of the total duration of the deviations during the reporting period into those that are due to control equipment problems, process problems, other known causes, and other unknown causes.


(5) An estimate of the quantity of each regulated pollutant emitted over any emission limit, and a description of the method used to estimate the emissions.


(d) For each CEMS or CPMS deviation, the semiannual compliance report must include the information in paragraphs (b)(1) through (3) of this section and the information included in paragraphs (d)(1) through (10) of this section, except that on and after December 1, 2020, the semiannual compliance report must also include the information included in paragraph (d)(11) of this section.


(1) The date and time that each CEMS or CPMS was inoperative except for zero (low-level) and high-level checks.


(2) The date and time that each CEMS or CPMS was out-of-control including the information in § 63.8(c)(8).


(3) A summary of the total duration of CEMS or CPMS downtime during the reporting period (reported in 4-hour periods), and the total duration of CEMS or CPMS downtime as a percent of the total engine test cell/stand operating time during that reporting period.


(4) A breakdown of the total duration of CEMS or CPMS downtime during the reporting period into periods that are due to monitoring equipment malfunctions, nonmonitoring equipment malfunctions, quality assurance/quality control calibrations, other known causes and other unknown causes.


(5) The monitoring equipment manufacturer(s) and model number(s) of each monitor.


(6) The date of the latest CEMS or CPMS certification or audit.


(7) The date and time period of each deviation from an operating limit in Table 2 to this subpart; date and time period of any bypass of the add-on control device; and whether each deviation occurred during a period of SSM or during another period.


(8) A summary of the total duration of each deviation from an operating limit in Table 2 to this subpart, each bypass of the add-on control device during the semiannual reporting period, and the total duration as a percent of the total source operating time during that semiannual reporting period.


(9) A breakdown of the total duration of the deviations from the operating limits in Table 2 to this subpart and bypasses of the add-on control device during the semiannual reporting period by identifying deviations due to startup, shutdown, control equipment problems, process problems, other known causes, and other unknown causes.


(10) A description of any changes in CEMS, CPMS, or controls since the last reporting period.


(11) The total operating time of each new or reconstructed engine test cell/stand during the reporting period.


(e) Prior to December 1, 2020, if you had an SSM of a control device or associated monitoring equipment during the semiannual reporting period that was not consistent with your SSMP, you must submit an immediate SSM report according to the requirements in § 63.10(d)(5)(ii).


(f) Within 60 days after the date of completing each performance test or performance evaluation required by this subpart, you must submit the results of the performance test following the procedures specified in paragraphs (f)(1) through (3) of this section.


(1) Data collected or performance evaluations of CMS measuring relative accuracy test audit (RATA) pollutants using test methods supported by the EPA’s Electronic Reporting Tool (ERT) as listed on the EPA’s ERT website (https://www.epa.gov/electronic-reporting-air-emissions/electronic-reporting-tool-ert) at the time of the test. Submit the results of the performance test or performance evaluation to the EPA via the Compliance and Emissions Data Reporting Interface (CEDRI), which can be accessed through the EPA’s Central Data Exchange (CDX) (https://cdx.epa.gov/). The data must be submitted in a file format generated through the use of the EPA’s ERT. Alternatively, you may submit an electronic file consistent with the extensible markup language (XML) schema listed on the EPA’s ERT website.


(2) Data collected or performance evaluations of CMS measuring RATA pollutants using test methods that are not supported by the EPA’s ERT as listed on the EPA’s ERT website at the time of the test. The results of the performance test or performance evaluation must be included as an attachment in the ERT or an alternate electronic file consistent with the XML schema listed on the EPA’s ERT website. Submit the ERT generated package or alternative file to the EPA via CEDRI.


(3) If you claim some of the information submitted under paragraph (f) of this section is CBI, you must submit a complete file, including information claimed to be CBI, to the EPA. The file must be generated through the use of the EPA’s ERT or an alternate electronic file consistent with the XML schema listed on the EPA’s ERT website. Submit the file on a compact disc, flash drive, or other commonly used electronic storage medium and clearly mark the medium as CBI. Mail the electronic medium to U.S. EPA/OAQPS/CORE CBI Office, Attention: Group Leader, Measurement Policy Group, MD C404-02, 4930 Old Page Rd., Durham, NC 27703. The same file with the CBI omitted must be submitted to the EPA via the EPA’s CDX as described in paragraph (f)(1) of this section.


(g) If you are required to submit reports following the procedure specified in this paragraph, you must submit reports to the EPA via CEDRI, which can be accessed through the EPA’s CDX (https://cdx.epa.gov/). You must use the appropriate electronic report template on the CEDRI website (https://www.epa.gov/electronic-reporting-air-emissions/compliance-and-emissions-data-reporting-interface-cedri) for this subpart. The report must be submitted by the deadline specified in this subpart, regardless of the method in which the report is submitted. If you claim some of the information required to be submitted via CEDRI is CBI, submit a complete report, including information claimed to be CBI, to the EPA. The report must be generated using the appropriate form on the CEDRI website. Submit the file on a compact disc, flash drive, or other commonly used electronic storage medium and clearly mark the medium as CBI. Mail the electronic medium to U.S. EPA/OAQPS/CORE CBI Office, Attention: Group Leader, Measurement Policy Group, MD C404-02, 4930 Old Page Rd., Durham, NC 27703. The same file with the CBI omitted must be submitted to the EPA via the EPA’s CDX as described earlier in this paragraph.


(h) If you are required to electronically submit a report through CEDRI in the EPA’s CDX, you may assert a claim of EPA system outage for failure to timely comply with the reporting requirement. To assert a claim of EPA system outage, you must meet the requirements outlined in paragraphs (h)(1) through (7) of this section.


(1) You must have been or will be precluded from accessing CEDRI and submitting a required report within the time prescribed due to an outage of either the EPA’s CEDRI or CDX systems.


(2) The outage must have occured within the period of time beginning five business days prior to the date that the submission is due.


(3) The outage may be planned or unplanned.


(4) You must submit notification to the Administrator in writing as soon as possible following the date you first knew, or through due diligence should have known, that the event may cause or has caused a delay in reporting.


(5) You must provide to the Administrator a written description identifying:


(i) The date(s) and time(s) when CDX or CEDRI was accessed and the system was unavailable;


(ii) A rationale for attributing the delay in reporting beyond the regulatory deadline to EPA system outage;


(iii) Measures taken or to be taken to minimize the delay in reporting; and


(iv) The date by which you propose to report, or if you have already met the reporting requirement at the time of the notification, the date you reported.


(6) The decision to accept the claim of EPA system outage and allow an extension to the reporting deadline is solely within the discretion of the Administrator.


(7) In any circumstance, the report must be submitted electronically as soon as possible after the outage is resolved.


(i) If you are required to electronically submit a report through CEDRI in the EPA’s CDX, you may assert a claim of force majeure for failure to timely comply with the reporting requirement. To assert a claim of force majuere, you must meet the requirements outlined in paragraphs (i)(1) through (5) of this section.


(1) You may submit a claim if a force majeure event is about to occur, occurs, or has occurred or there are lingering effects from such an event within the period of time beginning five business days prior to the date the submission is due. For the purposes of this section, a force majeure event is defined as an event that will be or has been caused by circumstances beyond the control of the affected facility, its contractors, or any entity controlled by the affected facility that prevents you from complying with the requirement to submit a report electronically within the time period prescribed. Examples of such events are acts of nature (e.g., hurricanes, earthquakes, or floods), acts of war or terrorism, or equipment failure or safety hazard beyond the control of the affected facility (e.g., large scale power outage).


(2) You must submit notification to the Administrator in writing as soon as possible following the date you first knew, or through due diligence should have known, that the event may cause or has caused a delay in reporting.


(3) You must provide to the Administrator:


(i) A written description of the force majeure event;


(ii) A rationale for attributing the delay in reporting beyond the regulatory deadline to the force majeure event;


(iii) Measures taken or to be taken to minimize the delay in reporting; and


(iv) The date by which you propose to report, or if you have already met the reporting requirement at the time of the notification, the date you reported.


(4) The decision to accept the claim of force majeure and allow an extension to the reporting deadline is solely within the discretion of the Administrator.


(5) In any circumstance, the reporting must occur as soon as possible after the force majeure event occurs.


[68 FR 28785, May 27, 2003, as amended at 85 FR 34346, June 3, 2020]


§ 63.9355 What records must I keep?

(a) You must keep the records as described in paragraphs (a)(1) through (5) of this section. After June 3, 2020, you must also keep the records as described in paragraphs (a)(6) through (8) of this section.


(1) A copy of each notification and report that you submitted to comply with this subpart, including all documentation supporting any Initial Notification or Notification of Compliance Status that you submitted, according to the requirements in § 63.10(b)(2)(xiv).


(2) Records of performance evaluations as required in § 63.10(b)(2)(viii).


(3) Records of the occurrence and duration of each malfunction of the air pollution control equipment, if applicable, as required in § 63.9355.


(4) Records of all maintenance on the air pollution control equipment, if applicable, as required in § 63.10(b)(iii).


(5) The calculation of the mass of organic HAP emission reduction by emission capture systems and add-on control devices.


(6) In the event that an affected unit fails to meet an applicable standard, record the number of failures. For each failure record the date, time, the cause, and duration of each failure.


(7) For each failure to meet an applicable standard, record and retain a list of the affected sources or equipment, an estimate of the quantity of each regulated pollutant emitted over any emission limit, and a description of the method used to estimate the emissions.


(8) Record actions taken to minimize emissions in accordance with § 63.9305, and any corrective actions taken to return the affected unit to its normal or usual manner of operation.


(b) For each CPMS, you must keep the records as described in paragraphs (b)(1) through (7) of this section.


(1) For each deviation, a record of whether the deviation occurred during a period of SSM of the control device and associated monitoring equipment.


(2) For affected sources prior to December 1, 2020, the records in § 63.6(e)(3)(iii) through (v) related to SSM.


(3) The records required to show continuous compliance with each operating limit specified in Table 2 to this subpart that applies to you.


(4) For each capture system that is a PTE, the data and documentation you used to support a determination that the capture system meets the criteria in Method 204 of appendix M to 40 CFR part 51 for a PTE and has a capture efficiency of 100 percent, as specified in § 63.9322(a).


(5) For each capture system that is not a PTE, the data and documentation you used to determine capture efficiency according to the requirements specified in §§ 63.9321 and 63.9322(b) through (e), including the records specified in paragraphs (b)(5)(i) and (ii) of this section that apply to you.


(i) Records for a gas-to-gas protocol using a temporary total enclosure or a building enclosure. Records of the mass of TVH emissions captured by the emission capture system as measured by Method 204B or C of appendix M to 40 CFR part 51 at the inlet to the add-on control device, including a copy of the test report. Records of the mass of TVH emissions not captured by the capture system that exited the temporary total enclosure or building enclosure during each capture efficiency test run as measured by Method 204D or E of appendix M to 40 CFR part 51, including a copy of the test report. Records documenting that the enclosure used for the capture efficiency test met the criteria in Method 204 of appendix M to 40 CFR part 51 for either a temporary total enclosure or a building enclosure.


(ii) Records for an alternative protocol. Records needed to document a capture efficiency determination using an alternative method or protocol as specified in § 63.9322(e), if applicable.


(6) The records specified in paragraphs (b)(6)(i) and (ii) of this section for each add-on control device organic HAP destruction or removal efficiency determination as specified in § 63.9323.


(i) Records of each add-on control device performance test conducted according to §§ 63.9321, 63.9322, and 63.9323.


(ii) Records of the engine testing conditions during the add-on control device performance test showing that the performance test was conducted under representative operating conditions.


(7) Records of the data and calculations you used to establish the emission capture and add-on control device operating limits as specified in § 63.9324 and to document compliance with the operating limits as specified in Table 2 to this subpart.


(c) For each CEMS, you must keep the records as described in paragraph (c)(1) through (5) of this section.


(1) Records described in § 63.10(b)(2)(vi) through (xi).


(2) Previous (i.e., superceded) versions of the performance evaluation plan as required in paragraph (c)(5) of this section.


(3) Request for alternatives to the relative accuracy test for CEMS as required in § 63.8(f)(6)(i), if applicable.


(4) For affected sources prior to December 1, 2020, the records in § 63.6(e)(3)(iii) through (v) related to SSM of the control device and associated monitoring equipment.


(5) The owner or operator shall keep these written procedures on record for the life of the affected source or until the affected source is no longer subject to the provisions of this part, to be made available for inspection, upon request, by the Administrator. If the performance evaluation plan is revised, the owner or operator shall keep previous (i.e., superseded) versions of the performance evaluation plan on record to be made available for inspection, upon request, by the Administrator, for a period of 5 years after each revision to the plan. The program of corrective action should be included in the plan required under § 63.8(d)(2).


(d) You must keep the records required in Table 5 to this subpart to show continuous compliance with each emission limitation that applies to you.


[68 FR 28785, May 27, 2003, as amended at 85 FR 34347, June 3, 2020]


§ 63.9360 In what form and how long must I keep my records?

(a) You must maintain all applicable records in such a manner that they can be readily accessed and are suitable for inspection according to § 63.10(b)(1).


(b) As specified in § 63.10(b)(1), you must keep each records for 5 years following the date of each occurrence, measurement, maintenance, corrective action, report, or record.


(c) You must retain your records of the most recent 2 years on site, or your records must be accessible on site. Your records of the remaining 3 years may be retained off site.


(d) Any records required to be maintained by this part that are submitted electronically via the EPA’s CEDRI may be maintained in electronic format. This ability to maintain electronic copies does not affect the requirement for facilities to make records, data, and reports available upon request to a delegated air agency or the EPA as part of an on-site compliance evaluation.


[68 FR 28785, May 27, 2003, as amended at 85 FR 34348, June 3, 2020]


Other Requirements and Information

§ 63.9365 What parts of the General Provisions apply to me?

Table 7 to this subpart shows which parts of the General Provisions in §§ 63.1 through 63.15 apply to you.


§ 63.9370 Who implements and enforces this subpart?

(a) This subpart can be implemented and enforced by us, the U.S. EPA, or a delegated authority such as your State, local, or tribal agency. If the U.S. EPA Administrator has delegated authority to your State, local, or tribal agency, then that agency, in addition to the U.S. EPA, has the authority to implement and enforce this subpart. You should contact your U.S. EPA Regional Office to find out if implementation and enforcement of this subpart is delegated to your State, local, or tribal agency.


(b) In delegating implementation and enforcement authority of this subpart to a State, local, or tribal agency under section 40 CFR part 63, subpart E, the authorities contained in paragraph (c) of this section are retained by the Administrator of U.S. EPA and are not transferred to the State, local, or tribal agency.


(c) The authorities that cannot be delegated to State, local, or tribal agencies are described in paragraphs (c)(1) through (4) of this section.


(1) Approval of alternatives to the emission limitations in § 63.9300 under § 63.6(g).


(2) Approval of major changes to test methods under § 63.7(e)(2)(ii) and (f) and as defined in § 63.90.


(3) Approval of major changes to monitoring under § 63.8(f) and as defined in § 63.90.


(4) Approval of major changes to recordkeeping and reporting under § 63.10(f) and as defined in § 63.90.


§ 63.9375 What definitions apply to this subpart?

Terms used in this subpart are defined in the CAA; in 40 CFR 63.2, and in this section:


CAA means the Clean Air Act (42 U.S.C. 7401 et seq., as amended by Public Law 101-549, 104 Statute 2399).


Area source means any stationary source of HAP that is not a major source as defined in this part.


Combustion turbine engine means a device in which air is compressed in a compressor, enters a combustion chamber, and is compressed further by the combustion of fuel injected into the combustion chamber. The hot compressed combustion gases then expand over a series of curved vanes or blades arranged on a central spindle that rotates.


Deviation means any instance in which an affected source subject to this subpart, or an owner or operator of such a source:


(1) Fails to meet any requirement or obligation established by this subpart, including but not limited to any emission limitations;


(2) Fails to meet any term or condition that is adopted to implement an applicable requirement in this subpart and that is included in the operating permit for any affected source required to obtain such a permit; or


(3) Prior to December 1, 2020, fails to meet any emission limitation or operating limit in this subpart during malfunction, regardless of whether or not such failure is permitted by this subpart.


Engine means any internal combustion engine, any combustion turbine engine, or any rocket engine.


Engine Test Cell/Stand means any apparatus used for testing uninstalled stationary or uninstalled mobile (motive) engines.


Hazardous Air Pollutant (HAP) means any air pollutant listed in or pursuant to section 112(b) of the CAA.


Internal combustion engine means a device in which air enters a combustion chamber, is mixed with fuel, compressed in the chamber, and combusted. Fuel may enter the combustion chamber with the air or be injected into the combustion chamber. Expansion of the hot combustion gases in the chamber rotates a shaft, either through a reciprocating or rotary action. For purposes of this subpart, this definition does not include combustion turbine engines.


Major source, as used in this subpart, shall have the same meaning as in § 63.2.


Malfunction means any sudden, infrequent, and not reasonably preventable failure of air pollution control equipment, process equipment, or a process to operate in a normal or usual manner which causes, or has the potential to cause, the emission limitations in an applicable standard to be exceeded. Failures that are caused in part by poor maintenance or careless operation are not malfunctions.


Rated power means the maximum power output of an engine in use.


Potential to emit means the maximum capacity of a stationary source to emit a pollutant under its physical and operational design. Any physical or operational limitation on the capacity of the stationary source to emit a pollutant, including air pollution control equipment and restrictions on hours of operation or on the type or amount of material combusted, stored, or processed, shall be treated as part of its design if the limitation or the effect it would have on emissions is federally enforceable.


Responsible official means responsible official as defined by 40 CFR 70.2.


Rocket engine means a device consisting of a combustion chamber in which materials referred to as propellants, which provide both the fuel and the oxygen for combustion, are burned. Combustion gases escape through a nozzle, providing thrust.


Uninstalled engine means an engine not installed in, or an integrated part of, the final product.


[68 FR 28785, May 27, 2003, as amended at 71 FR 20470, Apr. 20, 2006; 85 FR 34348, June 3, 2020]


Table 1 to Subpart PPPPP of Part 63—Emission Limitations

You must comply with the emission limits that apply to your affected source in the following table as required by § 63.9300.


For each new or reconstructed affected source located at a major source facility that is used in whole or in part for testing . . .
You must meet one of the following emission limitations:
1. internal combustion engines with rated power of 25 hp (19 kW) or morea. limit the concentration of CO or THC to 20 ppmvd or less (corrected to 15 percent O2 content); or

b. achieve a reduction in CO or THC of 96 percent or more between the inlet and outlet concentrations (corrected to 15 percent O2 content) of the emission control device.

Table 2 to Subpart PPPPP of Part 63—Operating Limits

If you are required to comply with operating limits in § 63.9302, you must comply with the applicable operating limits in the following table:


For the following device . . .
You must meet the following operating limit . . .
and you must demonstrate continuous compliance with the operating limit by . . .
1. Thermal oxidizera. The average combustion temperature in any 3-hour period must not fall below the combustion temperature limit established according to § 63.9324(a)i. Collecting the combustion temperature data according to § 63.9306(c);

ii. Reducing the data to 3-hour block averages; and

iii. Maintaining the 3-hour average combustion temperature at or above the temperature limit.
2. Catalytic oxidizera. The average temperature measured just before the catalyst bed in any 3-hour period must not fall below the limit established according to § 63.9324(b)i. Collecting the temperature data according to § 63.9306(c);

ii. Reducing the data to 3-hour block averages; and

iii. Maintaining the 3-hour average temperature before the catalyst bed at or above the temperature limit.
b. Either ensure that the average temperature difference across the catalyst bed in any 3-hour period does not fall below the temperature difference limit established according to § 63.9324(b)(2) or develop and implement an inspection and maintenance plan according to § 63.9324(b)(3) and (4)i. Either collecting the temperature data according to § 63.9306(c), reducing the data to 3-hour block averages, and maintaining the 3-hour average temperature difference at or above the temperature difference limit; or

ii. Complying with the inspection and maintenance plan developed according to § 63.9324(b)(3) and (4).
3. Emission capture system that is a PTE according to § 63.9322(a)a. The direction of the air flow at all times must be into the enclosure; and eitheri. Collecting the direction of air flow; and either the facial velocity of air through all natural draft openings according to § 63.9306(d)(1) or the pressure drop across the enclosure according to § 63.9306(d)(2); and

ii. Maintaining the facial velocity of air flow through all natural draft openings or the pressure drop at or above the facial velocity limit or pressure drop limit, and maintaining the direction of air flow into the enclosure at all times.
b. The average facial velocity of air through all natural draft openings in the enclosure must be at least 200 feet per minute; orFollow the requirements in 3ai and ii of this table.
c. The pressure drop across the enclosure must be at least 0.007 inch H2O, as established in Method 204 of appendix M to 40 CFR part 51Follow the requirements in 3ai and ii of this table.
4. Emission capture system that is not a PTE according to § 63.9322(a)a. The average gas volumetric flow rate or duct static pressure in each duct between a capture device and add-on control device inlet in any 3-hour period must not fall below the average volumetric flow rate or duct static pressure limit established for that capture device according § 63.9306(d)i. Collecting the gas volumetric flow rate or duct static pressure for each capture device according to § 63.9306(d);

ii. Reducing the data to 3-hour block averages; and

iii. Maintaining the 3-hour average gas volumetric flow rate or duct static pressure for each capture device at or above the gas volumetric flow rate or duct static pressure limit.

Table 3 to Subpart PPPPP of Part 63—Requirements for Initial Compliance Demonstrations

As stated in § 63.9321, you must demonstrate initial compliance with each emission limitation that applies to you according to the following table:


For each new or reconstructed affected source complying with . . .
You must . . .
Using . . .
According to the following requirements . . .
1. The CO or THC outlet concentration emission limitationa. Demonstrate CO or THC emissions are 20 ppmvd or lessi. EPA Methods 3A and 10 of appendix A to 40 CFR part 60 for CO measurement or EPA Method 25A of appendix A to 40 CFR part 60 for THC measurement; orYou must demonstrate that the outlet concentration of CO or THC emissions from the test cell/stand or emission control device is 20 ppmvd or less, corrected to 15 percent O2 content, using the average of the test runs in the performance test.
ii. A CEMS for CO or THC and O2 at the outlet of the engine test cell/stand or emission control deviceThis demonstration is conducted immediately following a successful performance evaluation of the CEMS as required in § 63.9320 (b). The demonstration consists of the first 4-hour rolling average of measurements. The CO or THC concentration must be corrected to 15 percent O2 content, dry basis using Equation 1 in § 63.9320.
2. The CO or THC percent reduction emission limitationa. Demonstrate a reduction in CO or THC of 96 percent or morei. You must conduct an initial performance test to determine the capture and control efficiencies of the equipment and to establish operating limits to be achieved on a continuous basis; orYou must demonstrate that the reduction in CO or THC emissions is at least 96 percent using the first 4-hour rolling average after a successful performance evaluation. Your inlet and outlet measurements must be on a dry basis and corrected to 15 percent O2 content.
ii. A CEMS for CO or THC and O2 at both the inlet and outlet of the emission control deviceThis demonstration is conducted immediately following a successful performance evaluation of the CEMS as required in § 63.9320(b). The demonstration consists of the first 4-hour rolling average of measurements. The inlet and outlet CO or THC concentrations must be corrected to 15 percent O2 content using Equation 1 in § 63.9320. The reduction in CO or THC is calculated using Equation 2 in § 63.9320.

[68 FR 28785, May 27, 2003, as amended at 85 FR 34348, June 3, 2020]


Table 4 to Subpart PPPPP of Part 63—Initial Compliance With Emission Limitations

As stated in § 63.9330, you must demonstrate initial compliance with each emission limitation that applies to you according to the following table:


For the . . .
You have demonstrated initial compliance if . . .
1. CO or THC concentration emission limitationThe first 4-hour rolling average CO or THC concentration is 20 ppmvd or less, corrected to 15 percent O2 content if CEMS are installed or the average of the test run averages during the performance test is 20 ppmvd or less, corrected to 15 percent O2 content.
2. CO or THC percent reduction emission limitationThe first 4-hour rolling average reduction in CO or THC is 96 percent or more, dry basis, corrected to 15 percent O2 content.

[68 FR 28785, May 27, 2003, as amended at 85 FR 34348, June 3, 2020]


Table 5 to Subpart PPPPP of Part 63—Continuous Compliance With Emission Limitations

As stated in § 63.9340, you must demonstrate continuous compliance with each emission limitation that applies to you according to the following table:


For the . . .
You must . . .
By . . .
1. CO or THC concentration emission limitationa. Demonstrate CO or THC emissions are 20 ppmvd or less over each 4- hour rolling averaging periodi. Collecting the CPMS data according to § 63.9306(a), reducing the measurements to 1-hour averages used to calculate the 3-hr block average; or

ii. Collecting the CEMS data according to § 63.9307(a), reducing the measurements to 1-hour averages, correcting them to 15 percent O2 content, dry basis, according to § 63.9320.
2. CO or THC percent reduction emission limitationa. Demonstrate a reduction in CO or THC of 96 percent or more over each 4-hour rolling averaging periodi. Collecting the CPMS data according to § 63.9306(a), reducing the measurements to 1-hour averages; or

ii. Collecting the CEMS data according to § 63.9307(b), reducing the measurements to 1-hour averages, correcting them to 15 percent O2 content, dry basis, calculating the CO or THC percent reduction according to § 63.9320.

[68 FR 28785, May 27, 2003, as amended at 85 FR 34345, June 3, 2020]


Table 6 to Subpart PPPPP of Part 63—Requirements for Reports

As stated in § 63.9350, you must submit each report that applies to you according to the following table:


If you own or operate a new or reconstructed affected source that must comply with emission limitations, you must submit a . . .
The report must contain . . .
You must submit the report . . .
1. Compliance reporta. If there are no deviations from the emission limitations that apply to you, a statement that there were no deviations from the emission limitations during the reporting periodSemiannually, according to the requirements in § 63.9350.
b. If there were no periods during which the CEMS or CPMS were out of control as specified in § 63.8(c)(7), a statement that there were no periods during which the CEMS or CPMS was out of control during the reporting periodSemiannually, according to the requirements in § 63.9350.
c. If you have a deviation from any emission limitation during the reporting period, the report must contain the information in § 63.9350(c)Semiannually, according to the requirements in § 63.9350.
d. If there were periods during which the CEMS or CPMS were out of control, as specified in § 63.8(c)(7), that report must contain the information in § 63.9350(d)Semiannually, according to the requirements in § 63.9350.
e. If you had an SSM of a control device or associated monitoring equipment during the reporting period, the report must include the information in § 63.10(d)(5)(i)Semiannually, according to the requirements in § 63.9350.

Table 7 to Subpart PPPPP of Part 63—Applicability of General Provisions to Subpart PPPPP

As stated in 63.9365, you must comply with the General Provisions in §§ 63.1 through 63.15 that apply to you according to the following table:


Citation
Subject
Applicable to subpart PPPPP
Explanation
§ 63.1(a)(1)-(12)General ApplicabilityYes
§ 63.1(b)(1)-(3)Initial Applicability DeterminationYesApplicability to subpart PPPPP is also specified in § 63.9285.
§ 63.1(c)(1)Applicability After Standard EstablishedYes
§ 63.1(c)(2)Applicability of Permit Program for Area SourcesNoArea sources are not subject to subpart PPPPP.
§ 63.1(c)(5)NotificationsYes
§ 63.1(c)(6)ApplicabilityReclassificationYes.
§ 63.1(d)[Reserved]
§ 63.1(e)Applicability of Permit Program Before Relevant Standard is SetYes
§ 63.2DefinitionsYesAdditional definitions are specified in § 63.9375.
§ 63.3Units and AbbreviationsYes
§ 63.4Prohibited Activities and CircumventionYes
§ 63.5(a)Construction/ReconstructionYes
§ 63.5(b)Requirements for Existing, Newly Constructed, and Reconstructed SourcesYes
§ 63.5(d)Application for Approval of Construction/ReconstructionYes
§ 63.5(e)Approval of Construction/ReconstructionYes
§ 63.5(f)Approval of Construction/Reconstruction based on Prior State ReviewYes
§ 63.6(a)Compliance With Standards and Maintenance Requirements-ApplicabilityYes
§ 63.6(b)(1)-(7)Compliance Dates for New and Reconstructed SourcesYes§ 63.9295 specifies the compliance dates.
§ 63.6(c)(1)-(2)Compliance Dates for Existing SourcesNoSubpart PPPPP does not establish standards for existing sources.
§ 63.6(c)(5)Compliance Dates for Existing SourcesYes§ 63.9295(b) specifies the compliance date if a new or reconstructed area source becomes a major source.
§ 63.6(e)(1)(i)Operation and MaintenanceYes before December 1, 2020. No on and after December 1, 2020See § 63.9305 for general duty requirement.
§ 63.6(e)(1)(ii)Operation and MaintenanceYes before December 1, 2020. No on and after December 1, 2020
§ 63.6(e)(1)(iii)Operation and MaintenanceYes
§ 63.6(e)(3)SSM PlanYes before December 1, 2020. No on and after December 1, 2020
§ 63.6(f)(1)Compliance Except During SSMYes before December 1, 2020. No on and after December 1, 2020
§ 63.6(f)(2)-(3)Methods for Determining ComplianceYes
§ 63.6(g)(1)-(3)Use of Alternative StandardsYes
§ 63.6(h)Compliance With Opacity/Visible Emission StandardsNoSubpart PPPPP does not establish opacity standards and does require continuous opacity monitoring systems (COMS).
§ 63.6(i)(1)-(16)Extension of ComplianceNoCompliance extension provisions apply to existing sources which do not have emission limitations in subpart PPPPP.
§ 63.6(j)Presidential Compliance ExemptionYes
§ 63.7(a)(1)-(2)Performance Test DatesYes
§ 63.7(a)(3)Performance Test Required By the AdministratorYes
§ 63.7(b)-(d)Performance Test Requirements-Notification, Quality Assurance, Facilities Necessary for Safe Testing, Conditions During TestingYes
§ 63.7(e)(1)Conditions for Conducting Performance TestsYes before December 1, 2020. No, see § 63.9321, on and after December 1, 2020
§ 63.7(e)(2)-(4)Conduct of Performance TestsYes
§ 63.7(f)Alternative Test MethodsYes
§ 63.7(g)-(h)Performance Testing Requirements-Data Analysis, Recordkeeping, Reporting, Waiver of TestYes
§ 63.8(a)(1)-(2)Monitoring Requirements—ApplicabilityYesSubpart PPPPP contains specific requirement for monitoring at § 63.9325.
§ 63.8(a)(4)Additional Monitoring RequirementsNoSubpart PPPPP does not have monitoring requirement for flares.
§ 63.8(b)Conduct of MonitoringYes
§ 63.8(c)(1)Continuous Monitoring System (CMS) Operation and MaintenanceYes
§ 63.8(c)(1)(i)General Duty to Minimize Emissions and CMS OperationYes before December 1, 2020. No on and after December 1, 2020
§ 63.8(c)(1)(ii)Operation and Maintenance of CMSYes
§ 63.8(c)(1)(iii)Requirement to Develop SSM Plan for CMSYes before December 1, 2020. No on and after December 1, 2020
§ 63.8(c)(2)-(3)Monitoring System InstallationYes
§ 63.8(c)(4)CMSNo§ 63.9335(a) and (b) specifies the requirements.
§ 63.8(c)(5)COMSNoSubpart PPPPP does not have opacity or VE standards.
§ 63.8(c)(6)-(8)CMS RequirementsYesExcept that subpart PPPPP does not require COMS.
§ 63.8(d)(1)-(2)CMS Quality ControlYes
§ 63.8(d)(3)CMS Quality ControlYes before December 1, 2020. No on and after December 1, 2020
§ 63.8(e)CMS PerformanceYesExcept for § 63.8(e)(5)(ii) which applies to COMS.
§ 63.8(f)(1)-(5)Alternative Monitoring MethodYes
§ 63.8(f)(6)Alternative to Relative Accuracy TestYes
§ 63.8(g)Data ReductionYes before December 1, 2020. No on and after December 1, 2020§§ 63.9335 and 63.9340 specify monitoring data reduction.
§ 63.9(a)-(b)Notification RequirementsYes
§ 63.9(c)Request for Compliance ExtensionNoCompliance extension to not apply to new or reconstructed sources.
§ 63.9(d)Notification of Special Compliance Requirements for New SourcesYes
§ 63.9(e)Notification of Performance TestNoSubpart PPPPP does not require performance testing.
§ 63.9(f)Notification of Opacity/VE testNoSubpart PPPPP does not have opacity/VE standards.
§ 63.9(g)(1)Additional Notifications When Using CMSYes
§ 63.9(g)(2)Additional Notifications When Using CMSNoSubpart PPPPP does not have opacity/VE standards.
§ 63.9(g)(3)Additional Notifications When Using CMSYes
§ 63.9(h)Notification of Compliance StatusYes
§ 63.9(i)Adjustment of Submittal DeadlinesYes
§ 63.9(j)Change in Previous InformationYes
§ 63.9(k)NotificationsElectronic reporting proceduresYes, only as specified in § 63.9(j).
§ 63.10(a)Recordkeeping/ReportingYes
§ 63.10(b)(1)General Recordkeeping RequirementsYes
§ 63.10(b)(2)(i)Recordkeeping of Occurrence and Duration of Startups and ShutdownsYes before December 1, 2020. No on and after December 1, 2020
§ 63.10(b)(2)(ii)Recordkeeping of Occurrence and Duration of MalfunctionsYes before December 1, 2020. No on and after December 1, 2020See § 63.9355 for recordkeeping of (1) date, time, and duration; (2) listing of affected source or equipment, and an estimate of the quantity of each regulated pollutant emitted over the standard; and (3) actions to minimize emissions and correct the failure.
§ 63.10(b)(2)(iii)Recordkeeping of Maintenance on Controls and Monitoring EquipmentYes
§ 63.10(b)(2)(iv)-(v)Actions Taken to Minimize Emissions During SSMYes before December 1, 2020. No on and after December 1, 2020
§ 63.10(b)(2)(vi)-(xi)CMS RecordsYes
§ 63.10(b)(2)(xii)RecordsYes
§ 63.10(b)(2)(xiii)RecordsYes
§ 63.10(b)(2)(xiv)RecordsYes
§ 63.10(b)(3)Recordkeeping for Applicability DeterminationsYes
§ 63.10(c)(1)-(6), (9)-(14)Additional Recordkeeping for CMSYes
§ 63.10(c)(7)-(8)Records of Excess Emissions and Parameter Monitoring Exceedances for CMSNoSpecific language is located at § 63.9355 of subpart PPPPP.
§ 63.10(c)(15)Records Regarding the SSM PlanYes before December 1, 2020. No on and after December 1, 2020
§ 63.10(d)(1)General Reporting RequirementsYes
§ 63.10(d)(2)Report of Performance Test ResultsYes
§ 63.10(d)(3)Reporting of Opacity or VE ObservationsNoSubpart PPPPP does not have opacity/VE standards.
§ 63.10(d)(4)Progress Reports for Sources with Compliance ExtensionsNoCompliance extensions do not apply to new or reconstructed sources.
§ 63.10(d)(5)SSM ReportsYes before December 1, 2020. No on and after December 1, 2020On and after December 1, 2020, see § 63.9350 for malfunction reporting requirements.
§ 63.10(e)(1) and (2)(i)Additional CMS ReportsYes
§ 63.10(e)(2)(ii)Additional CMS ReportsNoSubpart PPPPP does not require COMS.
§ 63.10(e)(3)Excess Emissions/CMS Performance ReportsNoSpecific language in located in § 63.9350 of subpart PPPPP.
§ 63.10(e)(4)COMS Data ReportsNoSubpart PPPPP does not require COMS.
§ 63.10(f)Waiver for Recordkeeping/ReportingYes
§ 63.11Control Device Requirements/FlaresNoSubpart PPPPP does not specify use of flares for compliance.
§ 63.12State Authority and DelegationsYes
§ 63.13AddressesYes
§ 63.14Incorporation by ReferenceYesASTM D 6522-00 and ANSI/ASME PTC 19.10-1981 (incorporated by reference—See § 63.14).
§ 63.15Availability of Information/ConfidentialityYes

[85 FR 34349, June 3, 2020, as amended at 85 FR 73917, Nov. 19, 2020]


Subpart QQQQQ—National Emission Standards for Hazardous Air Pollutants for Friction Materials Manufacturing Facilities


Source:67 FR 64506, Oct. 18, 2002, unless otherwise noted.

What This Subpart Covers

§ 63.9480 What is the purpose of this subpart?

This subpart establishes national emission standards for hazardous air pollutants (NESHAP) for friction materials manufacturing facilities that use a solvent-based process. This subpart also establishes requirements to demonstrate initial and continuous compliance with all applicable emission limitations in this subpart.


§ 63.9485 Am I subject to this subpart?

(a) You are subject to this subpart if you own or operate a friction materials manufacturing facility (as defined in § 63.9565) that is (or is part of) a major source of hazardous air pollutants (HAP) emissions. Your friction materials manufacturing facility is a major source of HAP if it emits or has the potential to emit any single HAP at a rate of 9.07 megagrams (10 tons) or more per year or any combination of HAP at a rate of 22.68 megagrams (25 tons) or more per year.


(b) The requirements in this subpart do not apply to research and development facilities, as defined in section 112(c)(7) of the Clean Air Act.


[67 FR 64506, Oct. 18, 2002, as amended at 85 FR 73917, Nov. 19, 2020]


§ 63.9490 What parts of my plant does this subpart cover?

(a) This subpart applies to each new, reconstructed, or existing affected source at your friction materials manufacturing facility.


(b) The affected source covered by this subpart is each new, reconstructed, or existing solvent mixer (as defined in § 63.9565) at your friction materials manufacturing facility.


(c) A solvent mixer at your friction materials manufacturing facility is new if you commence construction of the solvent mixer after October 18, 2002. An affected source is reconstructed if it meets the definition of “reconstruction” in § 63.2, and reconstruction is commenced after October 18, 2002.


(d) A solvent mixer at your friction materials manufacturing facility is existing if it is not new or reconstructed.


§ 63.9495 When do I have to comply with this subpart?

(a) If you have an existing solvent mixer, you must comply with each of the requirements for existing sources no later than October 18, 2005, except as otherwise specified at this section and §§ 63.9505, 63.9530, 63.9540, 63.9545, and Table 1 to this subpart.


(b) If you have a new or reconstructed solvent mixer for which construction or reconstruction commenced after October 18, 2002, but before May 4, 2018, you must comply with the requirements for new and reconstructed sources upon initial startup, except as otherwise specified at this section and §§ 63.9505, 63.9530, 63.9540, 63.9545, and Table 1 to this subpart.


(c) If your friction materials manufacturing facility is an area source that increases its emissions or its potential to emit such that it becomes a (or part of a) major source of HAP emissions, then paragraphs (c)(1) and (2) of this section apply.


(1) For any portion of the area source that becomes a new or reconstructed affected source, you must comply with the requirements for new and reconstructed sources upon startup or no later than October 18, 2002, whichever is later.


(2) For any portion of the area source that becomes an existing affected source, you must comply with the requirements for existing sources no later than 1 year after the area source becomes a major source or no later than October 18, 2005, whichever is later.


(d) You must meet the notification and schedule requirements in § 63.9535. Several of the notifications must be submitted before the compliance date for your affected source.


(e) Solvent mixers constructed or reconstructed after May 3, 2018, must be in compliance with this subpart at startup or by February 8, 2019, whichever is later.


[67 FR 64506, Oct. 18, 2002, as amended at 84 FR 2750, Feb. 8, 2019]


Emission Limitations

§ 63.9500 What emission limitations must I meet?

(a) For each new, reconstructed, or existing large solvent mixer at your friction materials manufacturing facility, you must limit HAP solvent emissions to the atmosphere to no more than 30 percent of that which would otherwise be emitted in the absence of solvent recovery and/or solvent substitution, based on a 7-day block average.


(b) For each new, reconstructed, or existing small solvent mixer at your friction materials manufacturing facility, you must limit HAP solvent emissions to the atmosphere to no more than 15 percent of that which would otherwise be emitted in the absence of solvent recovery and/or solvent substitution, based on a 7-day block average.


General Compliance Requirements

§ 63.9505 What are my general requirements for complying with this subpart?

(a) Before August 7, 2019, for each existing source and each new or reconstructed source for which construction or reconstruction commenced after October 18, 2002, but before May 4, 2018, you must be in compliance with the emission limitations in this subpart at all times, except during periods of startup, shutdown, or malfunction. On and after August 7, 2019, for each such source you must be in compliance with the emission limitations in this subpart at all times. For new and reconstructed sources for which construction or reconstruction commenced after May 3, 2018, you must be in compliance with the emissions limitations in this subpart at all times.


(b) Before August 7, 2019, for each existing source, and for each new or reconstructed source for which construction or reconstruction commenced after October 18, 2002, but before May 4, 2018, you must always operate and maintain your affected source, including air pollution control and monitoring equipment, according to the provisions in § 63.6(e)(1)(i). On and after August 7, 2019 for each such source, and after February 8, 2019 for new and reconstructed sources for which construction or reconstruction commenced after May 3, 2018, at all times you must operate and maintain any affected source, including associated air pollution control equipment and monitoring equipment, in a manner consistent with safety and good air pollution control practices for minimizing emissions. The general duty to minimize emissions does not require you to make any further efforts to reduce emissions if levels required by the applicable standard have been achieved. Determination of whether a source is operating in compliance with operation and maintenance requirements will be based on information available to the Administrator which may include, but is not limited to, monitoring results, review of operation and maintenance procedures, review of operation and maintenance records, and inspection of the source.


(c) Before August 7, 2019, for each existing source, and for each new or reconstructed source for which construction commenced after October 18, 2002, but before May 4, 2018, you must develop a written startup, shutdown, and malfunction plan according to the provisions in § 63.6(e)(3). For each such source, a startup, shutdown, and malfunction plan is not required on and after August 7, 2019. No startup, shutdown, and malfunction plan is required for any new or reconstructed source for which construction or reconstruction commenced after May 3, 2018.


[84 FR 2750, Feb. 8, 2019]


Initial Compliance Demonstration Requirements

§ 63.9510 By what date must I conduct my initial compliance demonstration?

(a) If you use a solvent recovery system and/or solvent substitution, you must conduct your initial compliance demonstration within 7 calendar days after the compliance date that is specified for your source in § 63.9495.


(b) If you use a control technique other than a solvent recovery system and/or solvent substitution, you must comply with the provisions in § 63.9570.


§ 63.9515 How do I demonstrate initial compliance with the emission limitation that applies to me?

(a) You have demonstrated initial compliance for each new, reconstructed, or existing large solvent mixer subject to the emission limitation in § 63.9500(a) if the HAP solvent discharged to the atmosphere during the first 7 days after the compliance date, determined according to the provisions in § 63.9520, does not exceed a 7-day block average of 30 percent of that which would otherwise be emitted in the absence of solvent recovery and/or solvent substitution.


(b) You have demonstrated initial compliance for each new, reconstructed, or existing small solvent mixer subject to the emission limitation in § 63.9500(b) if the HAP solvent discharged to the atmosphere during the first 7 days after the compliance date, determined according to the provisions in § 63.9520, does not exceed a 7-day block average of 15 percent of that which would otherwise be emitted in the absence of solvent recovery and/or solvent substitution.


(c) You must submit a notification of compliance status containing the results of the initial compliance demonstration according to § 63.9535(e).


§ 63.9520 What procedures must I use to demonstrate initial compliance?

(a) If you use a solvent recovery system, you must use the procedures in paragraphs (a)(1) through (8) of this section to demonstrate initial compliance with the emission limitations in § 63.9500(a) and (b).


(1) Record the date and time of each mix batch.


(2) Record the identity of each mix batch using a unique batch ID, as defined in § 63.9565.


(3) Measure and record the weight of HAP solvent loaded into the solvent mixer for each mix batch.


(4) Measure and record the weight of HAP solvent recovered for each mix batch.


(5) If you use a solvent recovery system, you must determine the percent of HAP solvent discharged to the atmosphere for each mix batch according to Equation 1 of this section as follows:


(Eq. 1)



Where:

Pb = Percent of HAP solvent discharged to the atmosphere for each mix batch, percent;

Srec = Weight of HAP solvent recovered for each mix batch, lb;

Smix = Weight of HAP solvent loaded into the solvent mixer for each mix batch, lb.

(6) If you use solvent substitution for a mix batch, you must record the use of a non-HAP material as a substitute for a HAP solvent for that mix batch and assign a value of 0 percent to the percent of HAP solvent discharged to the atmosphere for that mix batch (Pb).


(7) Determine the 7-day block average percent of HAP solvent discharged to the atmosphere according to Equation 2 of this section as follows:




Where:

%P7 = 7-day block average percent of HAP solvent discharged to the atmosphere, percent;

i = mix batch;

n = number of mix batches in 7-day block average.

(8) Have valid data for at least 90 percent of the mix batches over the 7-day averaging period.


(b) If you use a control technique other than a solvent recovery system and/or solvent substitution, you may apply to EPA for approval to use an alternative method of demonstrating compliance with the emission limitations for solvent mixers in § 63.9500(a) and (b), as provided in § 63.9570.


§ 63.9525 What are the installation, operation, and maintenance requirements for my weight measurement device?

(a) If you use a solvent recovery system, you must install, operate, and maintain a weight measurement device to measure the weight of HAP solvent loaded into the solvent mixer and the weight of HAP solvent recovered for each mix batch.


(b) For each weight measurement device required by this section, you must develop and submit for approval a site-specific monitoring plan that addresses the requirements of paragraphs (b)(1) through (6) of this section:


(1) Procedures for installing the weight measurement device;


(2) The minimum accuracy of the weight measurement device in pounds and as a percent of the average weight of solvent to be loaded into the solvent mixer;


(3) Site-specific procedures for how the measurements will be made;


(4) How the measurement data will be recorded, reduced, and stored;


(5) Procedures and acceptance criteria for calibration of the weight measurement device; and


(6) How the measurement device will be maintained, including a routine maintenance schedule and spare parts inventory list.


(c) The site-specific monitoring plan required in paragraph (b) of this section must include, at a minimum, the requirements of paragraphs (c)(1) through (3) of this section:


(1) The weight measurement device must have a minimum accuracy of ±0.05 kilograms (±0.1 pounds) or ±1 percent of the average weight of solvent to be loaded into the solvent mixer, whichever is greater.


(2) An initial multi-point calibration of the weight measurement device must be made using 5 points spanning the expected range of weight measurements before the weight measurement device can be used. The manufacturer’s calibration results can be used to meet this requirement.


(3) Once per day, an accuracy audit must be made using a single Class F calibration weight that corresponds to 20 to 80 percent of the average weight of solvent to be loaded into the solvent mixer. If the weight measurement device cannot reproduce the value of the calibration weight within ±0.05 kilograms (0.1 pounds) or ±1 percent of the average weight of solvent to be loaded into the solvent mixer, whichever is greater, the scale must be recalibrated before being used again. The recalibration must be performed with at least five Class F calibration weights spanning the expected range of weight measurements.


(d) You must operate and maintain the weight measurement device according to the site-specific monitoring plan.


(e) You must maintain records of all maintenance activities, calibrations, and calibration audits.


Continuous Compliance Requirements

§ 63.9530 How do I demonstrate continuous compliance with the emission limitation that applies to me?

(a) If you use a solvent recovery system and/or solvent substitution, you must demonstrate continuous compliance with the emission limitations for solvent mixers in § 63.9500(a) and (b) according to the provisions in paragraphs (a)(1) through (3) of this section.


(1) For existing sources and for new or reconstructed sources for which construction or reconstruction commenced after October 18, 2002, but before May 4, 2018, before August 7, 2019, except for during malfunctions of your weight measurement device and associated repairs, you must collect and record the information required in § 63.9520(a)(1) through (8) at all times that the affected source is operating and record all information needed to document conformance with these requirements. On and after August 7, 2019 for such sources, and after February 8, 2019 for new or reconstructed sources that commenced construction after May 3, 2018, you must collect and record the information required in § 63.9520(a)(1) through (8) at all times that the affected source is operating and record all information needed to document conformance with these requirements.


(2) For new, reconstructed, or existing large solvent mixers, maintain the 7-day block average percent of HAP solvent discharged to the atmosphere at or below 30 percent of that which would otherwise be emitted in the absence of solvent recovery and/or solvent substitution.


(3) For new, reconstructed, or existing small solvent mixers, maintain the 7-day block average percent of HAP solvent discharged to the atmosphere at or below 15 percent of that which would otherwise be emitted in the absence of solvent recovery and/or solvent substitution.


(b) If you use a control technique other than a solvent recovery system and/or solvent substitution, you must demonstrate continuous compliance with the emission limitations for solvent mixers in § 63.9500(a) and (b) according to the provisions in § 63.9570.


(c) You must report each instance in which you did not meet the emission limitations for solvent mixers in § 63.9500(a) and (b). This includes periods of startup, shutdown, or malfunction. These instances are deviations from the emission limitations in this subpart. These deviations must be reported according to the requirements in § 63.9540.


(d) [Reserved]


(e) For existing sources and for new or reconstructed sources which commenced construction or reconstruction after October 18, 2002, but before May 4, 2018, before August 7, 2019, consistent with §§ 63.6(e) and 63.7(e)(1), deviations that occur during a period of startup, shutdown, or malfunction are not violations if you demonstrate to the Administrator’s satisfaction that you were operating in accordance with § 63.6(e)(1). The Administrator will determine whether deviations that occur during a period of startup, shutdown, or malfunction are violations, according to the provisions in § 63.6(e). On and after August 7, 2019 for such sources, and after February 8, 2019 for new or reconstructed sources which commence construction or reconstruction after May 3, 2018, all deviations are considered violations.


[67 FR 64506, Oct. 18, 2002, as amended at 71 FR 20470, Apr. 20, 2006; 84 FR 2751, Feb. 8, 2019]


Notifications, Reports, and Records

§ 63.9535 What notifications must I submit and when?

(a) You must submit all of the notifications in §§ 63.8(f)(4) and 63.9(b), (c), (d), and (h) that apply to you by the specified dates.


(b) If you use a control technique other than a solvent recovery system and/or solvent substitution, you must comply with the provisions in § 63.9570.


(c) As specified in § 63.9(b)(2), if you start up your affected source before October 18, 2002, you must submit your initial notification no later than 120 calendar days after October 18, 2002, or no later than 120 days after the source becomes subject to this subpart, whichever is later.


(d) As specified in § 63.9(b)(3), if you start up your new affected source on or after October 18, 2002, you must submit your initial notification no later than 120 calendar days after you become subject to this subpart.


(e) You must submit a notification of compliance status according to § 63.9(h)(2)(ii). You must submit the notification of compliance status before the close of business on the 30th calendar day following the completion of the initial compliance demonstration.


[67 FR 64506, Oct. 18, 2002, as amended at 85 FR 73917, Nov. 19, 2020]


§ 63.9540 What reports must I submit and when?

(a) Unless the Administrator has approved a different schedule, you must submit each semiannual compliance report according to the requirements in paragraphs (a)(1) through (5) of this section.


(1) The first compliance report must cover the period beginning on the compliance date that is specified for your affected source in § 63.9495 and ending on June 30 or December 31, whichever date comes first after the compliance date that is specified for your source in § 63.9495.


(2) The first compliance report must be postmarked or delivered no later than July 31 or January 31, whichever date comes first after your first compliance report is due.


(3) Each subsequent compliance report must cover the semiannual reporting period from January 1 through June 30 or the semiannual reporting period from July 1 through December 31.


(4) Each subsequent compliance report must be postmarked or delivered no later than July 31 or January 31, whichever date comes first after the end of the semiannual reporting period.


(5) For each affected source that is subject to permitting regulations pursuant to 40 CFR part 70 or 71 of this chapter, and if the permitting authority has established dates for submitting semiannual reports pursuant to 40 CFR 70.6(a)(3)(iii)(A) or 40 CFR 71.6(a)(3)(iii)(A) of this chapter, you may submit the first and subsequent compliance reports according to the dates the permitting authority has established instead of according to the dates in paragraphs (a)(1) through (4) of this section.


(b) Each compliance report must include the information in paragraphs (b)(1) through (3) of this section, and if applicable, paragraphs (b)(4) through (6) of this section.


(1) Company name and address.


(2) Statement by a responsible official, with the official’s name, title, and signature, certifying that, based on information and belief formed after reasonable inquiry, the statements and information in the report are true, accurate, and complete.


(3) Date of report and beginning and ending dates of the reporting period.


(4) For existing sources and for new or reconstructed sources for which construction or reconstruction commenced after October 18, 2002, but before May 4, 2018, before August 7, 2019, if you had a startup, shutdown, or malfunction during the reporting period and you took actions consistent with your startup, shutdown, and malfunction plan, the compliance report must include the information in § 63.10(d)(5)(i). A startup, shutdown, and malfunction plan is not required for such sources on and after August 7, 2019.


(5) If there were no deviations from the emission limitations for solvent mixers in § 63.9500(a) and (b), a statement that there were no deviations from the emission limitations during the reporting period.


(6) If there were no periods during which a monitoring system was out-of-control as specified in § 63.8(c)(7), a statement that there were no periods during which a monitoring system was out-of-control during the reporting period.


(c) For each deviation from an emission limitation occurring at an affected source, you must include the information in paragraphs (b)(1) through (4) and (c)(1) and (2) of this section. This includes periods of startup, shutdown, or malfunction.


(1) The total operating time of each affected source during the reporting period.


(2) For existing sources and for new or reconstructed sources which commenced construction or reconstruction after October 18, 2002, but before May 4, 2018, before August 7, 2019, information on the number, duration, and cause of deviations (including unknown cause, if applicable), as applicable, and the corrective action taken. On and after August 7, 2019 for such sources, and after February 8, 2019 for new or reconstructed sources which commenced construction or reconstruction after May 3, 2018, information on the number of deviations to meet an emission limitation. For each instance, include the date, time, duration, and cause of deviations (including unknown cause, if applicable), as applicable, a list of the affected source or equipment, an estimate of the quantity of each regulated pollutant emitted over any emission limit, and a description of the method used to estimate the emissions, and the corrective action taken.


(d) For existing sources and for new or reconstructed sources which commenced construction or reconstruction after October 18, 2002, but before May 4, 2018, before August 7, 2019, if you had a startup, shutdown, or malfunction during the semiannual reporting period that was not consistent with your startup, shutdown, and malfunction plan, you must submit an immediate startup, shutdown, and malfunction report according to the requirements in § 63.10(d)(5)(ii). An immediate startup, shutdown, and malfunction report is not required for such sources on and after August 7, 2019.


(e) If you have obtained a title V operating permit for an affected source pursuant to 40 CFR part 70 or 71 of this chapter, you must report all deviations as defined in this subpart in the semiannual monitoring report required by 40 CFR 70.6(a)(3)(iii)(A) or 40 CFR 71.6(a)(3)(iii)(A) of this chapter. If you submit a compliance report for an affected source along with, or as part of, the semiannual monitoring report required by 40 CFR 70.6(a)(3)(iii)(A) or 40 CFR 71.6(a)(3)(iii)(A) of this chapter, and the compliance report includes all the required information concerning deviations from any emission limitation in this subpart, then submission of the compliance report satisfies any obligation to report the same deviations in the semiannual monitoring report. However, submission of a compliance report does not otherwise affect any obligation you may have to report deviations from permit requirements to your permitting authority.


[67 FR 64506, Oct. 18, 2002, as amended at 84 FR 2751, Feb. 8, 2019]


§ 63.9545 What records must I keep?

(a) You must keep the records in paragraphs (a)(1) and (2) of this section that apply to you.


(1) A copy of each notification and report that you submitted to comply with this subpart, including all documentation supporting any initial notification or notification of compliance status that you submitted, according to the requirements in § 63.10(b)(2)(xiv).


(2) For existing sources and for new or reconstructed sources which commenced construction or reconstruction after October 18, 2002, but before May 4, 2018, before August 7, 2019, the records in § 63.6(e)(3)(iii) through (v) related to startup, shutdown, or malfunction. For such sources, it is not required to keep records in § 63.6(e)(3)(iii) through (v) related to startup, shutdown, or malfunction on and after August 7, 2019.


(3) After February 8, 2019 for new or reconstructed sources which commenced construction or reconstruction after May 3, 2018, and on and after August 7, 2019 for all other affected sources, in the event that an affected unit fails to meet an applicable standard, record the number of deviations. For each deviation, record the date, time and duration of each deviation.


(i) For each deviation, record and retain cause of deviations (including unknown cause, if applicable), a list of the affected source or equipment, an estimate of the quantity of each regulated pollutant emitted over any emission limit, and a description of the method used to estimate the emissions.


(ii) Record actions taken to minimize emissions in accordance with § 63.9505, and any corrective actions taken to return the affected unit to its normal or usual manner of operation.


(b) You must keep the records required in § 63.9525 to show proper operation and maintenance of the weight measurement device.


(c) You must keep the records required in § 63.9530 to show continuous compliance with the emission limitations for solvent mixers in § 63.9500(a) and (b).


[67 FR 64506, Oct. 18, 2002, as amended at 84 FR 2751, Feb. 8, 2019]


§ 63.9550 In what form and how long must I keep my records?

(a) You must keep your records in a form suitable and readily available for expeditious review, according to § 63.10(b)(1).


(b) As specified in § 63.10(b)(1), you must keep each record for 5 years following the date of each occurrence, measurement, maintenance, corrective action, report, or record.


(c) You must keep each record on site for at least 2 years after the date of each occurrence, measurement, maintenance, corrective action, report, or record, according to § 63.10(b)(1). You can keep the records offsite for the remaining 3 years.


Other Requirements and Information

§ 63.9555 What parts of the General Provisions apply to me?

Table 1 to this subpart shows which parts of the General Provisions in §§ 63.1 through 63.15 apply to you.


§ 63.9560 Who implements and enforces this subpart?

(a) This subpart can be implemented and enforced by the U.S. EPA, or a delegated authority such as your State, local, or tribal agency. If the U.S. EPA Administrator has delegated authority to your State, local, or tribal agency, then that agency, in addition to the U.S. EPA, has the authority to implement and enforce this subpart. You should contact your U.S. EPA Regional Office to find out if this subpart is delegated to your State, local, or tribal agency.


(b) In delegating implementation and enforcement authority of this subpart to a State, local, or tribal agency under 40 CFR part 63, subpart E, the authorities contained in paragraphs (c)(1) through (4) of this section are retained by the Administrator of the U.S. EPA and are not transferred to the State, local, or tribal agency.


(c) The authorities that cannot be delegated to State, local or tribal agencies are as follows:


(1) Approval of alternatives to the emission limitations in § 63.9500(a) and (b) under § 63.6(g).


(2) Approval of major alternatives to test methods under § 63.7(e)(2)(ii) and (f) and as defined in § 63.90.


(3) Approval of major alternatives to monitoring under § 63.8(f) and as defined in § 63.90.


(4) Approval of major alternatives to recordkeeping and reporting under § 63.10(f) and as defined in § 63.90.


§ 63.9565 What definitions apply to this subpart?

Terms used in this subpart are defined in the Clean Air Act, in § 63.2, and in this section as follows:


Batch ID means a unique identifier used to differentiate each individual mix batch.


Deviation means any instance in which an affected source subject to this subpart, or an owner or operator of such a source:


(1) Fails to meet any requirement or obligation established by this subpart, including, but not limited to, any emission limitation (including any operating limit);


(2) Fails to meet any term or condition that is adopted to implement an applicable requirement in this subpart and that is included in the operating permit for any affected source required to obtain such a permit; or


(3) Fails to meet any emission limitation (including any operating limit) in this subpart during startup, shutdown, or malfunction, regardless of whether or not such failure is permitted by this subpart.


Friction ingredients means any of the components used in the manufacture of friction materials, excluding the HAP solvent. Friction ingredients include, but are not limited to, reinforcement materials, property modifiers, resins, and other additives.


Friction materials manufacturing facility means a facility that manufactures friction materials using a solvent-based process. Friction materials are used in the manufacture of products used to accelerate or decelerate objects. Products that use friction materials include, but are not limited to, disc brake pucks, disc brake pads, brake linings, brake shoes, brake segments, brake blocks, brake discs, clutch facings, and clutches.


HAP solvent means a solvent that contains 10 percent or more of any one HAP, as listed in section 112(b) of the Clean Air Act, or any combination of HAP that is added to a solvent mixer. Examples include hexane, toluene, and trichloroethylene.


Initial startup means the first time that equipment is put into operation. Initial startup does not include operation solely for testing equipment. Initial startup does not include subsequent startups (as defined in this section) following malfunction or shutdowns or following changes in product or between batch operations.


Large solvent mixer means a solvent mixer with a design capacity greater than or equal to 2,000 pounds, including friction ingredients and HAP solvent.


Mix batch means each batch of friction materials manufactured in a solvent mixer.


Responsible official means responsible official as defined in § 63.2.


7-day block average means an averaging technique for a weekly compliance determination where the calculated values for percent HAP solvent discharged to the atmosphere are averaged together for all mix batches (for which there are valid data) in a 7-day block period according to the equation provided in § 63.9520(a)(6).


Small solvent mixer means a solvent mixer with a design capacity less than 2,000 pounds, including friction ingredients and HAP solvent.


Solvent mixer means a mixer used in the friction materials manufacturing process in which HAP solvent is used as one of the ingredients in at least one batch during a semiannual reporting period. Trace amounts of HAP solvents in resins or other friction ingredients do not qualify mixers as solvent mixers.


Solvent recovery system means equipment used for the purpose of recovering the HAP solvent from the exhaust stream. An example of a solvent recovery system is a condenser.


Solvent substitution means substitution of a non-HAP material for a HAP solvent.


Startup means bringing equipment online and starting the production process.


Startup, shutdown, and malfunction plan means a plan developed according to the provisions of § 63.6(e)(3).


§ 63.9570 How do I apply for alternative compliance requirements?

(a) If you use a control technique other than a solvent recovery system and/or solvent substitution, you may request approval to use an alternative method of demonstrating compliance with the emission limitations in § 63.9500(a) and (b) according to the procedures in this section.


(b) You can request approval to use an alternative method of demonstrating compliance in the initial notification for existing sources, the notification of construction or reconstruction for new sources, or at any time.


(c) You must submit a description of the proposed testing, monitoring, recordkeeping, and reporting that will be used and the proposed basis for demonstrating compliance.


(1) If you have not previously performed testing, you must submit a proposed test plan. If you are seeking permission to use an alternative method of compliance based on previously performed testing, you must submit the results of testing, a description of the procedures followed in testing, and a description of pertinent conditions during testing.


(2) You must submit a monitoring plan that includes a description of the control technique, test results verifying the performance of the control technique, the appropriate operating parameters that will be monitored, and the frequency of measuring and recording to establish continuous compliance with the emission limitations in § 63.9500(a) and (b). You must also include the proposed performance specifications and quality assurance procedures for the monitors. The monitoring plan is subject to the Administrator’s approval. You must install, calibrate, operate, and maintain the monitors in accordance with the monitoring plan approved by the Administrator.


(d) Use of the alternative method of demonstrating compliance must not begin until approval is granted by the Administrator.


§§ 63.9571-63.9579 [Reserved]

Table 1 to Subpart QQQQQ of Part 63—Applicability of General Provisions to Subpart QQQQQ

As required in § 63.9505, you must comply with each applicable General Provisions requirement according to the following table:


Citation
Subject
Applies to subpart

QQQQQ?
Explanation
§ 63.1ApplicabilityYes
§ 63.2DefinitionsYes
§ 63.3Units and AbbreviationsYes
§ 63.4Prohibited ActivitiesYes
§ 63.5Construction/ReconstructionYes
§ 63.6(a)-(c), (i)-(j)Compliance with Standards and Maintenance RequirementsYes
§ 63.6(d)[Reserved]
§ 63.6(e)(1)(i)-(ii)SSM Operation and Maintenance RequirementsNo, for new or reconstructed sources which commenced construction or reconstruction after May 3, 2018. Yes, for all other affected sources before August 7, 2019, and No thereafterSubpart QQQQQ requires affected units to meet emissions standards at all times. See § 63.9505 for general duty requirement.
§ 63.6(e)(1)(iii), (e)(2)Operation and MaintenanceYes
§ 63.6(e)(3)SSM Plan RequirementsNo, for new or reconstructed sources which commenced construction or reconstruction after May 3, 2018. Yes, for all other affected sources before August 7, 2019, and No thereafterSubpart QQQQQ requires affected units to meet emissions standards at all times.
§ 63.6(f)(1)SSM ExemptionNo, for new or reconstructed sources which commenced construction or reconstruction after May 3, 2018. Yes, for all other affected sources before August 7, 2019, and No thereafterSubpart QQQQQ requires affected units to meet emissions standards at all times.
§ 63.6(f)(2)-(3)Compliance with Nonopacity Emission StandardsYes
§ 63.6(g)Use of an Alternative Nonopacity Emission StandardNoSubpart QQQQQ contains no work practice standards.
§ 63.6(h)Compliance with Opacity and Visible Emission StandardsNoSubpart QQQQQ contains no opacity or VE limits.
§ 63.7(a)(1)-(2)Applicability and Performance Test DatesNoSubpart QQQQQ includes dates for initial compliance demonstrations.
§ 63.7(a)(3), (b)-(h)Performance Testing RequirementsNoSubpart QQQQQ does not require performance tests.
§ 63.8(a)(1)-(2)Applicability and Relevant Standards for CMSYes
§ 63.8(a)(3)[Reserved]
§ 63.8(a)(4)Additional Monitoring Requirements for Control Devices in § 63.11NoSubpart QQQQQ does not require flares.
§ 63.8(b)Conduct of MonitoringYes
§ 63.8(c)(1)(i), (iii)Continuous Monitoring System (CMS) SSM RequirementsNo, for new or reconstructed sources which commenced construction or reconstruction after May 3, 2018. Yes, for all other affected sources before August 7, 2019, and No thereafter.
§ 63.8(c)(1)(ii), (c)(2), (c)(3)CMS Repairs, Operating Parameters, and Performance TestsYes
§ 63.8(c)(4)Continuous Monitoring System (CMS) RequirementsNoSubpart QQQQQ does not require CMS.
§ 63.8(c)(5)Continuous Opacity Monitoring System (COMS) Minimum ProceduresNoSubpart QQQQQ does not require COMS.
§ 63.8(c)(6)Zero and High Level Calibration Check RequirementsNoSubpart QQQQQ specifies calibration requirements.
§ 63.8(c)(7)-(8)Out-of-Control PeriodsNoSubpart QQQQQ specifies out-of-control periods and reporting requirements.
§ 63.8(d)CMS Quality ControlNoSubpart QQQQQ requires a monitoring plan that specifies CMS quality control procedures.
§ 63.8(e)CMS Performance EvaluationNoSubpart QQQQQ does not require CMS performance evaluations.
§ 63.8(f)(1)-(5)Alternative Monitoring ProcedureYes
§ 63.8(f)(6)Relative Accuracy Test Audit (RATA) AlternativeNoSubpart QQQQQ does not require continuous emissions monitoring systems (CEMS).
§ 63.8(g)(1)-(5)Data ReductionNoSubpart QQQQQ specifies data reduction requirements.
§ 63.9(a)-(d), (h)-(j)Notification RequirementsYesExcept that subpart QQQQQ does not require performance tests or CMS performance evaluations.
§ 63.9(e)Notification of Performance TestNoSubpart QQQQQ does not require performance tests.
§ 63.9(f)Notification of VE/Opacity TestNoSubpart QQQQQ contains no opacity or VE limits.
§ 63.9(g)Additional Notifications When Using CMSNoSubpart QQQQQ does not require CMS performance evaluations.
§ 63.9(k)Electronic reporting proceduresYesOnly as specified in § 63.9(j).
§ 63.10(a), (b)(1), (d)(1), (d)(4), (e)(3), (f)Recordkeeping and Reporting RequirementsYes
§ 63.10(b)(2)(i), (ii), (iv), (v)Recordkeeping for Startup, Shutdown and MalfunctionNo, for new or reconstructed sources which commenced construction or reconstruction after May 3, 2018. Yes, for all other affected sources before August 7, 2019, and No thereafterSee § 63.9545 for recordkeeping requirements.
§ 63.10(b)(2)(iii), (vi)-(xiv)Owner/Operator Recordkeeping RequirementsYes
§ 63.10(c)(1)-(6), (9)-(15)Additional Records for CMSNoSubpart QQQQQ specifies record requirements.
§ 63.10(c)(7)-(8)Records of Excess Emissions and Parameter Monitoring Exceedances for CMSNoSubpart QQQQQ specifies record requirements.
§ 63.10(d)(2)Reporting Results of Performance TestsNoSubpart QQQQQ does not require performance tests.
§ 63.10(d)(3)Reporting Opacity or VE ObservationsNoSubpart QQQQQ contains no opacity or VE limits.
§ 63.10(d)(5)SSM reportsNo, for new or reconstructed sources which commenced construction or reconstruction after May 3, 2018. Yes, for all other affected sources before August 7, 2019, and No thereafterSee § 63.9540 for malfunction reporting requirements.
§ 63.10(e)(1)-(2)Additional CMS ReportsNoSubpart QQQQQ does not require CMS.
§ 63.10(e)(4)Reporting COMS DataNoSubpart QQQQQ does not require COMS.
§ 63.11Control Device RequirementsNoSubpart QQQQQ does not require flares.
§§ 63.12-63.15Delegation, Addresses, Incorporation by Reference Availability of InformationYes

[67 FR 64506, Oct. 18, 2002, as amended at 84 FR 2752, Feb. 8, 2019; 85 FR 73917, Nov. 19, 2020]


Subpart RRRRR—National Emission Standards for Hazardous Air Pollutants: Taconite Iron Ore Processing


Source:68 FR 61888, Oct. 30, 2003, unless otherwise noted.

What This Subpart Covers

§ 63.9580 What is the purpose of this subpart?

This subpart establishes national emission standards for hazardous air pollutants (NESHAP) for taconite iron ore processing. This subpart also establishes requirements to demonstrate initial and continuous compliance with all applicable emission limitations (emission limits and operating limits), work practice standards, and operation and maintenance requirements in this subpart.


§ 63.9581 Am I subject to this subpart?

You are subject to this subpart if you own or operate a taconite iron ore processing plant that is (or is part of) a major source of hazardous air pollutant (HAP) emissions. Your taconite iron ore processing plant is a major source of HAP if it emits or has the potential to emit any single HAP at a rate of 10 tons or more per year or any combination of HAP at a rate of 25 tons or more per year.


[85 FR 73917, Nov. 19, 2020]


§ 63.9582 What parts of my plant does this subpart cover?

(a) This subpart applies to each new and existing affected source at your taconite iron ore processing plant.


(b) The affected sources are each new or existing ore crushing and handling operation, ore dryer, indurating furnace, and finished pellet handling operation at your taconite iron ore processing plant, as defined in § 63.9652.


(c) This subpart covers emissions from ore crushing and handling emission units, ore dryer stacks, indurating furnace stacks, finished pellet handling emission units, and fugitive dust emissions.


(d) An ore crushing and handling operation, ore dryer, indurating furnace, or finished pellet handling operation at your taconite iron ore processing plant is existing if you commenced construction or reconstruction of the affected source before December 18, 2002.


(e) An ore crushing and handling operation, ore dryer, indurating furnace, or finished pellet handling operation at your taconite iron ore processing plant is new if you commence construction or reconstruction of the affected source on or after December 18, 2002. An affected source is reconstructed if it meets the definition of reconstruction in § 63.2.


§ 63.9583 When do I have to comply with this subpart?

(a) If you have an existing affected source, you must comply with each emission limitation, work practice standard, and operation and maintenance requirement in this subpart that applies to you no later than October 30, 2006, except as specified in paragraph (f) of this section.


(b) If you have a new affected source and its initial startup date is on or before October 30, 2003, you must comply with each emission limitation, work practice standard, and operation and maintenance requirement in this subpart that applies to you by October 30, 2003, except as specified in paragraph (f) of this section.


(c) If you have a new affected source and its initial startup date is after October 30, 2003, you must comply with each emission limitation, work practice standard, and operation and maintenance requirement in this subpart that applies to you upon initial startup, except as specified in paragraph (f) of this section.


(d) If your taconite iron ore processing plant is an area source that becomes a major source of HAP, the compliance dates in paragraphs (d)(1) and (2) of this section apply to you.


(1) Any portion of the taconite iron ore processing plant that is a new affected source or a new reconstructed source must be in compliance with this subpart upon startup.


(2) All other parts of the taconite iron ore processing plant must be in compliance with this subpart no later than 3 years after the plant becomes a major source.


(e) You must meet the notification and schedule requirements in § 63.9640. Several of these notifications must be submitted before the compliance date for your affected source.


(f) If you have an affected indurating furnace that commenced construction before May 15, 2023, you must comply with the requirements in paragraphs (f)(1) through (7) of this section by March 8, 2027. If you have an affected indurating furnace that commenced construction or reconstruction on or after May 15, 2023, you must comply with the requirements in paragraphs (f)(1) through (7) of this section by March 6, 2024 or the date of initial startup, whichever is later.


(1) All applicable emission limits for mercury, hydrogen chloride, and hydrogen fluoride in tables 2 and 3 to this subpart.


(2) All applicable operating limits in § 63.9590(b)(5) through (8), established in accordance with § 63.9622(g) through (i), for each control device used to comply with the mercury, hydrogen chloride, and hydrogen fluoride emission limits.


(3) All applicable compliance requirements in §§ 63.9600, 63.9610, 63.9623, 63.9625, and 63.9637(a).


(4) The applicable performance testing or continuous emissions monitoring system (CEMS) requirements for mercury in §§ 63.9620(k), 63.9621(d), and 63.9630.


(5) All applicable performance testing requirements in §§ 63.9620(l), 63.9621(d), and 63.9630.


(6) The requirements to install and maintain monitoring equipment in § 63.6332(g) through (i) and the monitoring requirements in §§ 63.9631, 63.9633, and 63.9634 for each control device used to comply with the mercury, hydrogen chloride and hydrogen fluoride emission limits.


(7) The notification, reporting and recordkeeping requirements in §§ 63.9640, 63.9641, 63.9642, and 63.9643 applicable to the mercury, hydrogen chloride, and hydrogen fluoride emission standards.


[89 FR 16424, Mar. 6, 2024]


Emission Limitations and Work Practice Standards

§ 63.9590 What emission limitations and operating limits must I meet?

(a) You must meet each emission limit in tables 1 through 3 to this subpart that applies to you by the applicable compliance date specified in § 63.9583.


(b) You must meet each applicable operating limit for control devices in paragraphs (b)(1) through (8) of this section that applies to you by the applicable compliance date specified in § 63.9583. You are not required to establish and comply with operating limits for control devices used to reduce mercury emissions when you are using a CEMS to monitor and demonstrate compliance with the mercury emission limit in table 2 to this subpart.


(1) Except as provided in paragraph (b)(2) of this section, for each wet scrubber applied to meet any particulate matter emission limit in table 1 to this subpart, you must maintain the daily average pressure drop and daily average scrubber water flow rate at or above the minimum levels established in § 63.9622.


(2) On or before January 28, 2022, for affected sources that commenced construction or reconstruction on or before September 25, 2019, for each dynamic wet scrubber applied to meet any particulate matter emission limit in table 1 to this subpart, you must maintain the daily average scrubber water flow rate and either the daily average fan amperage (a surrogate for fan speed as revolutions per minute) or the daily average pressure drop at or above the minimum levels established during the initial performance test. After January 28, 2022, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, for each dynamic wet scrubber applied to meet any particulate matter emission limit in table 1 to this subpart, you must maintain the daily average scrubber water flow rate and the daily average fan amperage (a surrogate for fan speed as revolutions per minute) at or above the minimum levels established in § 63.9622.


(3) For each dry electrostatic precipitator (ESP) applied to meet any particulate matter emission limit in Table 1 to this subpart, you must meet the operating limits in paragraph (b)(3)(i) or (ii) of this section.


(i) Maintain the 6-minute average opacity of emissions exiting the control device stack at or below the level established during the initial performance test.


(ii) Maintain the daily average secondary voltage and daily average secondary current for each field at or above the minimum levels established during the initial performance test.


(4) For each wet ESP applied to meet any particulate matter emission limit in table 1 to this subpart, you must meet the operating limits in paragraphs (b)(4)(i) through (iii) of this section.


(i) Maintain the daily average secondary voltage for each field at or above the minimum levels established during the initial performance test.


(ii) Maintain the daily average stack outlet temperature at or below the maximum levels established during the initial performance test.


(iii) Maintain the daily average water flow rate at or above the minimum levels established during the initial performance test.


(5) For each wet scrubber and wet ESP used to meet the hydrogen chloride and hydrogen fluoride emission limits in table 3 to this subpart, you must maintain the daily average scrubber water flow rate and pH greater than or equal to the operating limits established for these parameters established in § 63.9622.


(6) For each activated carbon injection (ACI) system used to meet the mercury emission limit in table 2 to this subpart, you must maintain the daily average activated carbon injection rate greater than or equal to the average activated carbon injection rate established during the most recent performance test demonstrating compliance with the applicable emission limit. In addition, you must maintain the daily average carrier gas flow rate greater than or equal to the average carrier gas flow rate established during the most recent performance test demonstrating compliance with the applicable emission limit.


(7) For each dry sorbent injection (DSI) system used to meet the hydrogen chloride and hydrogen fluoride emission limits in table 3 to this subpart, you must maintain the daily average dry sorbent injection rate greater than or equal to the average dry sorbent injection rate established during the most recent performance test. demonstrating compliance with the applicable emission limit. In addition, you must maintain the daily average carrier gas flow rate greater than or equal to the average carrier gas flow rate established during the most recent performance test demonstrating compliance with the applicable emission limit.


(8) If you use any air pollution control device other than a baghouse, wet scrubber, dynamic scrubber, dry ESP, wet ESP, ACI, or DSI, you must submit a site-specific monitoring plan in accordance with § 63.9631(f).


(c) You may petition the Administrator for approval of alternatives to the monitoring requirements in paragraphs (b)(1) through (7) of this section as allowed under § 63.8(f) and as defined in § 63.90.


[68 FR 61888, Oct. 30, 2003, as amended at 85 FR 45492, July 28, 2020; 89 FR 16425, Mar. 6, 2024]


§ 63.9591 What work practice standards must I meet?

(a) You must prepare, and at all times operate according to, a fugitive dust emissions control plan that describes in detail the measures that will be put in place to control fugitive dust emissions from the locations listed in paragraphs (a)(1) through (6) of this section.


(1) Stockpiles (includes, but is not limited to, stockpiles of uncrushed ore, crushed ore, or finished pellets);


(2) Material transfer points;


(3) Plant roadways;


(4) Tailings basin;


(5) Pellet loading areas; and


(6) Yard areas.


(b) A copy of your fugitive dust emissions control plan must be submitted for approval to the Administrator on or before the applicable compliance date for the affected source as specified in § 63.9583. The requirement for the plant to operate according to the fugitive dust emissions control plan must be incorporated by reference in the operating permit for the plant that is issued by the designated permitting authority under 40 CFR part 70 or 40 CFR part 71.


(c) You can use an existing fugitive dust emissions control plan provided it meets the requirements in paragraphs (c)(1) through (3) of this section.


(1) The plan satisfies the requirements of paragraph (a) of this section.


(2) The plan describes the current measures to control fugitive dust emission sources.


(3) The plan has been approved as part of a State implementation plan or title V permit.


(d) You must maintain a current copy of the fugitive dust emissions control plan onsite, and it must be available for inspection upon request. You must keep the plan for the life of the affected source or until the affected source is no longer subject to the requirements of this subpart.


Operation and Maintenance Requirements

§ 63.9600 What are my operation and maintenance requirements?

(a) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, you must always operate and maintain your affected source, including air pollution control and monitoring equipment, according to the provisions in § 63.6(e)(1)(i). After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, at all times, you must always operate and maintain any affected source, including associated air pollution control equipment and monitoring equipment, in a manner consistent with safety and good air pollution control practices for minimizing emissions. The general duty to minimize emissions does not require the owner or operator to make any further efforts to reduce emissions if levels required by the applicable standard have been achieved. Determination of whether such operation and maintenance procedures are being used will be based on information available to the Administrator which may include, but is not limited to, monitoring results, review of operation and maintenance procedures, review of operation and maintenance records, and inspection of the source.


(b) You must prepare, and at all times, operate according to, a written operation and maintenance plan for each control device applied to meet any particulate matter emission limit in table 1 to this subpart, mercury emission limit in table 2 to this subpart, hydrogen chloride and hydrogen fluoride emission limit in table 3 to this subpart, and to meet the requirement of each indurating furnace subject to good combustion practices (GCP). Each site-specific operation and maintenance plan must be submitted to the Administrator on or before the compliance date that is specified in § 63.9583 for your affected source. The plan you submit must explain why the chosen practices (i.e., quantified objectives) are effective in performing corrective actions or GCP in minimizing the formation of formaldehyde (and other products of incomplete combustion). The Administrator will review the adequacy of the site-specific practices and objectives you will follow and the records you will keep to demonstrate compliance with your Plan. If the Administrator determines that any portion of your operation and maintenance plan is not adequate, we can reject those portions of the plan, and request that you provide additional information addressing the relevant issues. In the interim of this process, you will continue to follow your current site-specific practices and objectives, as submitted, until your revisions are accepted as adequate by the Administrator. You must maintain a current copy of the operation and maintenance plan onsite, and it must be available for inspection upon request. You must keep the plan for the life of the affected source or until the affected source is no longer subject to the requirements of this subpart. Each operation and maintenance plan must address the elements in paragraphs (b)(1) through (4) of this section.


(1) Preventative maintenance for each control device, including a preventative maintenance schedule that is consistent with the manufacturer’s instructions for routine and long-term maintenance.


(2) Corrective action procedures for bag leak detection systems. On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, in the event a bag leak detection system alarm is triggered, you must initiate corrective action to determine the cause of the alarm within 1 hour of the alarm, initiate corrective action to correct the cause of the problem within 24 hours of the alarm, and complete the corrective action as soon as practicable. Corrective actions may include, but are not limited to, the actions listed in paragraphs (b)(2)(i) through (vi) of this section. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, in the event a bag leak detection system alarm is triggered, you must initiate corrective action to determine the cause of the alarm within 1 hour of the alarm, initiate corrective action to correct the cause of the problem within 24 hours of the alarm, and complete the corrective action as soon as practicable. If the alarm sounds more than 5 percent of the operating time during a 6-month period as determined according to § 63.9634(d)(3), it is considered an operating parameter deviation. Corrective actions may include, but are not limited to, the actions listed in paragraphs (b)(2)(i) through (vi) of this section.


(i) Inspecting the baghouse for air leaks, torn or broken bags or filter media, or any other condition that may cause an increase in emissions.


(ii) Sealing off defective bags or filter media.


(iii) Replacing defective bags or filter media or otherwise repairing the control device.


(iv) Sealing off a defective baghouse compartment.


(v) Cleaning the bag leak detection system probe, or otherwise repairing the bag leak detection system.


(vi) Adjusting the process operation producing the particulate emissions.


(3) Corrective action procedures for continuous parameter monitoring systems (CPMS) for all air pollution control devices except for baghouses. In the event you exceed an established operating limit for an air pollution control device except for a baghouse, you must initiate corrective action to determine the cause of the operating limit exceedance and complete the corrective action within 10 calendar days. The corrective action procedures you take must be consistent with the installation, operation, and maintenance procedures listed in your site-specific CPMS monitoring plan in accordance with § 63.9632(b).


(4) Good combustion practices for indurating furnaces. You must identify and implement a set of site-specific GCP for each type of indurating furnace at your plant. These GCP should correspond to your standard operating procedures for maintaining the proper and efficient combustion within each indurating furnace. Good combustion practices include, but are not limited to, the elements listed in paragraphs (b)(4)(i) through (v) of this section.


(i) Proper operating conditions for each indurating furnace (e.g., minimum combustion temperature, maximum carbon monoxide concentration in the furnace exhaust gases, burner alignment, or proper fuel-air distribution/mixing).


(ii) Routine inspection and preventative maintenance and corresponding schedules of each indurating furnace.


(iii) Performance analyses of each indurating furnace.


(iv) Keeping applicable operator logs.


(v) Keeping applicable records to document compliance with each element.


[68 FR 61888, Oct. 30, 2003, as amended at 85 FR 45492, July 28, 2020; 89 FR 16425, Mar. 6, 2024]


General Compliance Requirements

§ 63.9610 What are my general requirements for complying with this subpart?

(a) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, you must be in compliance with the requirements in paragraphs (a)(1) through (6) of this section at all times, except during periods of startup, shutdown, and malfunction. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, for affected sources that commenced construction or reconstruction after September 25, 2019, you must be in compliance with the emission limitations, standards, and operation and maintenance requirements for the particulate matter emission standards in this subpart at all times.


(1) The emission limitations in § 63.9590.


(2) The work practice standards in § 63.9591.


(3) The operation and maintenance requirements in § 63.9600.


(4) The notification requirements in § 63.9640.


(5) The reporting requirements in § 63.9641.


(6) The recordkeeping requirements in § 63.9642.


(b) During the period between the compliance date specified for your affected source in § 63.9583 and the date upon which continuous monitoring systems have been installed and certified and any applicable operating limits have been set, you must maintain a log detailing the operation and maintenance of the process and emissions control equipment. This includes the daily monitoring and recordkeeping of air pollution control device operating parameters as specified in § 63.9590(b).


(c) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, you must develop a written startup, shutdown, and malfunction plan according to the provisions in § 63.6(e)(3). For affected sources, a startup, shutdown, and malfunction plan is not required after January 25, 2021. No startup, shutdown, and malfunction plan is required for affected sources that commenced construction or reconstruction after September 25, 2019.


(d) On and after the applicable compliance date specified in § 63.9583(f), you must be in compliance with all applicable emission limitations for mercury, hydrogen chloride and hydrogen fluoride in tables 2 and 3 to this subpart and with the requirements in paragraphs (d)(1) through (6) of this section at all times.


(1) All applicable operating limits in § 63.9590(b)(5) through (8).


(2) All applicable operation and maintenance requirements in § 63.9600 for control devices and monitoring equipment used to comply with the emissions limits.


(3) The requirements in § 63.9631(j), if you use emissions averaging to demonstrate compliance with the mercury standards.


(4) The requirements in § 63.9631(k), if you use continuous emissions monitoring system(s) (CEMS) to demonstrate compliance with the mercury standards.


(5) The requirements in § 63.9634(n), if you elect to adjust the activated carbon injection rate based on the taconite pellet production rate.


(6) The notification, reporting and recordkeeping requirements in §§ 63.9640 through 63.9643.


[68 FR 61888, Oct. 30, 2003, as amended at 71 FR 20470, Apr. 20, 2006; 85 FR 45492, July 28, 2020; 89 FR 16426, Mar. 6, 2024]


Initial Compliance Requirements

§ 63.9620 On which units and by what date must I conduct performance tests or other initial compliance demonstrations?

(a) For each ore crushing and handling affected source, you must demonstrate initial compliance with the emission limits in Table 1 to this subpart by conducting an initial performance test for particulate matter as specified in paragraphs (a)(1) and (2) of this section.


(1) Except as provided in paragraph (e) of this section, an initial performance test must be performed on all stacks associated with ore crushing and handling.


(2) Initial performance tests must be completed no later than 180 calendar days after the compliance date specified in § 63.9583. Performance tests conducted between October 30, 2003 and no later than 180 days after the corresponding compliance date can be used for initial compliance demonstration, provided the tests meet the initial performance testing requirements of this subpart.


(b) For each indurating furnace affected source, you must demonstrate initial compliance with the emission limits in Table 1 to this subpart by conducting an initial performance test for particulate matter as specified in paragraphs (b)(1) and (2) of this section.


(1) An initial performance test must be performed on all stacks associated with each indurating furnace.


(2) Initial performance tests must be completed no later than 180 calendar days after the compliance date specified in § 63.9583. Performance tests conducted between October 30, 2003, and no later than 180 days after the corresponding compliance date can be used for initial compliance demonstration, provided the tests meet the initial performance testing requirements of this subpart. For an indurating furnace with multiple stacks, the performance tests for all stacks must be completed within 7 calendar days of commencement of the performance tests, to the extent practicable, and the indurating furnace and associated control device (where applicable) operating characteristics must remain representative and consistent for the duration of the stack tests. If you determine that the performance tests cannot be completed within 7 calendar days, the Administrator must be notified within 24 hours of making that determination.


(c) For each finished pellet handling affected source, you must demonstrate initial compliance with the emission limits in Table 1 to this subpart by conducting an initial performance test for particulate matter as specified in paragraphs (c)(1) and (2) of this section.


(1) Except as provided in paragraph (e) of this section, an initial performance test must be performed on all stacks associated with finished pellet handling.


(2) Initial performance tests must be completed no later than 180 calendar days after the compliance date specified in § 63.9583. Performance tests conducted between October 30, 2003 and no later than 180 days after the corresponding compliance date can be used for initial compliance demonstration, provided the tests meet the initial compliance testing requirements of this subpart.


(d) For each ore dryer affected source, you must demonstrate initial compliance with the emission limits in Table 1 to this subpart by conducting an initial performance test for particulate matter as specified in paragraphs (d)(1) and (2) of this section.


(1) An initial performance test must be performed on all stacks associated with each ore dryer.


(2) Initial performance tests must be completed no later than 180 calendar days after the compliance date specified in § 63.9583. Performance tests conducted between October 30, 2003 and no later than 180 days after the corresponding compliance date can be used for initial compliance demonstration, provided the tests meet the initial compliance testing requirements of this subpart. For ore dryers with multiple stacks, the performance tests for all stacks must be completed within a reasonable period of time, such that the ore dryer operating characteristics remain representative for the duration of the stack tests.


(e) For ore crushing and handling affected sources and finished pellet handling affected sources, in lieu of conducting initial performance tests for particulate matter on all stacks, you may elect to group a maximum of six similar emission units together and conduct an initial compliance test on one representative emission unit within each group of similar emission units. The determination of whether emission units are similar must meet the criteria in paragraph (f) of this section. If you decide to test representative emission units, you must prepare and submit a testing plan as described in paragraph (g) of this section.


(f) If you elect to test representative emission units as provided in paragraph (e) of this section, the units that are grouped together as similar units must meet the criteria in paragraphs (f)(1) and (2) of this section.


(1) All emission units within a group must be of the same process type (e.g., primary crushers, secondary crushers, tertiary crushers, fine crushers, ore conveyors, ore bins, ore screens, grate feed, pellet loadout, hearth layer, cooling stacks, pellet conveyor, and pellet screens). You cannot group emission units from different process types together for the purposes of this section.


(2) All emission units within a group must also have the same type of air pollution control device (e.g., wet scrubbers, dynamic wet scrubbers, rotoclones, multiclones, wet and dry ESP, and baghouses). You cannot group emission units with different air pollution control device types together for the purposes of this section.


(3) The site-specific operating limits established for the emission unit selected as representative of a group of similar emission units will be used as the operating limit for each emission unit within the group. The operating limit established for the representative unit must be met by each emission unit within the group.


(g) If you plan to conduct initial performance tests on representative emission units within an ore crushing and handling affected source or a finished pellet handling affected source, you must submit a testing plan for initial performance tests. This testing plan must be submitted to the Administrator or delegated authority no later than 90 days prior to the first scheduled initial performance test. The testing plan must contain the information specified in paragraphs (g)(1) through (3) of this section.


(1) A list of all emission units. This list must clearly identify all emission units that have been grouped together as similar emission units. Within each group of emission units, you must identify the emission unit that will be the representative unit for that group and subject to initial performance testing.


(2) A list of the process type and type of air pollution control device on each emission unit.


(3) A schedule indicating when you will conduct an initial performance test for particulate matter for each representative emission unit.


(h) For each work practice standard and operation and maintenance requirement that applies to you where initial compliance is not demonstrated using a performance test, you must demonstrate initial compliance within 30 calendar days after the compliance date that is specified for your affected source in § 63.9583.


(i) If you commenced construction or reconstruction of an affected source between December 18, 2002 and October 30, 2003 , you must demonstrate initial compliance with either the proposed emission limit or the promulgated emission limit no later than 180 calendar days after October 30, 2003 or no later than 180 calendar days after startup of the source, whichever is later, according to § 63.7(a)(2)(ix).


(j) If you commenced construction or reconstruction of an affected source between December 18, 2002 and October 30, 2003, and you chose to comply with the proposed emission limit when demonstrating initial compliance, you must conduct a second performance test to demonstrate compliance with the promulgated emission limit by 3 years and 180 calendar days after October 30, 2003, or after startup of the source, whichever is later, according to § 63.7(a)(2)(ix).


(k) For each indurating furnace, you must demonstrate initial compliance with the mercury emission limits in table 2 to this subpart in accordance with the procedures specified in either paragraph (k)(1) or (2) of this section.


(1) Complete an initial performance test on all stacks associated with each indurating furnace no later than 180 calendar days after the compliance date specified in § 63.9583(f). Performance tests conducted between March 6, 2024 and 180 days after the corresponding compliance date can be used for initial compliance demonstration, provided the tests meet the initial performance testing requirements of this subpart. For an indurating furnace with multiple stacks, the performance tests for all stacks must be completed within 7 calendar days of commencement of the performance tests, to the extent practicable, and the indurating furnace and associated control device (where applicable) operating characteristics must remain representative and consistent for the duration of the stack tests. If you determine that the performance tests cannot be completed within 7 calendar days, the Administrator must be notified within 24 hours of making that determination.


(2) You may use a 30-day rolling average of the 1-hour arithmetic average CEMS data. You must conduct a performance evaluation of each CEMS within 180 days of installation of the monitoring system. The initial performance evaluation must be conducted prior to collecting CEMS data that will be used for the initial compliance demonstration.


(l) For each indurating furnace, you must demonstrate initial compliance with the emission limits in table 3 to this subpart by conducting initial performance tests for hydrogen chloride and hydrogen fluoride on all stacks associated with each indurating furnace. Initial performance tests must be completed no later than 180 calendar days after the compliance date specified in § 63.9583(f). Performance tests conducted between March 6, 2024 and 180 days after the corresponding compliance date can be used for initial compliance demonstration, provided the tests meet the initial performance testing requirements of this subpart. For an indurating furnace with multiple stacks, the performance tests for all stacks must be completed within 7 calendar days of commencement of the performance tests, to the extent practicable, and the indurating furnace and associated control device (where applicable) operating characteristics must remain representative and consistent for the duration of the stack tests. If you determine that the performance tests cannot be conducted within 7 calendar days, the Administrator must be notified within 24 hours of making that determination.


[68 FR 61888, Oct. 30, 2003, as amended at 85 FR 45492, July 28, 2020; 89 FR 16426, Mar. 6, 2024]


§ 63.9621 What test methods and other procedures must I use to demonstrate initial compliance with the emission limits?

(a) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, you must conduct each performance test that applies to your affected source according to the requirements in § 63.7(e)(1) and paragraphs (b) and (c) of this section. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, you must conduct each performance test that applies to your affected source, including the initial performance tests for mercury required in § 63.9620(k)(1) and the initial performance tests for hydrogen chloride and hydrogen fluoride required in § 63.9620(l), under normal operating conditions of the affected source. The owner or operator may not conduct performance tests during periods of malfunction. The owner or operator must record the process information that is necessary to document operating conditions during the test and include in such record an explanation to support that such conditions represent normal operation. Upon request, the owner or operator shall make available to the Administrator such records as may be necessary to determine the conditions of performance tests. You must also conduct each performance test that applies to your affected source according to the requirements in paragraphs (b) and (c) of this section.


(b) For each ore crushing and handling affected source and each finished pellet handling affected source, you must determine compliance with the applicable emission limit for particulate matter in Table 1 to this subpart by following the test methods and procedures in paragraphs (b)(1) through (3) of this section.


(1) Except as provided in § 63.9620(e), determine the concentration of particulate matter in the stack gas for each emission unit according to the test methods listed in paragraphs (b)(1)(i) through (v) of this section.


(i) EPA Method 1 or 1A in appendix A-1 to part 60 of this chapter to select sampling port locations and the number of traverse points. Sampling ports must be located at the outlet of the control device and prior to any releases to the atmosphere.


(ii) EPA Method 2, 2A, 2C, 2D, or 2F in appendix A-1 to part 60 of this chapter or EPA Method 2G in appendix A-2 to part 60 of this chapter, as applicable, to determine the volumetric flow rate of the stack gas.


(iii) EPA Method 3A or 3B in appendix A-2 to part 60 of this chapter to determine the dry molecular weight of the stack gas. The voluntary consensus standard ANSI/ASME PTC 19.10-1981 (incorporated by reference-see § 63.14) may be used as an alternative to the manual procedures (but not instrumental procedures) in EPA Method 3B.


(iv) EPA Method 4 in appendix A-3 to part 60 of this chapter to determine the moisture content of the stack gas.


(v) EPA Method 5 or 5D in appendix A-3 to part 60 of this chapter or EPA Method 17 in appendix A-6 to part 60 of this chapter to determine the concentration of particulate matter.


(2) Each EPA Method 5, 5D, or 17 performance test must consist of three separate runs. Each run must be conducted for a minimum of 1 hour. If any measurement result is reported as below the method detection limit, use the method detection limit for that value when calculating the average particulate matter concentration. The average particulate matter concentration from the three runs will be used to determine compliance, as shown in Equation 1 of this section.




Where:

Ci = Average particulate matter concentration for emission unit, grains per dry standard cubic foot, (gr/dscf);

C1 = Particulate matter concentration for run 1 corresponding to emission unit, gr/dscf;

C2 = Particulate matter concentration for run 2 corresponding to emission unit, gr/dscf; and

C3 = Particulate matter concentration for run 3 corresponding to emission unit, gr/dscf.

(3) For each ore crushing and handling affected source and each finished pellet handling affected source, you must determine the flow-weighted mean concentration of particulate matter emissions from all emission units in each affected source following the procedure in paragraph (b)(3)(i) or (ii) of this section.


(i) If an initial performance test is conducted on all emission units within an affected source, calculate the flow-weighted mean concentration of particulate matter emissions from the affected source using Equation 2 of this section.





Where:

Ca = Flow-weighted mean concentration of particulate matter for all emission units within affected source, (gr/dscf);

Ci = Average particulate matter concentration measured during the performance test from emission unit “i” in affected source, as determined using Equation 1 of this section, gr/dscf;

Qi = Average volumetric flow rate of stack gas measured during the performance test from emission unit “i” in affected source, dscf/hr; and

n = Number of emission units in affected source.

(ii) If you are grouping similar emission units together in accordance with § 63.9620(e), you must follow the procedures in paragraphs (b)(3)(ii)(A) through (C) of this section.


(A) Assign the average particulate matter concentration measured from the representative unit, as determined from Equation 1 of this section, to each emission unit within the corresponding group of similar units.


(B) Establish the maximum operating volumetric flow rate of exhaust gas from each emission unit within each group of similar units.


(C) Using the data from paragraphs (b)(3)(ii)(A) and (B) of this section, calculate the flow-weighted mean concentration of particulate matter emissions from the affected source using Equation 3 of this section.





Where:

Ca = Flow-weighted mean concentration of particulate matter for all emission units within affected source, gr/dscf;

Ck = Average particulate matter concentration measured during the performance test from the representative emission unit in group “k” of affected source “a,” as determined using Equation 1 of this section, gr/dscf;

Qk = Sum of the maximum operating volumetric flow rates of stack gas from all similar emission units within group “k” of affected source, dscf/hr; and

m = Number of similar emission unit groups in affected source.

(c) For each ore dryer affected source and each indurating furnace affected source, you must determine compliance with the applicable emission limit for particulate matter in table 1 to this subpart by following the test methods and procedures in paragraphs (c)(1) through (2) of this section.


(1) Determine the concentration of particulate matter for each stack according to the test methods listed in paragraphs (c)(1)(i) through (v) of this section.


(i) EPA Method 1 or 1A in appendix A-1 to part 60 of this chapter to select sampling port locations and the number of traverse points. Sampling ports must be located at the outlet of the control device and prior to any releases to the atmosphere.


(ii) EPA Method 2, 2A, 2C, 2D, or 2F in appendix A-1 to part 60 of this chapter or EPA Method 2G in appendix A-2 to part 60 of this chapter, as applicable, to determine the volumetric flow rate of the stack gas.


(iii) EPA Method 3A or 3B in appendix A-2 to part 60 of this chapter to determine the dry molecular weight of the stack gas. The voluntary consensus standard ANSI/ASME PTC 19.10-1981 (incorporated by reference-see § 63.14) may be used as an alternative to the manual procedures (but not instrumental procedures) in EPA Method 3B.


(iv) EPA Method 4 in appendix A-3 to part 60 of this chapter to determine the moisture content of the stack gas.


(v) EPA Method 5 or 5D in appendix A-3 to part 60 of this chapter to determine the concentration of particulate matter.


(2) Each EPA Method 5 or 5D performance test must consist of three separate runs. Each run must be conducted for a minimum of 1 hour. If any measurement result is reported as below the method detection limit, use the method detection limit for that value when calculating the average particulate matter concentration. The average particulate matter concentration from the three runs will be used to determine compliance, as shown in Equation 1 of this section.


(d) For each indurating furnace subject to the initial performance testing under § 63.9620(k)(1) or (l), you must determine compliance with the applicable emission limits for mercury, hydrogen chloride and hydrogen fluoride in tables 2 and 3 to this subpart by following the test methods and procedures in paragraphs (d)(1) through (9) of this section. You are not required to complete the initial performance test for mercury emissions when you are using a CEMS in accordance with paragraph (e) of this section.


(1) The furnace must be operated at or above 90 percent of capacity throughout the duration of the performance testing. If testing cannot be performed at or above 90 percent of capacity, you must provide an explanation for the lower production rate in your performance test plan. The lower production rate must be approved by the Administrator prior to beginning performance testing. For indurating furnaces that comply with the mercury emissions limit in table 2 to this subpart by adjusting the activated carbon injection rate based on the taconite pellet production rate, you must complete the performance testing for mercury in accordance with the provisions in § 63.9634(n).


(2) Use the methods specified in paragraphs (c)(1)(i) through (iv) of this section to select sampling port locations and the number of traverse points and to determine the volumetric flow rate, dry molecular weight, and moisture content of the stack gas.


(3) Determine the concentration of mercury for each stack using Method 29 or Method 30B in 40 CFR part 60, appendix A, or the voluntary consensus standard ASTM D6784-16 (incorporated by reference, see § 63.14). For Method 29 and ASTM D6784-16, the sample volume must be at least 1.7 dry standard cubic meters (dscm) (60 dry standard cubic feet) per run. For Method 30B, each test run must be at least one hour in duration.


(4) Determine the concentration of hydrogen chloride and hydrogen fluoride for each stack using Method 26A in 40 CFR part 60, appendix A. Each test must consist of three separate runs. The minimum sample volume must be at least 2 dscm per run.


(5) During each stack test run, determine the weight of taconite pellets produced and calculate the emissions rate of each pollutant in pounds of pollutant per long ton (lb/LT) of pellets produced for each test run. The weight of taconite pellets produced must be determined by measurement using weigh hoppers, belt weigh feeders, or weighed quantities in shipments, or calculated using the bulk density and volume measurements. If any measurement result for any pollutant is reported as below the method detection limit, use the method detection limit as the measured emissions level for that pollutant when calculating the emission rate. If the furnace has more than one stack, calculate the total emissions rate for each test run by summing the emissions across all stacks, as shown in Equation 4.




Where:

Ef,i = Emissions rate for test run “i” for all emission stacks on indurating furnace “f”, lb/LT of pellets produced,

Cs = Emission rate for stack “s” measured during test run “i” on indurating furnace “f”, lb/dscf,

Qs = Average volumetric flow rate of stack gas measured at stack “s” during test run “i” on indurating furnace “f”, dscf/hour;

Pf = Pellets produced in indurating furnace “f” during the stack test, LT; and

n = Number of emissions stacks on furnace “f”.

(6) Calculate the average emissions rate for each furnace using the three test runs, as show in Equation 5 of this section.




Where:

Ef = Average emission rate for indurating furnace “f”, lb/LT of pellets produced,

E1 = Emissions rate for run 1 for indurating furnace “f”, lb/LT of pellets produced,

E2 = Emissions rate for run 2 for indurating furnace “f”, lb/LT of pellets produced, and

E3 = Emissions rate for run 3 for indurating furnace “f”, lb/LT of pellets produced.

(7) For each indurating furnace constructed or reconstructed on or after May 15, 2023, determine compliance with the applicable mercury emission limit in table 2 to this subpart by calculating the average emissions rate from the three test runs performed on the furnace using Equations 4 and 5 of this section.


(8) For each indurating furnace constructed or reconstructed before May 15, 2023, you must determine compliance with the applicable mercury emission limit in accordance with the procedures specified in either paragraph (d)(8)(i) or (ii) of this section.


(i) Determine compliance with the mercury limit for individual furnaces in table 2 to this subpart by calculating the average mercury emissions rate for each affected indurating furnace using Equations 4 and 5 of this section, or


(ii) Determine compliance with the mercury limit for groups of indurating furnaces in table 2 to this subpart in accordance with the method in § 63.9623(d).


(9) Determine compliance with the applicable hydrogen chloride and hydrogen fluoride emission limits in table 3 to this subpart by calculating the average emissions rate for each indurating furnace for the three test runs performed on the furnace using Equations 4 and 5 of this section.


(e) For each indurating furnace using mercury CEMS to demonstrate compliance with the applicable emission limits for mercury, you must determine compliance with the applicable mercury limit in table 2 to this subpart by using a 30-day rolling average of the 1-hour arithmetic average CEMS data, including CEMS data during startup and shutdown as defined in this subpart. The mercury CEMS must be installed, calibrated, maintained, and operated as accordance with the requirements in § 63.9631(j).


[68 FR 61888, Oct. 30, 2003, as amended at 85 FR 45492, July 28, 2020; 89 FR 16427, Mar. 6, 2024]


§ 63.9622 What test methods and other procedures must I use to establish and demonstrate initial compliance with the operating limits?

(a) For wet scrubbers subject to performance testing in § 63.9620 and operating limits for pressure drop and scrubber water flow rate in § 63.9590(b)(1), you must establish site-specific operating limits according to the procedures in paragraphs (a)(1) through (3) of this section.


(1) Using the CPMS required in § 63.9631(b), measure and record the pressure drop and scrubber water flow rate every 15 minutes during each run of the particulate matter performance test.


(2) Calculate and record the average pressure drop and scrubber water flow rate for each individual test run. Your operating limits are established as the lowest average pressure drop and the lowest average scrubber water flow rate corresponding to any of the three test runs, except as specified in paragraph (g)(2) of this section.


(3) If a rod-deck venturi scrubber is applied to an indurating furnace to meet any particulate matter emission limit in table 1 to this subpart, you may establish a lower average pressure drop operating limit by using historical average pressure drop data from a certified performance test completed on or after December 18, 2002 instead of using the average pressure drop value determined during the initial performance test, as specified in paragraph (a)(2) of this section. If historical average pressure drop data are used to establish an operating limit (i.e., using data from a certified performance test conducted prior to the promulgation date of the final rule), then the average particulate matter concentration corresponding to the historical performance test must be at or below the applicable indurating furnace emission limit, as listed in table 1 to this subpart.


(b) On or before January 28, 2022, for affected sources that commenced construction or reconstruction on or before September 25, 2019, for dynamic wet scrubbers subject to performance testing in § 63.9620 and operating limits for scrubber water flow rate and either fan amperage or pressure drop in § 63.9590(b)(2), you must establish site-specific operating limits according to the procedures in paragraphs (b)(1) and (2) of this section. After January 28, 2022, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, for dynamic wet scrubbers subject to performance testing in § 63.9620 and operating limits for scrubber water flow rate and fan amperage in § 63.9590(b)(2), you must establish site-specific operating limits according to the procedures in paragraphs (b)(1) and (2) of this section.


(1) On or before January 28, 2022, for affected sources that commenced construction or reconstruction on or before September 25, 2019, using the CPMS required in § 63.9631(b), measure and record the scrubber water flow rate and either the fan amperage or pressure drop every 15 minutes during each run of the particulate matter performance test. After January 28, 2022, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, using the CPMS required in § 63.9631(b), measure and record the scrubber water flow rate and the fan amperage every 15 minutes during each run of the particulate matter performance test.


(2) On or before January 28, 2022, for affected sources that commenced construction or reconstruction on or before September 25, 2019, calculate and record the average scrubber water flow rate and either the average fan amperage or the average pressure drop for each individual test run. Your operating limits are established as the lowest average scrubber water flow rate and either the lowest average fan amperage or pressure drop value corresponding to any of the three test runs. After January 28, 2022, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, calculate and record the average scrubber water flow rate and the average fan amperage for each individual test run. Your operating limits are established as the lowest average scrubber water flow rate and the lowest average fan amperage value corresponding to any of the three test runs, except as specified in paragraph (g)(2) of this section.


(c) For a dry ESP subject to performance testing in § 63.9620 and operating limits in § 63.9590(b)(3), you must establish a site-specific operating limit according to the procedures in paragraphs (c)(1) or (2) of this section.


(1) If the operating limit for your dry ESP is a 6-minute average opacity of emissions value, then you must follow the requirements in paragraphs (c)(1)(i) through (iii) of this section.


(i) Using the continuous opacity monitoring system (COMS) required in § 63.9631(d)(1), measure and record the opacity of emissions from each control device stack during the particulate matter performance test.


(ii) Compute and record the 6-minute opacity averages from 24 or more data points equally spaced over each 6-minute period (e.g., at 15-second intervals) during the test runs.


(iii) Using the opacity measurements from a performance test that meets the emission limit, determine the opacity value corresponding to the 99 percent upper confidence level of a normal distribution of the 6-minute opacity averages.


(2) If the operating limit for your dry ESP is the daily average secondary voltage and daily average secondary current for each field, then you must follow the requirements in paragraphs (c)(2)(i) and (ii) of this section.


(i) Using the CPMS required in § 63.9631(d)(2), measure and record the secondary voltage and secondary current for each dry ESP field every 15 minutes during each run of the particulate matter performance test.


(ii) Calculate and record the average secondary voltage and secondary current for each dry ESP field for each individual test run. Your operating limits are established as the lowest average secondary voltage and secondary current value for each dry ESP field corresponding to any of the three test runs.


(d) For a wet ESP subject to performance testing in § 63.9620 and operating limit in § 63.9590(b)(4), you must establish a site-specific operating limit according to the procedures in paragraphs (d)(1) and (2) of this section.


(1) Using the CPMS required in § 63.9631(e), measure and record the parametric values in paragraphs (d)(1)(i) through (iii) of this section for each wet ESP field every 15 minutes during each run of the particulate matter performance test.


(i) Secondary voltage;


(ii) Water flow rate; and


(iii) Stack outlet temperature.


(2) For each individual test run, calculate and record the average value for each operating parameter in paragraphs (d)(1)(i) through (iii) of this section for each wet ESP field. Your operating limits are established as the lowest average value for each operating parameter of secondary voltage and water flow rate corresponding to any of the three test runs, and the highest average value for each stack outlet temperature corresponding to any of the three test runs.


(e) If you use an air pollution control device other than a wet scrubber, dynamic wet scrubber, dry ESP, wet ESP, or baghouse, and it is subject to performance testing in § 63.9620, you must submit a site-specific monitoring plan in accordance with § 63.9631(f). The site-specific monitoring plan must include the site-specific procedures for demonstrating initial and continuous compliance with the corresponding operating limits.


(f) You may change the operating limits for any air pollution control device as long as you meet the requirements in paragraphs (f)(1) through (3) of this section.


(1) Submit a written notification to the Administrator of your request to conduct a new performance test to revise the operating limit.


(2) Conduct a performance test to demonstrate compliance with the applicable emission limitation in table 1 to this subpart.


(3) Establish revised operating limits according to the applicable procedures in paragraphs (a) through (e) of this section.


(g) For wet scrubbers and wet ESPs subject to performance testing in § 63.9620(l) and operating limits for scrubber water flow rate and pH in § 63.9590(b)(5), you must establish site-specific operating limits according to the procedures in paragraphs (g)(1) and (2) of this section.


(1) Using the CPMS required in § 63.9631(b), measure and record the scrubber water flow rate and pH of the scrubber water effluent every 15 minutes during each run of the performance test for hydrogen chloride and hydrogen fluoride.


(2) Calculate and record the average scrubber water flow rate and average pH of the scrubber water effluent for each individual test run. Your operating limit must be established as the average scrubber water flow rate and average pH of the scrubber water of the three test runs. If a higher average flow rate is measured during the most recent PM performance test, the operating limit for the daily average scrubber water flow rate is the average scrubber water flow rate measured during the most recent PM performance test. If a higher average flow rate is measured during the most recent HCl and HF performance test, the operating limit for the daily average scrubber water flow rate is the average scrubber water flow rate measured during the most recent HCl and HF performance test.


(h) For ACI systems subject to performance testing in § 63.9620(k)(1) and operating limits for activated carbon sorbent injection rate and carrier gas flow rate in § 63.9590(b)(6), you must establish site-specific operating limits according to the procedures in paragraphs (h)(1) and (2) of this section.


(1) Using the CPMS required in § 63.9631(b), measure and record the activated carbon injection rate and carrier gas flow rate every 15 minutes during each run of the performance test for mercury.


(2) Calculate and record the average activated carbon injection rate and carrier gas flow rate for each individual test run. Your operating limit must be established as the highest activated carbon injection rate and carrier gas flow rate of the three test runs.


(i) For DSI systems subject to performance testing in § 63.9620(l) and operating limits for sorbent injection rate and carrier gas flow rate in § 63.9590(b)(7), you must establish site-specific operating limits according to the procedures in paragraphs (i)(1) and (2) of this section.


(1) Using the CPMS required in § 63.9631(b), measure and record the sorbent injection rate and carrier gas flow rate every 15 minutes during each run of the performance test for hydrogen chloride and hydrogen fluoride.


(2) Calculate and record the average sorbent injection rate and carrier gas flow rate for each individual test run. Your operating limit must be established as the highest average sorbent injection rate and carrier gas flow rate of the three test runs.


[68 FR 61888, Oct. 30, 2003, as amended at 85 FR 45493, July 28, 2020; 89 FR 16428, Mar. 6, 2024]


§ 63.9623 How do I demonstrate initial compliance with the emission limitations that apply to me?

(a) For each affected source subject to an emission limit in tables 1 through 3 to this subpart, you must demonstrate initial compliance by meeting the emission limit requirements in paragraphs (a)(1) through (8) of this section by the compliance date specified in § 63.9583.


(1) For ore crushing and handling, the flow-weighted mean concentration of particulate matter, determined according to the procedures in §§ 63.9620(a) and 63.9621(b), must not exceed the emission limits in table 1 to this subpart.


(2) For indurating furnaces, the flow-weighted mean concentration of particulate matter, determined according to the procedures in §§ 63.9620(b) and 63.9621(c), must not exceed the emission limits in table 1 to this subpart.


(3) For finished pellet handling, the flow-weighted mean concentration of particulate matter, determined according to the procedures in §§ 63.9620(c) and 63.9621(b), must not exceed the emission limits in table 1 to this subpart.


(4) For ore dryers, the flow-weighted mean concentration of particulate matter, determined according to the procedures in §§ 63.9620(d) and 63.9621(c), must not exceed the emission limits in table 1 to this subpart.


(5) For indurating furnaces not using emissions averaging, the mercury emissions determined according to the procedures in §§ 63.9620(k)(1) or (2) and 63.9621(d), must not exceed the applicable emission limit in table 2 to this subpart.


(6) For indurating furnaces that comply with the mercury emissions limit using emissions averaging, the average mercury emissions determined according to the procedures in §§ 63.9620(k)(1) or (2), 63.9621(d) and 63.9634(m), must not exceed the applicable emission limit in table 2 to this subpart.


(7) For indurating furnaces that comply with the mercury emissions limit by adjusting the activated carbon injection rate based on the taconite pellet production rate, the mercury emissions determined according to the procedures in §§ 63.9620(k)(1) or (2), 63.9621(d) or (e), and 63.9634(n), must not exceed the applicable emission limit in table 2 to this subpart.


(8) For indurating furnaces, the hydrogen chloride and hydrogen fluoride emissions determined according to the procedures in §§ 63.9620(l) and 63.9621(d), must not exceed the applicable emission limit in table 3 to this subpart.


(b) For each affected source subject to an emission limit in table 1 to this subpart, you must demonstrate initial compliance by meeting the operating limit requirements in paragraphs (b)(1) through (5) of this section.


(1) For each wet scrubber subject to performance testing in § 63.9620 and operating limits for pressure drop and scrubber water flow rate in § 63.9590(b)(1), you have established appropriate site-specific operating limits and have a record of the pressure drop and scrubber water flow rate measured during the performance test in accordance with § 63.9622(a).


(2) On or before January 28, 2022, for affected sources that commenced construction or reconstruction on or before September 25, 2019, for each dynamic wet scrubber subject to performance testing in § 63.9620 and operating limits for scrubber water flow rate and either fan amperage or pressure drop in § 63.9590(b)(2), you have established appropriate site-specific operating limits and have a record of the scrubber water flow rate and either the fan amperage or pressure drop value, measured during the performance test in accordance with § 63.9622(b). After January 28, 2022, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, for each dynamic wet scrubber subject to performance testing in § 63.9620 and operating limits for scrubber water flow rate and fan amperage in § 63.9590(b)(2), you have established appropriate site-specific operating limits and have a record of the scrubber water flow rate and the fan amperage value, measured during the performance test in accordance with § 63.9622(b).


(3) For each dry ESP subject to performance testing in § 63.9620 and one of the operating limits in § 63.9590(b)(3), you must meet the requirements in paragraph (b)(3)(i) or (ii) of this section.


(i) If you are subject to the operating limit for opacity in § 63.9590(b)(3)(i), you have established appropriate site-specific operating limits and have a record of the opacity measured during the performance test in accordance with § 63.9622(c)(1).


(ii) If you are subject to the operating limit for secondary voltage and secondary current in § 63.9590(b)(3)(ii), you have established appropriate site-specific operating limits and have a record of the secondary voltage and secondary current measured during the performance test in accordance with § 63.9622(c)(2).


(4) For each wet ESP subject to performance testing in § 63.9620 and operating limits for secondary voltage, water flow rate, and stack outlet temperature in § 63.9590(b)(4), you have established appropriate site-specific operating limits and have a record of the secondary voltage, water flow rate, and stack outlet temperature measured during the performance test in accordance with § 63.9622(d).


(5) For other air pollution control devices subject to performance testing in § 63.9620 and operating limits in accordance with § 63.9590(b)(8), you have submitted a site-specific monitoring plan in accordance with § 63.9631(f) and have a record of the site-specific operating limits as measured during the performance test in accordance with § 63.9622(e).


(c) Except as specified in paragraph (e) of this section, you must demonstrate initial compliance with the emission limits in tables 2 and 3 to this subpart, by meeting the operating limit requirements in paragraphs (c)(1) through (3) of this section.


(1) For each wet scrubber and wet ESP subject to performance testing in § 63.9620(k) and operating limits for scrubber water flow rate and pH in § 63.9590(b)(5), you have established appropriate site-specific operating limits and have a record of the scrubber water flow rate and pH measured during the performance test in accordance with § 63.9622(g).


(2) For each ACI subject to performance testing in § 63.9620(k) and operating limits for activated carbon injection rate and carrier gas flow rate in § 63.9590(b)(6), you have established appropriate site-specific operating limits and have a record of the activated carbon injection rate and carrier gas flow rate measured during the performance test in accordance with § 63.9622(i).(3) For each DSI subject to performance testing in § 63.9620(k) and operating limits for sorbent injection rate and carrier gas flow rate in § 63.9590(b)(7), you have established appropriate site-specific operating limit and have a record of the sorbent injection rate and carrier gas flow rate measured during the performance test in accordance with § 63.9622(h).


(d) If you elect to comply with the mercury limit in table 2 to this subpart using emissions averaging for indurating furnaces constructed or reconstructed before May 15, 2023, you must comply with the requirements in paragraphs (d)(1) through (4) of this section.


(1) Before submitting the implementation plan required in paragraph (d)(3) of this section, you must complete the mercury stack testing required in § 63.9620(k)(1) or install, calibrate, and operate a mercury CEMS pursuant to § 63.9620(k)(2) and paragraph (e) of this section for all indurating furnaces you wish to include in the mercury emission average.


(2) You must develop and submit to the applicable regulatory authority for review and approval, an implementation plan for mercury emission averaging no later than 180 days before the date you intend to demonstrate compliance using the emission averaging option. You must include the information contained in paragraphs (d)(2)(i) through (iii) of this section in your implementation plan.


(i) Identification of all indurating furnaces in the averaging group, including the typical taconite pellet production rate, control technology installed, and types of fuel(s) that will be burned.


(ii) The mercury emission rate for each furnace for each of the fuels identified in paragraph (d)(2)(i) of this section.


(iii) The date on which you are requesting emission averaging to commence.


(3) The regulatory authority shall review and approve or disapprove the plan according to the following criteria:


(i) Whether the content of the plan includes all the information specified in paragraph (d)(2) of this section, and


(ii) Whether the plan presents sufficient information to determine that compliance will be achieved and maintained.


(4) The applicable regulatory authority shall not approve an emission averaging implementation plan containing any of the following provisions:


(i) Averaging that includes indurating furnaces constructed or reconstructed on or after May 15, 2023, or


(ii) Averaging between indurating furnaces located at different facilities.


(e) If you elect to demonstrate compliance with the mercury limit in table 2 to this subpart using a mercury CEMS, you must calculate the 30-day rolling average of 1-hour arithmetic average emission concentrations, including CEMS data during startup and shutdown, calculated using equation 19-19 in section 12.4.1 of EPA Reference Method 19 at appendix A-7 of 40 CFR part 60. The 1-hour arithmetic averages for CEMS must be calculated using the data points required under § 63.8(c)(4)(ii).


(f) For each emission limitation and operating limit that applies to you, you must submit a notification of compliance status according to § 63.9640(e)


[68 FR 61888, Oct. 30, 2003, as amended at 85 FR 45494, July 28, 2020;89 FR 16429, Mar. 6, 2024]


§ 63.9624 How do I demonstrate initial compliance with the work practice standards that apply to me?

You must demonstrate initial compliance with the work practice standards by meeting the requirements in paragraphs (a) through (c) of this section.


(a) You must prepare a fugitive dust emissions control plan in accordance with the requirements in § 63.9591.


(b) You must submit to the Administrator the fugitive dust emissions control plan in accordance with the requirements in § 63.9591.


(c) You must implement each control practice according to the procedures specified in your fugitive dust emissions control plan.


§ 63.9625 How do I demonstrate initial compliance with the operation and maintenance requirements that apply to me?

For each air pollution control device subject to operating limits in § 63.9590(b), you have demonstrated initial compliance with the operation and maintenance requirements if you meet all of the requirements in paragraphs (a) through (d) of this section.


(a) You have prepared the operation and maintenance plan for air pollution control devices in accordance with § 63.9600(b).


(b) You have operated each air pollution control device according to the procedures in the operation and maintenance plan.


(c) You have submitted a notification of compliance status according to the requirements in § 63.9640(e).


(d) You have prepared a site-specific monitoring plan in accordance with § 63.9632(b).


[68 FR 61888, Oct. 30, 2003, as amended at 85 FR 45494, July 28, 2020]


Continuous Compliance Requirements

§ 63.9630 When must I conduct subsequent performance tests?

(a) You must conduct subsequent performance tests to demonstrate continued compliance with the ore crushing and handling emission limits in Table 1 to this subpart according to the schedule developed by your permitting authority and shown in your title V permit. If a title V permit has not been issued, you must submit a testing plan and schedule, containing the information specified in paragraph (e) of this section, to the permitting authority for approval.


(b) You must conduct subsequent performance tests on all stacks associated with indurating furnaces to demonstrate continued compliance with the indurating furnace emission limits in tables 1 through 3 to this subpart according to the schedule developed by your permitting authority and shown in your title V permit, but no less frequent than twice per 5-year permit term. If a title V permit has not been issued, you must submit a testing plan and schedule, containing the information specified in paragraph (e) of this section, to the permitting authority for approval. For an indurating furnace with multiple stacks, the performance tests for all stacks must be conducted within 7 calendar days of commencement of the performance tests, to the extent practicable, and the indurating furnace and associated control device (where applicable) operating characteristics must remain representative and consistent for the duration of the stack tests. If you determine that the performance tests cannot be completed within 7 calendar days, the Administrator must be notified within 24 hours of making that determination. Performance testing for mercury is not required for furnaces using CEMS to demonstrate compliance with the mercury emission limits in table 2 to this subpart.


(c) You must conduct subsequent performance tests to demonstrate continued compliance with the finished pellet handling emission limits in Table 1 to this subpart according to the schedule developed by your permitting authority and shown in your title V permit. If a title V permit has not been issued, you must submit a testing plan and schedule, containing the information specified in paragraph (e) of this section, to the permitting authority for approval.


(d) You must conduct subsequent performance tests on all stacks associated with ore dryers to demonstrate continued compliance with the ore dryer emission limits in Table 1 to this subpart according to the schedule developed by your permitting authority and shown in your title V permit. If a title V permit has not been issued, you must submit a testing plan and schedule, containing the information specified in paragraph (e) of this section, to the permitting authority for approval. For ore dryers with multiple stacks, the performance tests for all stacks associated with an ore dryer must be conducted within a reasonable period of time, such that the ore dryer operating characteristics remain representative for the duration of the stack tests.


(e) If your plant does not have a title V permit, you must submit a testing plan for subsequent performance tests as required in paragraphs (a) through (d) of this section. This testing plan must be submitted to the Administrator on or before the compliance date that is specified in § 63.9583. The testing plan must contain the information specified in paragraphs (e)(1) and (2) of this section. You must maintain a current copy of the testing plan onsite, and it must be available for inspection upon request. You must keep the plan for the life of the affected source or until the affected source is no longer subject to the requirements of this subpart.


(1) A list of all emission units.


(2) A schedule indicating when you will conduct subsequent performance tests for particulate matter, mercury, hydrogen chloride and hydrogen fluoride for each of the emission units.


[68 FR 61888, Oct. 30, 2003, as amended at 89 FR 16431, Mar. 6, 2024]


§ 63.9631 What are my monitoring requirements?

(a) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, for each baghouse applied to meet any particulate matter emission limit in Table 1 to this subpart, you must install, operate, and maintain a bag leak detection system to monitor the relative change in particulate matter loadings according to the requirements in § 63.9632(a), and conduct inspections at their specified frequencies according to the requirements in paragraphs (a)(1) through (8) of this section. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, for each baghouse applied to meet any particulate matter emission limit in Table 1 to this subpart, you must install, operate, and maintain a bag leak detection system to monitor the relative change in particulate matter loadings according to the requirements in § 63.9632(a), and conduct inspections at their specified frequencies according to the requirements in paragraphs (a)(1) through (6) and (8) of this section. For each baghouse applied to meet any particulate matter emission limit in Table 1 to this subpart that is not required by § 63.9632(a) to be equipped with a bag leak detection system, you must conduct inspections at their specified frequencies according to the requirements in paragraphs (a)(1) through (8) of this section.


(1) Monitor the pressure drop across each baghouse cell each day to ensure pressure drop is within the normal operating range.


(2) Confirm that dust is being removed from hoppers through weekly visual inspections or other means of ensuring the proper functioning of removal mechanisms.


(3) Check the compressed air supply of pulse-jet baghouses each day.


(4) Monitor cleaning cycles to ensure proper operation using an appropriate methodology.


(5) Check bag cleaning mechanisms for proper functioning through monthly visual inspections or equivalent means.


(6) Make monthly visual checks of bag tension on reverse air and shaker-type baghouses to ensure that bags are not kinked (kneed or bent) or lying on their sides. You do not have to make this check for shaker-type baghouses that have self-tensioning (spring-loaded) devices.


(7) Confirm the physical integrity of the baghouse through quarterly visual inspections of the baghouse interior for air leaks.


(8) Inspect fans for wear, material buildup, and corrosion through quarterly visual inspections, vibration detectors, or equivalent means.


(b) Except as provided in paragraph (c) of this section, for each wet scrubber subject to the operating limits for pressure drop and scrubber water flow rate in § 63.9590(b)(1), you must install, operate, and maintain a CPMS according to the requirements in § 63.9632(b) through (e) and monitor the daily average pressure drop and daily average scrubber water flow rate according to the requirements in § 63.9633.


(c) On or before January 28, 2022, for affected sources that commenced construction or reconstruction on or before September 25, 2019, for each dynamic wet scrubber subject to the scrubber water flow rate and either the fan amperage or pressure drop operating limits in § 63.9590(b)(2), you must install, operate, and maintain a CPMS according to the requirements in § 63.9632(b) through (e) and monitor the daily average scrubber water flow rate and either the daily average fan amperage or the daily average pressure drop according to the requirements in § 63.9633. After January 28, 2022, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, for each dynamic wet scrubber subject to the scrubber water flow rate and the fan amperage operating limits in § 63.9590(b)(2), you must install, operate, and maintain a CPMS according to the requirements in § 63.9632(b) through (e) and monitor the daily average scrubber water flow rate and the daily average fan amperage according to the requirements in § 63.9633.


(d) For each dry ESP subject to the operating limits in § 63.9590(b)(3), you must follow the monitoring requirements in paragraph (d)(1) or (2) of this section.


(1) If the operating limit you choose to monitor is the 6-minute average opacity of emissions in accordance with § 63.9590(b)(3)(i), you must install, operate, and maintain a COMS according to the requirements in § 63.9632(f) and monitor the 6-minute average opacity of emissions exiting each control device stack according to the requirements in § 63.9633.


(2) If the operating limit you choose to monitor is average secondary voltage and average secondary current for each dry ESP field in accordance with § 63.9590(b)(3)(ii), you must install, operate, and maintain a CPMS according to the requirements in § 63.9632(b) through (e) and monitor the daily average secondary voltage and daily average secondary current according to the requirements in § 63.9633.


(e) For each wet ESP subject to the operating limits in § 63.9590(b)(4), you must install, operate, and maintain a CPMS according to the requirements in § 63.9632(b) through (e) and monitor the daily average secondary voltage, daily average stack outlet temperature, and daily average water flow rate according to the requirements in § 63.9633.


(f) For each wet scrubber and wet ESP subject to the operating limits in § 63.9590(b)(5), you must install, operate, and maintain a CPMS according to the requirements in § 63.9632(g) and monitor the daily average scrubber water flow rate and pH of the scrubber water effluent.


(g) For each ACI system subject to the operating limits in § 63.9590(b)(6), you must install, operate, and maintain a CPMS according to the requirements in § 63.9632(h) and (i) and monitor the daily average activated carbon injection rate and carrier gas flow rate.


(h) For each DSI system subject to the operating limits in § 63.9590(b)(7), you must install, operate, and maintain a CPMS according to the requirements in § 63.9632(h) and (i) and monitor the daily average sorbent injection rate and carrier gas flow rate.


(i) If you use any air pollution control device other than a baghouse, wet scrubber, dry ESP, wet ESP, DSI, or ACI, you must submit a site-specific monitoring plan that includes the information in paragraphs (i)(1) through (4) of this section. The monitoring plan is subject to approval by the Administrator. You must maintain a current copy of the monitoring plan onsite, and it must be available for inspection upon request. You must keep the plan for the life of the affected source or until the affected source is no longer subject to the requirements of this subpart.


(1) A description of the device.


(2) Test results collected in accordance with § 63.9621 verifying the performance of the device for reducing emissions of particulate matter, mercury, hydrogen chloride, and hydrogen fluoride to the atmosphere to the levels required by this subpart.


(3) A copy of the operation and maintenance plan required in § 63.9600(b).


(4) Appropriate operating parameters that will be monitored to maintain continuous compliance with the applicable emission limitation(s).


(j) If you elect to comply with the mercury limit in table 2 to this subpart using emissions averaging in accordance with an implementation plan approved under the provisions in § 63.9623(d) or you elect to adjust the activated carbon injection rate based on the taconite pellet production rate in accordance with the procedures in § 63.9634(n), you must determine and record the mass of taconite pellets produced each month by each furnace included in the emissions averaging group. The weight of taconite pellets produced must be determined by measurement using weigh hoppers, belt weigh feeders, or weighed quantities in shipments, or calculated using the bulk density and volume measurements.


(k) If you elect to demonstrate compliance with the mercury emissions limits in table 2 to this subpart using a CEMS to measure mercury emissions, you must comply with the requirements in (k)(1) through (5).


(1) Notify the Administrator one month before starting use of the CEMS and notify the Administrator 180-days before ceasing use of the CEMS.


(2) Each CEMS must be installed, certified, calibrated, and maintained according to the requirements of performance specifications 6 and 12A of 40 CFR part 60, appendix B, and quality assurance procedure 6 of 40 CFR part 60, appendix F.


(3) Operate the mercury CEMS in accordance with performance specification 12A of 40 CFR part 60, appendix B. The duration of the performance test must be 30 operating days. For each day in which the unit operates, you must obtain hourly mercury concentration data, and stack gas volumetric flow rate data.


(4) You must complete the initial performance evaluation of the CEMS within 180 days after notifying the Administrator and before starting to use the CEMS data in lieu of performance testing and monitoring operating parameters to demonstrate compliance.


(5) Collect CEMS hourly averages for all operating hours on a 30-day rolling average basis. The one-hour arithmetic averages, expressed in units of lb/LT, must be used to calculate 30-day rolling average emissions to determine compliance with the applicable emission limit in table 2 to this subpart.


[68 FR 61888, Oct. 30, 2003, as amended at 85 FR 45494, July 28, 2020; 89 FR 16431, Mar. 6, 2024]


§ 63.9632 What are the installation, operation, and maintenance requirements for my monitoring equipment?

(a) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, for each negative pressure baghouse or positive pressure baghouse equipped with a stack, applied to meet any particulate emission limit in Table 1 to this subpart, you must install, operate, and maintain a bag leak detection system for each exhaust stack according to the requirements in paragraphs (a)(1) and (2) and (a)(4) through (9) of this section. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, for each negative pressure baghouse or positive pressure baghouse equipped with a stack, applied to meet any particulate emission limit in Table 1 to this subpart, you must install, operate, and maintain a bag leak detection system for each exhaust stack according to the requirements in paragraphs (a)(1) through (9) of this section.


(1) The system must be certified by the manufacturer to be capable of detecting emissions of particulate matter at concentrations of 10 milligrams per actual cubic meter (0.0044 grains per actual cubic foot) or less.


(2) The system must provide output of relative changes in particulate matter loadings.


(3) The bag leak detection system must be equipped with a device to continuously record the output signal from the sensor.


(4) The system must be equipped with an alarm that will sound when an increase in relative particulate loadings is detected over the alarm level set point established according to paragraph (a)(5) of this section. The alarm must be located such that it can be heard by the appropriate plant personnel.


(5) For each bag leak detection system, you must develop and submit to the Administrator for approval, a site-specific monitoring plan that addresses the items identified in paragraphs (a)(5)(i) through (v) of this section. The monitoring plan shall be consistent with the manufacturer’s specifications and recommendations contained in the U.S. Environmental Protection Agency (U.S. EPA) guidance document, “Fabric Filter Bag Leak Detection Guidance” (EPA-454/R-98-015) (incorporated by reference—see § 63.14). You must operate and maintain the bag leak detection system according to the site-specific monitoring plan at all times. The plan shall describe all of the items in paragraphs (a)(5)(i) through (v) of this section.


(i) Installation of the bag leak detection system.


(ii) Initial and periodic adjustment of the bag leak detection system including how the alarm set-point will be established.


(iii) Operation of the bag leak detection system including quality assurance procedures.


(iv) How the bag leak detection system will be maintained including a routine maintenance schedule and spare parts inventory list.


(v) How the bag leak detection system output shall be recorded and stored.


(6) To make the initial adjustment of the system, establish the baseline output by adjusting the sensitivity (range) and the averaging period of the device. Then, establish the alarm set points and the alarm delay time (if applicable).


(7) Following initial adjustment, do not adjust sensitivity or range, averaging period, alarm set point, or alarm delay time, without approval from the Administrator except as provided for in paragraph (a)(7)(i) of this section. In no event may the sensitivity be increased more than 100 percent or decreased by more than 50 percent over a 365-day period unless such adjustment follows a complete baghouse inspection that demonstrates the baghouse is in good operating condition.


(i) Once per quarter, you may adjust the sensitivity or range of the bag leak detection system to account for seasonal effects, including temperature and humidity, according to the procedures identified in the site-specific monitoring plan required under paragraph (a)(5) of this section.


(ii) [Reserved]


(8) Where multiple detectors are required, the system’s instrumentation and alarm may be shared among detectors.


(9) The bag leak detector sensor must be installed downstream of the baghouse and upstream of any wet scrubber.


(b) For each CPMS required in § 63.9631, you must develop and make available for inspection upon request by the permitting authority a site-specific monitoring plan that addresses the requirements in paragraphs (b)(1) through (7) of this section.


(1) Installation of the CPMS sampling probe or other interface at a measurement location relative to each affected emission unit such that the measurement is representative of control of the exhaust emissions (e.g., on or downstream of the last control device).


(2) Performance and equipment specifications for the sample interface, the parametric signal analyzer, and the data collection and reduction system.


(3) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, performance evaluation procedures and acceptance criteria (e.g., calibrations). After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, performance evaluation procedures, a schedule for performing such procedures, and acceptance criteria (e.g., calibrations), as well as corrective action to be taken if a performance evaluation does not meet the acceptance criteria. If a CPMS calibration fails, the CPMS is considered to be inoperative until you take corrective action and the system passes calibration.


(4) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, ongoing operation and maintenance procedures in accordance with the general requirements of § 63.8(c)(1), (3), (4)(ii), (7), and (8). After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, ongoing operation and maintenance procedures and a schedule for preventative maintenance procedures, in a manner consistent with good air pollution control practices and in accordance with the general requirements of § 63.8(c)(1)(ii), (c)(3), (c)(4)(ii), and (c)(7) and (8).


(5) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, ongoing data quality assurance procedures in accordance with the general requirements of § 63.8(d). After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, ongoing data quality assurance procedures in accordance with the general requirements of § 63.8(d)(1) and (2). The owner or operator shall keep these written procedures on record for the life of the affected source or until the affected source is no longer subject to the provisions of this part, to be made available for inspection, upon request, by the Administrator. If the performance evaluation plan is revised, the owner or operator shall keep previous (i.e., superseded) versions of the performance evaluation plan on record to be made available for inspection, upon request, by the Administrator, for a period of 5 years after each revision to the plan.


(6) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, ongoing recordkeeping and reporting procedures in accordance with the general requirements of § 63.10(c), (e)(1), and (e)(2)(i). After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, ongoing recordkeeping and reporting procedures in accordance with the general requirements of § 63.10(c)(1) through (14), (e)(1), and (e)(2)(i).


(7) Corrective action procedures that you will follow in the event an air pollution control device, except for a baghouse, exceeds an established operating limit as required in § 63.9600(b)(3).


(c) Unless otherwise specified, each CPMS must meet the requirements in paragraphs (c)(1) and (2) of this section.


(1) Each CPMS must complete a minimum of one cycle of operation for each successive 15-minute period and must have valid data for at least 95 percent of every daily averaging period.


(2) Each CPMS must determine and record the daily average of all recorded readings.


(d) You must conduct a performance evaluation of each CPMS in accordance with your site-specific monitoring plan.


(e) You must operate and maintain the CPMS in continuous operation according to the site-specific monitoring plan.


(f) For each dry ESP subject to the opacity operating limit in § 63.9590(b)(3)(i), you must install, operate, and maintain each COMS according to the requirements in paragraphs (f)(1) through (4) of this section.


(1) You must install each COMS and conduct a performance evaluation of each COMS according to § 63.8 and Performance Specification 1 in appendix B to 40 CFR part 60.


(2) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, you must develop and implement a quality control program for operating and maintaining each COMS according to § 63.8. At a minimum, the quality control program must include a daily calibration drift assessment, quarterly performance audit, and annual zero alignment of each COMS. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, you must develop and implement a quality control program for operating and maintaining each COMS according to § 63.8(a) and (b), (c)(1)(ii), (c)(2) through (8), (d)(1) and (2), and (e) through (g) and Procedure 3 in appendix F to 40 CFR part 60. At a minimum, the quality control program must include a daily calibration drift assessment, quarterly performance audit, and annual zero alignment of each COMS.


(3) You must operate and maintain each COMS according to § 63.8(e) and your quality control program. You must also identify periods the COMS is out of control, including any periods that the COMS fails to pass a daily calibration drift assessment, quarterly performance audit, or annual zero alignment audit.


(4) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, you must determine and record the 6-minute average opacity for periods during which the COMS is not out of control. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, you must determine and record the 6-minute average opacity for periods during which the COMS is not out of control. All COMS must complete a minimum of one cycle of sampling and analyzing for each successive 10-second period and one cycle of data recording for each successive 6-minute period.


(g) For each pH measurement device, in addition to the requirements in paragraphs (b) through (e) of this section, you must meet the requirements in paragraphs (g)(1) through (4) of this section.


(1) The minimum accuracy of the pH measurement device must be ±0.2 pH units.


(2) Locate the pH sensor in a position that provides a representative measurement of scrubber effluent pH.


(3) Ensure the sample is properly mixed and representative of the fluid to be measured.


(4) Check the pH meter’s calibration on at least two points every 8 hours of process operation.


(h) For each mass flow rate monitor used for measuring the sorbent or activated carbon injection rate, in addition to the requirements in paragraphs (b) through (e) of this section, you must meet the requirements of (h)(1) through (4) of this section.


(1) The minimum accuracy of the mass flow rate monitor must be ±5 percent over the normal range of flow measured.


(2) Locate the device in a position(s) that provides a representative measurement of the total sorbent injection rate.


(3) Install and calibrate the device in accordance with manufacturer’s procedures and specifications.


(4) At least annually, conduct a performance evaluation of the injection rate monitoring system in accordance with your monitoring plan.


(i) For each carrier gas flow rate monitor, in addition to the requirements in paragraphs (b) through (e) of this section, you must meet the requirements of (i)(1) through (4) of this section.


(1) The minimum accuracy of the gas flow rate monitor must be ±5 percent over the normal range of flow measured or 280 liters per minute (10 cubic feet per minute), whichever is greater.


(2) Locate the device in a position(s) that provides a representative measurement of the carrier gas flow rate.


(3) Install and calibrate the device in accordance with manufacturer’s procedures and specifications.


(4) At least annually, conduct a performance evaluation of the carrier gas flow rate monitoring system in accordance with your monitoring plan.


[68 FR 61888, Oct. 30, 2003, as amended at 85 FR 45494, July 28, 2020; 89 FR 16432, Mar. 6, 2024]


§ 63.9633 How do I monitor and collect data to demonstrate continuous compliance?

(a) Except for monitoring malfunctions, out of control periods, associated repairs, and required quality assurance or control activities (including as applicable, calibration checks and required zero and span adjustments), you must monitor continuously (or collect data at all required intervals) at all times an affected source is operating.


(b) You may not use data recorded during monitoring malfunctions, out of control periods, associated repairs, and required quality assurance or control activities in data averages and calculations used to report emission or operating levels, or to fulfill a minimum data availability requirement. You must use all the data collected during all other periods in assessing compliance.


(c) A monitoring malfunction is any sudden, infrequent, not reasonably preventable failure of the monitoring system to provide valid data. Monitoring failures that are caused in part by poor maintenance or careless operation are not considered malfunctions.


[68 FR 61888, Oct. 30, 2003, as amended at 85 FR 45496, July 28, 2020]


§ 63.9634 How do I demonstrate continuous compliance with the emission limitations that apply to me?

(a) For each affected source subject to an emission limit in table 1 to this subpart, you must demonstrate continuous compliance by meeting the requirements in paragraphs (b) through (h) of this section.


(b) For ore crushing and handling affected sources and finished pellet handling affected sources, you must demonstrate continuous compliance by meeting the requirements in paragraphs (b)(1) through (3) of this section.


(1) The flow-weighted mean concentration of particulate matter for all ore crushing and handling emission units and for all finished pellet handling emission units must be maintained at or below the emission limits in Table 1 to this subpart.


(2) You must conduct subsequent performance tests for emission units in the ore crushing and handling and finished pellet handling affected sources following the schedule in your title V permit. If a title V permit has not been issued, you must conduct subsequent performance tests according to a testing plan approved by the Administrator or delegated authority.


(3) For ore crushing and handling and finished pellet handling emission units not selected for initial performance testing and defined within a group of similar emission units in accordance with § 63.9620(e), the site-specific operating limits established for the emission unit selected as representative of a group of similar emission units will be used as the operating limit for each emission unit within the group. The operating limit established for the representative unit must be met by each emission unit within the group.


(c) For ore dryers and indurating furnaces, you must demonstrate continuous compliance by meeting the requirements in paragraphs (c)(1) and (2) of this section.


(1) The flow-weighted mean concentration of particulate matter for all stacks from the ore dryer or indurating furnace must be maintained at or below the emission limits in Table 1 to this subpart.


(2) For ore dryers, you must conduct subsequent performance tests following the schedule in your title V permit. For indurating furnaces, you must conduct subsequent performance tests following the schedule in your title V permit, but no less frequent than twice per 5-year permit term. If a title V permit has not been issued, you must conduct subsequent performance tests according to a testing plan approved by the Administrator or delegated authority.


(d) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, for each baghouse applied to meet any particulate emission limit in Table 1 to this subpart, you must demonstrate continuous compliance by completing the requirements in paragraphs (d)(1) and (2) of this section. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, for each baghouse applied to meet any particulate emission limit in Table 1 to this subpart, you must demonstrate continuous compliance by completing the requirements in paragraphs (d)(1) through (3) of this section.


(1) Maintaining records of the time you initiated corrective action in the event of a bag leak detection system alarm, the corrective action(s) taken, and the date on which corrective action was completed.


(2) Inspecting and maintaining each baghouse according to the requirements in § 63.9631(a) and recording all information needed to document conformance with the requirements in § 63.9631(a). If you increase or decrease the sensitivity of the bag leak detection system beyond the limits specified in your site-specific monitoring plan, you must include a copy of the required written certification by a responsible official in the next semiannual compliance report.


(3) Each bag leak detection system must be operated and maintained such that the alarm does not sound more than 5 percent of the operating time during a 6-month period. Calculate the alarm time as specified in paragraphs (d)(3)(i) through (iii) of this section.


(i) If inspection of the fabric filter demonstrates that no corrective action is required, no alarm time is counted.


(ii) If corrective action is required, each alarm time (i.e., time that the alarm sounds) is counted as a minimum of 1 hour.


(iii) If it takes longer than 1 hour to initiate corrective action, each alarm time is counted as the actual amount of time taken to initiate corrective action.


(e) Except as provided in paragraph (f) of this section, for each wet scrubber subject to the operating limits for pressure drop and scrubber water flow rate in § 63.9590(b)(1), you must demonstrate continuous compliance by completing the requirements of paragraphs (e)(1) through (4) of this section.


(1) Maintaining the daily average pressure drop and daily average scrubber water flow rate at or above the minimum levels established during the initial or subsequent performance test.


(2) Operating and maintaining each wet scrubber CPMS according to § 63.9632(b) and recording all information needed to document conformance with these requirements.


(3) Collecting and reducing monitoring data for pressure drop and scrubber water flow rate according to § 63.9632(c) and recording all information needed to document conformance with these requirements.


(4) If the daily average pressure drop or daily average scrubber water flow rate is below the operating limits established for a corresponding emission unit or group of similar emission units, you must then follow the corrective action procedures in paragraph (l) of this section.


(f) On or before January 28, 2022, for affected sources that commenced construction or reconstruction on or before September 25, 2019, for each dynamic wet scrubber subject to the operating limits for scrubber water flow rate and either the fan amperage or pressure drop in § 63.9590(b)(2), you must demonstrate continuous compliance by completing the requirements of paragraphs (f)(1) through (4) of this section. After January 28, 2022, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, for each dynamic wet scrubber subject to the operating limits for scrubber water flow rate and the fan amperage in § 63.9590(b)(2), you must demonstrate continuous compliance by completing the requirements of paragraphs (f)(1) through (4) of this section.


(1) On or before January 28, 2022, for affected sources that commenced construction or reconstruction on or before September 25, 2019, maintaining the daily average scrubber water flow rate and either the daily average fan amperage or the daily average pressure drop at or above the minimum levels established during the initial or subsequent performance test. After January 28, 2022, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, maintaining the daily average scrubber water flow rate and the daily average fan amperage at or above the minimum levels established during the initial or subsequent performance test.


(2) Operating and maintaining each dynamic wet scrubber CPMS according to § 63.9632(b) and recording all information needed to document conformance with these requirements.


(3) On or before January 28, 2022, for affected sources that commenced construction or reconstruction on or before September 25, 2019, collecting and reducing monitoring data for scrubber water flow rate and either fan amperage or pressure drop according to § 63.9632(c) and recording all information needed to document conformance with the requirements in § 63.9632(c). After January 28, 2022, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, collecting and reducing monitoring data for scrubber water flow rate and fan amperage according to § 63.9632(c) and recording all information needed to document conformance with the requirements in § 63.9632(c).


(4) On or before January 28, 2022, for affected sources that commenced construction or reconstruction on or before September 25, 2019, if the daily average scrubber water flow rate, daily average fan amperage, or daily average pressure drop is below the operating limits established for a corresponding emission unit or group of similar emission units, you must then follow the corrective action procedures in paragraph (l) of this section. After January 28, 2022, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, if the daily average scrubber water flow rate or daily average fan amperage, is below the operating limits established for a corresponding emission unit or group of similar emission units, you must then follow the corrective action procedures in paragraph (l) of this section.


(g) For each dry ESP subject to operating limits in § 63.9590(b)(3), you must demonstrate continuous compliance by completing the requirements of paragraph (g)(1) or (2) of this section.


(1) If the operating limit for your dry ESP is a 6-minute average opacity of emissions value, then you must follow the requirements in paragraphs (g)(1)(i) through (iii) of this section.


(i) Maintaining the 6-minute average opacity of emissions at or below the maximum level established during the initial or subsequent performance test.


(ii) Operating and maintaining each COMS and reducing the COMS data according to § 63.9632(f).


(iii) If the 6-minute average opacity of emissions is above the operating limits established for a corresponding emission unit, you must then follow the corrective action procedures in paragraph (l) of this section.


(2) If the operating limit for your dry ESP is the daily average secondary voltage and daily average secondary current for each field, then you must follow the requirements in paragraphs (g)(2)(i) through (iv) of this section.


(i) Maintaining the daily average secondary voltage or daily average secondary current for each field at or above the minimum levels established during the initial or subsequent performance test.


(ii) Operating and maintaining each dry ESP CPMS according to § 63.9632(b) and recording all information needed to document conformance with these requirements.


(iii) Collecting and reducing monitoring data for secondary voltage or secondary current for each field according to § 63.9632(c) and recording all information needed to document conformance with these requirements.


(iv) If the daily average secondary voltage or daily average secondary current for each field is below the operating limits established for a corresponding emission unit, you must then follow the corrective action procedures in paragraph (l) of this section.


(h) For each wet ESP subject to the operating limits for secondary voltage, stack outlet temperature, and water flow rate in § 63.9590(b)(4), you must demonstrate continuous compliance by completing the requirements of paragraphs (h)(1) through (4) of this section.


(1) Maintaining the daily average secondary voltage and daily average scrubber water flow rate for each field at or above the minimum levels established during the initial or subsequent performance test. Maintaining the daily average stack outlet temperature at or below the maximum levels established during the initial or subsequent performance test.


(2) Operating and maintaining each wet ESP CPMS according to § 63.9632(b) and recording all information needed to document conformance with these requirements.


(3) Collecting and reducing monitoring data for secondary voltage, stack outlet temperature, and water flow rate according to § 63.9632(c) and recording all information needed to document conformance with these requirements.


(4) If the daily average secondary voltage, stack outlet temperature, or water flow rate does not meet the operating limits established for a corresponding emission unit, you must then follow the corrective action procedures in paragraph (l) of this section.


(i) For each affected indurating furnace subject to a hydrogen chloride and hydrogen fluoride emission limit in table 3 to this subpart, you must demonstrate continuous compliance by meeting the requirements in paragraphs (i)(1) and (2) of this section.


(1) For each wet scrubber and wet ESP subject to the operating limits for scrubber water flow rate and pH in § 63.9590(b)(5), you must demonstrate continuous compliance by completing the requirements of paragraphs (i)(1)(i) through (iv) of this section.


(i) Maintaining the daily average scrubber water flow rate and daily average pH of the scrubber water effluent at or above the minimum level established during the most recent performance test. If a higher average flow rate is measured during the last PM performance test, the operating limit for daily average scrubber water flow rate is the highest average scrubber water flow rate measured during the last PM performance test.


(ii) Operating and maintaining each of the CPMS used to measure scrubber water flow rate and pH according to § 63.9632(g) and recording all information needed to document conformance with these requirements.


(iii) Collecting and reducing monitoring data for scrubber water flow rate and pH according to § 63.9632(c) and recording all information needed to document conformance with these requirements.


(iv) If the daily average scrubber water flow rate or daily average pH is below the operating limits established for control device, you must follow the corrective action procedures in paragraph (l) of this section.


(2) For each DSI subject to the operating limits for sorbent injection rate and carrier gas flow rate in § 63.9590(b)(7), you must demonstrate continuous compliance by completing the requirements of paragraphs (i)(2)(i) through (iv) of this section.


(i) Maintain the daily average sorbent injection rate and carrier gas flow rate at or above the minimum level established during the most recent performance test.


(ii) Operate and maintain each CPMS used to measure the sorbent injection rate according to § 63.9632(h) and the carrier gas flow rate according to § 63.9632(i) and recording all information needed to document compliance with these requirements.


(iii) Collect and reduce monitoring data for the sorbent injection rate and carrier gas flow rate according to § 63.9632(c) and recording all information needed to document compliance with these requirements.


(iv) If the daily average the sorbent injection rate or carrier gas flow rate is below the operating limit established for the control device, you must follow the corrective action procedures in paragraph (l) of this section.


(j) For each affected indurating furnace using ACI to comply with the mercury emission limit in table 2 to this subpart, you must demonstrate continuous compliance by meeting the requirements of paragraphs (j)(1) or (2) of this section.


(1) If you use CEMS to demonstrate compliance, you must comply with the requirements in paragraphs (j)(1)(i) and (ii) of this section.


(i) You must operate a mercury CEMS in accordance with performance specification 12A at 40 CFR part 60, appendix B; these monitoring systems must be quality assured according to procedure 5 of 40 CFR 60, appendix F. You must demonstrate compliance with the mercury emissions limit using a 30-day rolling average of these 1-hour mercury concentrations or mass emissions rates, including CEMS data during startup and shutdown as defined in this subpart, calculated using equation 19-19 in section 12.4.1 of EPA Reference Method 19 at 40 CFR part 60, appendix A-7 of this part.


(ii) Owners or operators using a mercury CEMS to determine mass emission rate must install, operate, calibrate and maintain an instrument for continuously measuring and recording the mercury mass emissions rate to the atmosphere according to the requirements of performance specification 6 at 40 CFR part 60, appendix B and conducting an annual relative accuracy test of the continuous emission rate monitoring system according to section 8.2 of performance specification 6.


(2) If you do not use CEMS to demonstrate compliance, you must demonstrate continuous compliance by meeting the requirements of paragraphs (j)(2)(i) through (iv) of this section.


(i) Maintain the daily average activated carbon injection rate and carrier gas flow rate at or above the minimum level established during the most recent performance test.


(ii) Operate and maintain each CPMS used to measure the activated carbon injection rate according to § 63.9632(h) and the carrier gas flow rate according to § 63.9632(i), and record all information needed to document compliance with these requirements.


(iii) Collect and reduce monitoring data for the activated carbon injection rate and carrier gas flow rate according to § 63.9632(c) and record all information needed to document conformance with these requirements.


(iv) If the daily average of the activated carbon injection rate or carrier gas flow rate is below the operating limit established for the control device, you must follow the corrective action procedures in paragraph (l) of this section.


(k) If you use an air pollution control device other than a wet scrubber, dynamic wet scrubber, dry ESP, wet ESP, DSI, ACI, or baghouse, you must submit a site-specific monitoring plan in accordance with § 63.9631(f). The site-specific monitoring plan must include the site-specific procedures for demonstrating initial and continuous compliance with the corresponding operating limits.


(l) If the daily average operating parameter value for an emission unit or group of similar emission units does not meet the corresponding established operating limit, you must then follow the procedures in paragraphs (l)(1) through (4) of this section.


(1) You must initiate and complete initial corrective action within 10 calendar days and demonstrate that the initial corrective action was successful. During any period of corrective action, you must continue to monitor, and record all required operating parameters for equipment that remains in operation. After the initial corrective action, if the daily average operating parameter value for the emission unit or group of similar emission units meets the operating limit established for the corresponding unit or group, then the corrective action was successful and the emission unit or group of similar emission units is in compliance with the established operating limits.


(2) If the initial corrective action required in paragraph (l)(1) of this section was not successful, then you must complete additional corrective action within 10 calendar days and demonstrate that the subsequent corrective action was successful. During any period of corrective action, you must continue to monitor, and record all required operating parameters for equipment that remains in operation. If the daily average operating parameter value for the emission unit or group of similar emission units meets the operating limit established for the corresponding unit or group, then the corrective action was successful, and the emission unit or group of similar emission units is in compliance with the established operating limits.


(3) If the second attempt at corrective action required in paragraph (l)(2) of this section was not successful, then you must repeat the procedures of paragraph (l)(2) of this section until the corrective action is successful. If the third attempt at corrective action is unsuccessful, you must conduct another performance test in accordance with the procedures in § 63.9622(f) and report to the Administrator as a deviation the third unsuccessful attempt at corrective action.


(4) After the third unsuccessful attempt at corrective action, you must submit to the Administrator the written report required in paragraph (l)(3) of this section within 5 calendar days after the third unsuccessful attempt at corrective action. This report must notify the Administrator that a deviation has occurred and document the types of corrective measures taken to address the problem that resulted in the deviation of established operating parameters and the resulting operating limits.


(m) If you elect to comply with the mercury limit in table 2 to this subpart using emissions averaging in accordance with an implementation plan approved under the provisions in § 63.9623(d), you must comply with the requirements in paragraphs (m)(1) through (5) of this section.


(1) For furnaces included in the emissions averaging group that do not use mercury CEMS, you must comply with the requirements in paragraph (m)(1)(i) or (ii) as applicable.


(i) For furnaces equipped with ACI systems, you must comply with the requirements in paragraph (j) of this section.


(ii) For furnaces equipped with a mercury control device or method other than ACI, you must comply with your site-specific monitoring plan in accordance with the requirements in paragraph (k) of this section.


(2) For furnaces included in the emissions averaging group that use mercury CEMS, you must comply with the requirements in paragraph (i)(1) of this section.


(3) Calculate the monthly production-weighted average emission rate using either the mercury CEMS data or mercury emission rate determined during the last performance test and the actual taconite pellet production data for each furnace included in the emissions averaging option, as shown in Equation 6 of this section.




Where:

Eg = Monthly production-weighted average mercury emission rate for month “g” for the group of indurating furnaces, lb/LT of pellets produced,

Ef = Average mercury emission rate for furnace “f”, as determined using either mercury CEMS data or the emission rate determined during the last compliance stack test and calculated using Equation 5 of § 63.9621(d)(7)(i), lb/LT of pellets produced,

Pf = Total monthly production of finished taconite pellets for furnace “f”, in LT, and

n = Number of furnaces in the averaging group.

(4) Until 12 monthly weighted average emission rates have been accumulated, the monthly weighted average emissions rate, calculated as shown in paragraph (m)(3) of this section, must not exceed the mercury emission limit in table 3 of this subpart in any calendar month.


(5) After 12 monthly weighted average emission rates have been accumulated, for each subsequent calendar month, you must use Equation 7 of this section to calculate the 12-month rolling average of the monthly weighted average emission rates for the current month and the previous 11 months. The 12-month rolling weighted average emissions rate for the furnaces included in the group must not exceed the mercury emission limit in table 3 of this subpart.




Where:

Eavg = 12-month rolling average emission rate, lb/LT.

Ei = Monthly weighted average for month “i” calculated as shown in Equation 6 of this section.

(n) You may elect to demonstrate continuous compliance with the mercury limit in table 2 to this subpart by adjusting the activated carbon injection rate based on the taconite pellet production rate. You must comply with the requirements in paragraphs (n)(1) through (7) of this section.


(1) Measure the activated carbon injection and mercury emissions rate at a minimum of three different production levels corresponding to the maximum, minimum and median finished taconite pellet production rates, using the methods specified in § 63.9620(k).


(2) Develop a correlation curve by plotting the production rate and corresponding carbon injection rate for the maximum, median and minimum production rates. Use only data where the mercury emission rate is below the applicable mercury emissions standard in table 2 to this subpart. Plot the production rates as the independent (or x) variable and the activated carbon injection rate as the dependent (or y) variable for each pellet production rate. Construct the graph by drawing straight line segments between each point plotted.


(3) You must develop and submit to the applicable regulatory authority for review and approval, an implementation plan no later than 180 days before the date you intend to demonstrate compliance by adjusting the activated carbon injection rate based on the taconite pellet production. You must include the information listed in paragraphs (n)(3)(i) through (iv) of this section in your implementation plan.


(i) Identification of the indurating furnace, including the typical maximum and minimum taconite pellet production rate, mercury control technology installed, and types of fuel(s) that will be burned.


(ii) The mercury emissions and activated carbon injection rates at maximum, median and minimum taconite pellet production rates, and the methods used to measure the mercury emissions, activated carbon injection rate and taconite pellet production.


(iii) The correlation curve developed in paragraph (n)(2) of this section.


(iv) The date on which you are requesting to commence adjusting the activated carbon rate based on the taconite production rate.


(4) Install, calibrate, maintain, and operate a CPMS to monitor and record the activated carbon injection rate and taconite pellet production rate.


(5) Maintain the carbon injection rate at or above the rate established by the correlation curve corresponding to the taconite pellet production rate. If the taconite pellet production rate drops below the minimum rate established in paragraph (n)(3) of this section, you must maintain the activated carbon injection rate at or above the rate established for the minimum taconite pellet production rate.


(6) Keep records of the activated carbon injection rate and taconite pellet production rate for each hour of operation in order to demonstrate that the activated carbon injection rate remains in compliance with paragraph (n)(5) of this section.


(7) Establish a new correlation curve at least twice per 5-year permit term.


[68 FR 61888, Oct. 30, 2003, as amended at 85 FR 45496, July 28, 2020; 89 FR 16432, Mar. 6, 2024]


§ 63.9635 How do I demonstrate continuous compliance with the work practice standards that apply to me?

(a) You must demonstrate continuous compliance with the work practice standard requirements in § 63.9591 by operating in accordance with your fugitive dust emissions control plan at all times.


(b) You must maintain a current copy of the fugitive dust emissions control plan required in § 63.9591 onsite and it must be available for inspection upon request. You must keep the plan for the life of the affected source or until the affected source is no longer subject to the requirements of this subpart.


§ 63.9636 How do I demonstrate continuous compliance with the operation and maintenance requirements that apply to me?

(a) For each control device used to comply with an emission standard in § 63.9590(a), you must demonstrate continuous compliance with the operation and maintenance requirements in § 63.9600(b) by completing the requirements of paragraphs (a)(1) through (4) of this section.


(1) Performing preventative maintenance for each control device in accordance with § 63.9600(b)(1) and recording all information needed to document conformance with these requirements;


(2) Initiating and completing corrective action for a bag leak detection system alarm in accordance with § 63.9600(b)(2) and recording all information needed to document conformance with these requirements;


(3) Initiating and completing corrective action for a CPMS when you exceed an established operating limit for an air pollution control device except for a baghouse in accordance with § 63.9600(b)(3) and recording all information needed to document conformance with these requirements; and


(4) Implementing and maintaining site-specific good combustion practices for each indurating furnace in accordance with § 63.9600(b)(4) and recording all information needed to document conformance with these requirements.


(b) You must maintain a current copy of the operation and maintenance plan required in § 63.9600(b) onsite, and it must be available for inspection upon request. You must keep the plan for the life of the affected source or until the affected source is no longer subject to the requirements of this subpart.


[68 FR 61888, Oct. 30, 2003, as amended at 89 FR 16435, Mar. 6, 2024]


§ 63.9637 What other requirements must I meet to demonstrate continuous compliance?

(a) Deviations. You must report each instance in which you did not meet each emission limitation in tables 1 through 3 to this subpart that applies to you. You also must report each instance in which you did not meet the work practice standards in § 63.9591 and each instance in which you did not meet each operation and maintenance requirement in § 63.9600 that applies to you. These instances are deviations from the emission limitations, work practice standards, and operation and maintenance requirements in this subpart. These deviations must be reported in accordance with the requirements in § 63.9641.


(b) Startups, shutdowns, and malfunctions. For existing sources and for new or reconstructed sources which commenced construction or reconstruction on or before September 25, 2019, on or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, consistent with §§ 63.6(e) and 63.7(e)(1), deviations that occur during a period of startup, shutdown, or malfunction are not violations if you demonstrate to the Administrator’s satisfaction that you were operating in accordance with § 63.6(e)(1). The Administrator will determine whether deviations that occur during a period of startup, shutdown, or malfunction are violations, according to the provisions in § 63.6(e). After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, the exemptions for periods of startup, shutdown, and malfunction in § 63.6(e) no longer apply.


[85 FR 45497, July 28, 2020, as amended at 89 FR 16435, Mar. 6, 2024]


Notifications, Reports, and Records

§ 63.9640 What notifications must I submit and when?

(a) You must submit all of the notifications in §§ 63.7(b) and (c), 63.8(f)(4), and 63.9(b) through (h) that apply to you by the specified dates.


(b) As specified in § 63.9(b)(2), if you start up your affected source before October 30, 2003, you must submit your initial notification no later than 120 calendar days after October 30, 2003, or no later than 120 days after the source becomes subject to this subpart, whichever is later.


(c) As specified in § 63.9(b)(3), if you start up your new affected source on or after October 30, 2003, you must submit your initial notification no later than 120 calendar days after you become subject to this subpart.


(d) If you are required to conduct a performance test, you must submit a notification of intent to conduct a performance test at least 60 calendar days before the performance test is scheduled to begin, as required in § 63.7(b)(1).


(e) If you are required to conduct a performance test or other initial compliance demonstration, you must submit a notification of compliance status according to § 63.9(h)(2)(ii). The initial notification of compliance status must be submitted by the dates specified in paragraphs (e)(1) and (2) of this section.


(1) For each initial compliance demonstration that does not include a performance test, you must submit the notification of compliance status before the close of business on the 30th calendar day following completion of the initial compliance demonstration.


(2) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, for each initial compliance demonstration that does include a performance test, you must submit the notification of compliance status, including the performance test results, before the close of business on the 60th calendar day following the completion of the performance test according to § 63.10(d)(2). After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, for each initial compliance demonstration that does include a performance test, you must submit the notification of compliance status, including the performance test results, before the close of business on the 60th calendar day following the completion of the performance test according to § 63.10(d)(2). If the performance test results have been submitted electronically in accordance with § 63.9641(f), the process unit(s) tested, the pollutant(s) tested, and the date that such performance test was conducted may be submitted in the notification of compliance status report in lieu of the performance test results. The performance test results must be submitted to the Compliance and Emissions Data Reporting Interface (CEDRI) by the date the notification of compliance status report is submitted.


(f) If you elect to use CEMS to demonstrate compliance with the mercury standards in table 2 to this subpart, you must submit a notification of intent to use CEMS at least one month prior to making the change. If you are currently using CEMS to demonstrate compliance with the mercury standards, you must submit a notification of intent to cease using CEMS to demonstrate compliance at least 180 days prior to making the change.


(g) If you elect to use the mercury emissions averaging compliance option, you must submit a notification of intent at least 180 days prior to making the change. If you are currently using the mercury emissions averaging compliance option, you must submit a notification of intent to cease using emissions averaging at least 30 days prior to making the change.


[68 FR 61888, Oct. 30, 2003, as amended at 85 FR 45497, July 28, 2020; 85 FR 73917, Nov. 19, 2020; 89 FR 16435, Mar. 6, 2024]


§ 63.9641 What reports must I submit and when?

(a) Compliance report due dates. Unless the Administrator has approved a different schedule, you must submit a semiannual compliance report to your permitting authority according to the requirements in paragraphs (a)(1) through (5) of this section.


(1) The first compliance report must cover the period beginning on the compliance date that is specified for your affected source in § 63.9583 and ending on June 30 or December 31, whichever date comes first after the compliance date that is specified for your source in § 63.9583.


(2) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, the first compliance report must be postmarked or delivered no later than July 31 or January 31, whichever date comes first after your first compliance report is due. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, the first compliance report must be electronically submitted, postmarked or delivered no later than July 31 or January 31, whichever date comes first after your first compliance report is due.


(3) Each subsequent compliance report must cover the semiannual reporting period from January 1 through June 30 or the semiannual reporting period from July 1 through December 31.


(4) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, each subsequent compliance report must be postmarked or delivered no later than July 31 or January 31, whichever date comes first after the end of the semiannual reporting period. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, each subsequent compliance report must be electronically submitted, postmarked or delivered no later than July 31 or January 31, whichever date comes first after the end of the semiannual reporting period.


(5) For each affected source that is subject to permitting regulations pursuant to 40 CFR part 70 or 40 CFR part 71, and if the permitting authority has established dates for submitting semiannual reports pursuant to 40 CFR 70.6(a)(3)(iii)(A) or 40 CFR 71.6(a)(3)(iii)(A), you may submit the first and subsequent compliance reports according to the dates the permitting authority has established instead of according to the dates in paragraphs (a)(1) through (4) of this section.


(b) Compliance report contents. Each compliance report must include the information in paragraphs (b)(1) through (8) of this section, as applicable.


(1) Company name and address.


(2) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, statement by a responsible official, with the official’s name, title, and signature, certifying the truth, accuracy, and completeness of the content of the report. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, statement by a responsible official, with the official’s name, title, and signature, certifying the truth, accuracy, and completeness of the content of the report. If your report is submitted via CEDRI, the certifier’s electronic signature during the submission process replaces the requirement in this paragraph (b)(2).


(3) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, date of report and beginning and ending dates of the reporting period. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, date of report and beginning and ending dates of the reporting period. You are no longer required to provide the date of report when the report is submitted via CEDRI.


(4) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, if you had a startup, shutdown, or malfunction during the reporting period and you took actions consistent with your startup, shutdown, and malfunction plan, the compliance report must include the information in § 63.10(d)(5)(i). A startup, shutdown, and malfunction plan and the information in § 63.10(d)(5)(i) is not required after January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and is not required after July 28, 2020, for affected sources that commenced construction or reconstruction after September 25, 2019.


(5) If there were no deviations from the continuous compliance requirements in §§ 63.9634 through 63.9636 that apply to you, then provide a statement that there were no deviations from the emission limitations, work practice standards, or operation and maintenance requirements during the reporting period.


(6) If there were no periods during which a continuous monitoring system (including a CPMS, COMS, or CEMS) was out-of-control as specified in § 63.8(c)(7), then provide a statement that there were no periods during which a continuous monitoring system was out-of-control during the reporting period.


(7) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, for each deviation from an emission limitation in Table 1 to this subpart that occurs at an affected source where you are not using a continuous monitoring system (including a CPMS or COMS) to comply with an emission limitation in this subpart, the compliance report must contain the information in paragraphs (b)(1) through (4) of this section and the information in paragraphs (b)(7)(i) and (ii) of this section. This includes periods of startup, shutdown, and malfunction. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, for each deviation from an emission limitation in Table 1 to this subpart that occurs at an affected source where you are not using a continuous monitoring system (including a CPMS or COMS) to comply with an emission limitation in this subpart, the compliance report must contain the information in paragraphs (b)(7)(i) and (ii) of this section.


(i) The total operating time in hours of each affected source during the reporting period.


(ii) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, information on the number, duration, and cause of deviation (including unknown cause) as applicable, and the corrective action taken. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, information on the affected sources or equipment, the emission limit deviated from, the start date, start time, duration in hours, and cause of each deviation (including unknown cause) as applicable, an estimate of the quantity in pounds of each regulated pollutant emitted over an emission limit and a description of the method used to estimate the emissions, and the corrective action taken.


(8) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, for each deviation from an emission limitation occurring at an affected source where you are using a continuous monitoring system (including a CPMS or COMS) to comply with the emission limitation in this subpart, you must include the information in paragraphs (b)(1) through (4) of this section and the information in paragraphs (b)(8)(i) through (xi) of this section. This includes periods of startup, shutdown, and malfunction. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, for each deviation from an emission limitation occurring at an affected source where you are using a continuous monitoring system (including a CPMS, COMS, or CEMS) to comply with the emission limitation in this subpart, you must include the information in paragraphs (b)(1) through (4) of this section and the information in paragraphs (b)(8)(i) through (xi) of this section.


(i) The date and time that each malfunction started and stopped.


(ii) The start date, start time, and duration in hours (or minutes for COMS) that each continuous monitoring system was inoperative, except for zero (low-level) and high-level checks.


(iii) The start date, start time, and duration that each continuous monitoring system was out-of-control, including the information in § 63.8(c)(8).


(iv) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, for each affected source or equipment, the date and time that each deviation started and stopped, the cause of the deviation, and whether each deviation occurred during a period of startup, shutdown, or malfunction or during another period. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, for each affected source or equipment, the date and time that each deviation started and stopped, the cause of the deviation, and whether each deviation occurred during a period of malfunction or during another period


(v) The total duration of all deviations for each Continuous Monitoring System (CMS) during the reporting period, the total operating time in hours of the affected source during the reporting period, and the total duration as a percent of the total source operating time during that reporting period.


(vi) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, a breakdown of the total duration of the deviations during the reporting period including those that are due to startup, shutdown, control equipment problems, process problems, other known causes, and other unknown causes. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, a breakdown of the total duration of the deviations during the reporting period including those that are due to control equipment problems, process problems, other known causes, and other unknown causes.


(vii) The total duration of continuous monitoring system downtime for each continuous monitoring system during the reporting period, the total operating time in hours of the affected source during the reporting period, and the total duration of continuous monitoring system downtime as a percent of the total source operating time during the reporting period.


(viii) A brief description of the process units.


(ix) The monitoring equipment manufacturer and model number and the pollutant or parameter monitored.


(x) The date of the latest continuous monitoring system certification or audit.


(xi) A description of any changes in continuous monitoring systems, processes, or controls since the last reporting period.


(c) Submitting compliance reports electronically. Beginning on January 25, 2021, submit all subsequent compliance reports to the EPA via CEDRI, which can be accessed through the EPA’s Central Data Exchange (CDX) (https://cdx.epa.gov/). The EPA will make all the information submitted through CEDRI available to the public without further notice to you. Do not use CEDRI to submit information you claim as confidential business information (CBI). Anything submitted using CEDRI cannot later be claimed to be CBI. You must use the appropriate electronic report template on the CEDRI website (https://www.epa.gov/electronic-reporting-air-emissions/compliance-and-emissions-data-reporting-interface-cedri) for this subpart. The report must be submitted by the deadline specified in this subpart, regardless of the method in which the report is submitted. Although we do not expect persons to assert a claim of CBI, if persons wish to assert a CBI claim, submit a complete report, including information claimed to be CBI, to the EPA. The report must be generated using the appropriate form on the CEDRI website. Clearly mark the part or all of the information that you claim to be CBI. Information not marked as CBI may be authorized for public release without prior notice. Information marked as CBI will not be disclosed except in accordance with procedures set forth in 40 CFR part 2. Submit the file following the procedures in paragraph (c)(1) or (2) of this section. The same file with the CBI omitted must be submitted to the EPA via the EPA’s CDX as described earlier in this paragraph (c). All CBI claims must be asserted at the time of submission. Furthermore, under CAA section 114(c) emissions data is not entitled to confidential treatment, and EPA is required to make emissions data available to the public. Thus, emissions data will not be protected as CBI and will be made publicly available. On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, if you had a startup, shutdown, or malfunction during the reporting period that is not consistent with your startup, shutdown, and malfunction plan you must submit an immediate startup, shutdown and malfunction report according to the requirements in § 63.10(d)(5)(ii). After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, an immediate startup, shutdown, and malfunction report is not required.


(1) The preferred method to receive CBI is for it to be transmitted electronically using email attachments, File Transfer Protocol, or other online file sharing services. Electronic submissions must be transmitted directly to the OAQPS CBI Office at the email address [email protected], and as described above, should include clear CBI markings and be flagged to the attention of the Taconite Iron Ore Processing Sector Lead. If assistance is needed with submitting large electronic files that exceed the file size limit for email attachments, and if you do not have your own file sharing service, please email [email protected] to request a file transfer link.


(2) If you cannot transmit the file electronically, you may send CBI information through the postal service to the following address: U.S. EPA, Attn: OAQPS Document Control Officer and Taconite Iron Ore Processing Sector Lead, Mail Drop: C404-02, 109 T.W. Alexander Drive, P.O. Box 12055, RTP, NC 27711. The mailed CBI material should be double wrapped and clearly marked. Any CBI markings should not show through the outer envelope.


(d) Part 70 monitoring report. If you have obtained a title V operating permit for an affected source pursuant to 40 CFR part 70 or 40 CFR part 71, you must report all deviations as defined in this subpart in the semiannual monitoring report required by 40 CFR 70.6(a)(3)(iii)(A) or 40 CFR 71.6(a)(3)(iii)(A). If you submit a compliance report for an affected source along with, or as part of, the semiannual monitoring report required by 40 CFR 70.6(a)(3)(iii)(A) or 40 CFR 71.6(a)(3)(iii)(A), and the compliance report includes all the required information concerning deviations from any emission limitation or operation and maintenance requirement in this subpart, submission of the compliance report satisfies any obligation to report the same deviations in the semiannual monitoring report. However, submission of a compliance report does not otherwise affect any obligation you may have to report deviations from permit requirements for an affected source to your permitting authority.


(e) Immediate corrective action report. If you had three unsuccessful attempts of applying corrective action as described in § 63.9634(l) on an emission unit or group of emission units, then you must submit an immediate corrective action report. Within 5 calendar days after the third unsuccessful attempt at corrective action, you must submit to the Administrator a written report in accordance with § 63.9634(l)(3) and (4). This report must notify the Administrator that a deviation has occurred and document the types of corrective measures taken to address the problem that resulted in the deviation of established operating parameters and the resulting operating limits.


(f) Performance tests. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, within 60 days after the date of completing each performance test required by this subpart, you must submit the results of the performance test following the procedures specified in paragraphs (f)(1) through (3) of this section.


(1) Data collected using test methods supported by the EPA’s Electronic Reporting Tool (ERT) as listed on the EPA’s ERT website (https://www.epa.gov/electronic-reporting-air-emissions/electronic-reporting-tool-ert) at the time of the test. Submit the results of the performance test to the EPA via CEDRI, which can be accessed through the EPA’s CDX (https://cdx.epa.gov/). The data must be submitted in a file format generated through the use of the EPA’s ERT. Alternatively, you may submit an electronic file consistent with the extensible markup language (XML) schema listed on the EPA’s ERT website.


(2) Data collected using test methods that are not supported by the EPA’s ERT as listed on the EPA’s ERT website at the time of the test. The results of the performance test must be included as an attachment in the ERT or an alternate electronic file consistent with the XML schema listed on the EPA’s ERT website. Submit the ERT generated package or alternative file to the EPA via CEDRI.


(3) Confidential business information (CBI).


(i) The EPA will make all the information submitted through CEDRI available to the public without further notice to you. Do not use CEDRI to submit information you claim as CBI. Although we do not expect persons to assert a claim of CBI, if you wish to assert a CBI claim for some of the information submitted under paragraph (f)(1) or (2) of this section, you must submit a complete file, including information claimed to be CBI, to the EPA.


(ii) The file must be generated using the EPA’s ERT or an alternate electronic file consistent with the XML schema listed on the EPA’s ERT website.


(iii) Clearly mark the part or all of the information that you claim to be CBI. Information not marked as CBI may be authorized for public release without prior notice. Information marked as CBI will not be disclosed except in accordance with procedures set forth in 40 CFR part 2.


(iv) The preferred method to receive CBI is for it to be transmitted electronically using email attachments, File Transfer Protocol, or other online file sharing services. Electronic submissions must be transmitted directly to the OAQPS CBI Office at the email address [email protected], and as described above, should include clear CBI markings and be flagged to the attention of the Group Leader, Measurement Policy Group. If assistance is needed with submitting large electronic files that exceed the file size limit for email attachments, and if you do not have your own file sharing service, please email [email protected] to request a file transfer link.


(v) If you cannot transmit the file electronically, you may send CBI information through the postal service to the following address: U.S. EPA, Attn: OAQPS Document Control Officer and Measurement Policy Group Lead, Mail Drop: C404-02, 109 T.W. Alexander Drive, P.O. Box 12055, RTP, NC 27711. The mailed CBI material should be double wrapped and clearly marked. Any CBI markings should not show through the outer envelope.


(vi) All CBI claims must be asserted at the time of submission. Anything submitted using CEDRI cannot later be claimed CBI. Furthermore, under CAA section 114(c), emissions data is not entitled to confidential treatment, and the EPA is required to make emissions data available to the public. Thus, emissions data will not be protected as CBI and will be made publicly available.


(vii) You must submit the same file submitted to the CBI office with the CBI omitted to the EPA via the EPA’s CDX as described in § 63.9(k).


(g) Claims of EPA system outage. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, if you are required to electronically submit a report through CEDRI in the EPA’s CDX, you may assert a claim of EPA system outage for failure to timely comply with the reporting requirement. To assert a claim of EPA system outage, you must meet the requirements outlined in paragraphs (g)(1) through (7) of this section.


(1) You must have been or will be precluded from accessing CEDRI and submitting a required report within the time prescribed due to an outage of either the EPA’s CEDRI or CDX systems.


(2) The outage must have occurred within the period of time beginning five business days prior to the date that the submission is due.


(3) The outage may be planned or unplanned.


(4) You must submit notification to the Administrator in writing as soon as possible following the date you first knew, or through due diligence should have known, that the event may cause or has caused a delay in reporting.


(5) You must provide to the Administrator a written description identifying:


(i) The date(s) and time(s) when CDX or CEDRI was accessed and the system was unavailable;


(ii) A rationale for attributing the delay in reporting beyond the regulatory deadline to EPA system outage;


(iii) Measures taken or to be taken to minimize the delay in reporting; and


(iv) The date by which you propose to report, or if you have already met the reporting requirement at the time of the notification, the date you reported.


(6) The decision to accept the claim of EPA system outage and allow an extension to the reporting deadline is solely within the discretion of the Administrator.


(7) In any circumstance, the report must be submitted electronically as soon as possible after the outage is resolved.


(h) Claims of force majeure. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, if you are required to electronically submit a report through CEDRI in the EPA’s CDX, you may assert a claim of force majeure for failure to timely comply with the reporting requirement. To assert a claim of force majeure, you must meet the requirements outlined in paragraphs (h)(1) through (5) of this section.


(1) You may submit a claim if a force majeure event is about to occur, occurs, or has occurred or there are lingering effects from such an event within the period of time beginning five business days prior to the date the submission is due. For the purposes of this section, a force majeure event is defined as an event that will be or has been caused by circumstances beyond the control of the affected facility, its contractors, or any entity controlled by the affected facility that prevents you from complying with the requirement to submit a report electronically within the time period prescribed. Examples of such events are acts of nature (e.g., hurricanes, earthquakes, or floods), acts of war or terrorism, or equipment failure or safety hazard beyond the control of the affected facility (e.g., large scale power outage).


(2) You must submit notification to the Administrator in writing as soon as possible following the date you first knew, or through due diligence should have known, that the event may cause or has caused a delay in reporting.


(3) You must provide to the Administrator:


(i) A written description of the force majeure event;


(ii) A rationale for attributing the delay in reporting beyond the regulatory deadline to the force majeure event;


(iii) Measures taken or to be taken to minimize the delay in reporting; and


(iv) The date by which you propose to report, or if you have already met the reporting requirement at the time of the notification, the date you reported.


(4) The decision to accept the claim of force majeure and allow an extension to the reporting deadline is solely within the discretion of the Administrator.


(5) In any circumstance, the reporting must occur as soon as possible after the force majeure event occurs.


(i) Use of CEMS for mercury. If you use CEMS to demonstrate compliance with the mercury emissions limits in table 2 to this subpart, you must submit the results of the performance evaluation following the procedure specified in either paragraph (i)(1) or (2) of this section within 60 days after the date of completing each CEMS performance evaluation (as defined in § 63.2).


(1) For performance evaluations of continuous monitoring systems measuring relative accuracy test audit (RATA) pollutants that are supported by the EPA’s ERT as listed on the EPA’s ERT website at the time of the evaluation, you must submit the results of the performance evaluation to the EPA via the CEDRI. Performance evaluation data must be submitted in a file format generated through the use of the EPA’s ERT or an alternate file format consistent with the XML schema listed on the EPA’s ERT website. If you claim that some of the performance evaluation information being transmitted is CBI, you must submit a complete file generated through the use of the EPA’s ERT or an alternate electronic file consistent with the XML schema listed on the EPA’s ERT website, including information claimed to be CBI, on a compact disc, flash drive, or other commonly used electronic storage media to the EPA. The electronic media must be clearly marked as CBI and mailed to U.S. EPA/OAQPS/CORE CBI Office, Attention: Group Leader, Measurement Policy Group, MD C404-02, 4930 Old Page Rd., Durham, NC 27703. The same ERT or alternate file with the CBI omitted must be submitted to the EPA via the EPA’s CDX as described earlier in this section.


(2) For any performance evaluations of continuous monitoring systems measuring RATA pollutants that are not supported by the EPA’s ERT as listed on the ERT website at the time of the evaluation, you must submit the results of the performance evaluation to the Administrator at the appropriate address listed in § 63.13.


[68 FR 61888, Oct. 30, 2003, as amended at 85 FR 45498, July 28, 2020; 89 FR 16435, Mar. 6, 2024]


§ 63.9642 What records must I keep?

(a) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, you must keep the records listed in paragraphs (a)(1) through (3) of this section. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, you must keep the records listed in paragraphs (a)(1) through (6) of this section.


(1) A copy of each notification and report that you submitted to comply with this subpart, including all documentation supporting any initial notification or notification of compliance status that you submitted, according to the requirements in § 63.10(b)(2)(xiv).


(2) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, the records in § 63.6(e)(3)(iii) through (v) related to startup, shutdown, and malfunction. After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, a startup, shutdown, and malfunction plan is not required.


(3) Records of performance tests and performance evaluations as required in § 63.10(b)(2)(viii).


(4) In the event that an affected unit fails to meet an applicable standard, record the number of failures. For each failure record the date, time, the cause and duration of each failure.


(5) For each failure to meet an applicable standard, record and retain a list of the affected sources or equipment, an estimate of the quantity of each regulated pollutant emitted over any emission limit and a description of the method used to estimate the emissions.


(6) Record actions taken in accordance with the general duty requirements to minimize emissions in § 63.9600(a) and any corrective actions taken to return the affected unit to its normal or usual manner of operation.


(b) For each COMS and CEMS, you must keep the records specified in paragraphs (b)(1) through (5) of this section.


(1) Records described in § 63.10(b)(2)(vi) through (xi).


(2) Monitoring data for COMS during a performance evaluation as required in § 63.6(h)(7)(i) and (ii).


(3) On or before January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, previous (that is, superseded) versions of the performance evaluation plan as required in § 63.8(d)(3). After January 25, 2021, for affected sources that commenced construction or reconstruction on or before September 25, 2019, and after July 28, 2020, or upon start-up, which ever date is later, for affected sources that commenced construction or reconstruction after September 25, 2019, previous (that is, superseded) versions of the performance evaluation plan as required in § 63.9632(b)(5), with the program of corrective action included in the plan required under § 63.8(d)(2).


(4) Records of the date and time that each deviation started and stopped, and whether the deviation occurred during a period of startup, shutdown, or malfunction or during another period.


(5) If you use mercury CEMS to demonstrate compliance with the mercury emission standard in table 2 of the subpart in accordance with § 63.9623(e), records of requests for alternatives to the relative accuracy test for CEMS as required in § 63.8(f)(6)(i).


(c) You must keep the records required in §§ 63.9634 through 63.9636 to show continuous compliance with each emission limitation, work practice standard, and operation and maintenance requirement that applies to you.


(d) If you elect the mercury emissions averaging compliance alternative pursuant to § 63.9623(d), you must keep a copy of the emission averaging implementation plan required in § 63.9623(d)(2), records of the taconite pellet production rate for each furnace included in the averaging, and all calculations required under § 63.9634(m).


(e) If you elect to adjust the activated carbon injection rate based on the taconite pellet production rate in accordance with the provisions in § 63.9634(n), you must keep a copy of the activated carbon injection implementation plan and records of the taconite pellet production rate and activated carbon injection rate.


(f) If you use CEMS to demonstrate compliance with the mercury emissions limits in table 2 to this subpart, you must keep records of the notifications required in § 63.9642(f).


[68 FR 61888, Oct. 30, 2003, as amended at 85 FR 45500, July 28, 2020; 89 FR 16437, Mar. 6, 2024]


§ 63.9643 In what form and how long must I keep my records?

(a) Your records must be in a form suitable and readily available for expeditious review, according to § 63.10(b)(1).


(b) As specified in § 63.10(b)(1), you must keep each record for 5 years following the date of each occurrence, measurement, maintenance, corrective action, report, or record.


(c) You must keep each record on site for at least 2 years after the date of each occurrence, measurement, maintenance, corrective action, report, or record according to § 63.10(b)(1). You can keep the records offsite for the remaining 3 years.


Other Requirements and Information

§ 63.9650 What parts of the General Provisions apply to me?

Table 4 to this subpart shows which parts of the General Provisions in §§ 63.1 through 63.16 apply to you.


[89 FR 16437, Mar. 6, 2024]


§ 63.9651 Who implements and enforces this subpart?

(a) This subpart can be implemented and enforced by us, the EPA, or a delegated authority such as your State, local, or tribal agency. If the EPA Administrator has delegated authority to your State, local, or tribal agency, then that agency has the authority to implement and enforce this subpart. You should contact your EPA Regional Office to find out if this subpart is delegated to your State, local, or tribal agency.


(b) In delegating implementation and enforcement authority of this subpart to a State, local, or tribal agency under subpart E of this part, the authorities contained in paragraph (c) of this section are retained by the Administrator of the EPA and are not transferred to the State, local, or tribal agency.


(c) The authorities that will not be delegated to state, local, or tribal agencies are specified in paragraphs (c)(1) through (5) of this section.


(1) Approval of non-opacity emission limitations and work practice standards under § 63.6(h)(9) and as defined in § 63.90.


(2) Approval of major alternatives to test methods under § 63.7(e)(2)(ii) and (f) and as defined in § 63.90.


(3) Approval of major alternatives to monitoring under § 63.8(f) and as defined in § 63.90.


(4) Approval of major alternatives to recordkeeping and reporting under § 63.10(f) and as defined in § 63.90.


(5) Approval of an alternative to any electronic reporting to the EPA required by this subpart.


[68 FR 61888, Oct. 30, 2003, as amended at 85 FR 45501, July 28, 2020]


§ 63.9652 What definitions apply to this subpart?

Terms used in this subpart are defined in the Clean Air Act, in § 63.2, and in this section as follows.


Activated carbon injection (ACI) system means an add-on air pollution control system in which activated carbon or brominated activated carbon is injected into the flue gas steam upstream of a particulate matter control device to adsorb mercury in the exhaust stream. The absorbed mercury remains absorbed to the activated carbon and is collected in a primary or secondary particulate matter control device.


Affected source means each new or existing ore crushing and handling operation, ore dryer, indurating furnace, or finished pellet handling operation, at your taconite iron ore processing plant.


Bag leak detection system means a system that is capable of continuously monitoring relative particulate matter (dust) loadings in the exhaust of a baghouse to detect bag leaks and other upset conditions. A bag leak detection system includes, but is not limited to, an instrument that operates on triboelectric, light scattering, light transmittance, or other effect to continuously monitor relative particulate matter loadings.


Crusher means a machine used to crush taconite ore and includes feeders or conveyors located immediately below the crushing surfaces. Crushers include, but are not limited to, gyratory crushers and cone crushers.


Deviation means any instance in which an affected source subject to this subpart, or an owner or operator of such a source:


(1) Fails to meet any requirement or obligation established by this subpart, including but not limited to any emission limitation (including operating limits) or operation and maintenance requirement; or


(2) Fails to meet any term or condition that is adopted to implement an applicable requirement in this subpart and that is included in the operating permit for any affected source required to obtain such a permit.


Dry sorbent injection (DSI) system means an add-on air pollution control system that injects dry alkaline sorbent (dry injection) or sprays an alkaline sorbent (spray dryer) to react with and neutralize acid gas in the exhaust stream forming a dry powder material that is collected by a primary or secondary particulate matter control device.


Dynamic wet scrubber means an air emissions control device which utilizes a mechanically powered fan to cause contact between the process exhaust gas stream and the scrubbing liquid which are introduced concurrently into the fan inlet.


Electrostatic Precipitator (ESP) means a device that removes suspended particulate matter from flue exhaust by applying a high-voltage electrostatic charge to the particles, which are then attracted to and collected on a grounded plate. In a dry ESP, the particles are dislodged from the plate by rapping and are collected in a hopper positioned below the plate. In a wet ESP, particulates are removed from the plate by washing with water.


Emission limitation means any emission limit, opacity limit, or operating limit.


Finished pellet handling means the transfer of fired taconite pellets from the indurating furnace to the finished pellet stockpiles at the plant. Finished pellet handling includes, but is not limited to, furnace discharge or grate discharge, and finished pellet screening, transfer, and storage. The atmospheric pellet cooler vent stack and gravity conveyor gallery vents designed to remove heat and water vapor from the structure are not included as a part of the finished pellet handling affected source.


Fugitive dust emission source means a stationary source from which particles are discharged to the atmosphere due to wind or mechanical inducement such as vehicle traffic. Fugitive dust sources include, but are not limited to:


(1) Stockpiles (includes, but is not limited to, stockpiles of uncrushed ore, crushed ore, or finished pellets);


(2) Material transfer points;


(3) Plant roadways;


(4) Tailings basins;


(5) Pellet loading areas; and


(6) Yard areas.


Grate feed means the transfer of unfired taconite pellets from the pelletizer into the indurating furnace.


Grate kiln indurating furnace means a furnace system that consists of a traveling grate, a rotary kiln, and an annular cooler. The grate kiln indurating furnace begins at the point where the grate feed conveyor discharges the green balls onto the furnace traveling grate and ends where the hardened pellets exit the cooler. The atmospheric pellet cooler vent stack is not included as part of the grate kiln indurating furnace.


Indurating means the process whereby unfired taconite pellets, called green balls, are hardened at high temperature in an indurating furnace. Types of indurating furnaces include straight grate indurating furnaces and grate kiln indurating furnaces.


Ore crushing and handling means the process whereby dry taconite ore is crushed and screened. Ore crushing and handling includes, but is not limited to, all dry crushing operations (e.g., primary, secondary, and tertiary crushing), dry ore conveyance and transfer points, dry ore classification and screening, dry ore storage and stockpiling, dry milling, dry cobbing (i.e., dry magnetic separation), and the grate feed. Ore crushing and handling specifically excludes any operations where the dry crushed ore is saturated with water, such as wet milling and wet magnetic separation.


Ore dryer means a rotary dryer that repeatedly tumbles wet taconite ore concentrate through a heated air stream to reduce the amount of entrained moisture in the taconite ore concentrate.


Pellet cooler vent stacks means atmospheric vents in the cooler section of the grate kiln indurating furnace that exhaust cooling air that is not returned for recuperation. Pellet cooler vent stacks are not to be confused with the cooler discharge stack, which is in the pellet loadout or dumping area.


Pellet loading area means that portion of a taconite iron ore processing plant where taconite pellets are loaded into trucks or railcars.


Responsible official means responsible official as defined in § 63.2.


Rod-deck venturi scrubber means a wet scrubber emission control device in which the inlet air flows through a bed of parallel metal pipes spaced apart to produce a series of parallel venturi throats.


Screen means a device for separating material according to size by passing undersize material through one or more mesh surfaces (screens) in series and retaining oversize material on the mesh surfaces (screens).


Storage bin means a facility for storage (including surge bins and hoppers) of taconite ore or taconite pellets prior to further processing or loading.


Straight grate indurating furnace means a furnace system that consists of a traveling grate that carries the taconite pellets through different furnace temperature zones. In the straight grate indurating furnace a layer of fired pellets, called the hearth layer, is placed on the traveling grate prior to the addition of unfired pellets. The straight grate indurating furnace begins at the point where the grate feed conveyor discharges the green balls onto the furnace traveling grate and ends where the hardened pellets drop off of the traveling grate.


Taconite iron ore processing means the separation and concentration of iron ore from taconite, a low-grade iron ore, to produce taconite pellets.


Taconite ore means a low-grade iron ore suitable for concentration of magnetite or hematite by fine grinding and magnetic or flotation treatment, from which pellets containing iron can be produced.


Tailings basin means a natural or artificial impoundment in which gangue or other refuse material resulting from the washing, concentration or treatment of ground taconite iron ore is confined.


Wet scrubber means an air pollution control device that removes particulate matter and acid gases from the waste gas stream of stationary sources. The pollutants are removed primarily through the impaction, diffusion, interception and/or absorption of the pollutant onto droplets of liquid. Wet scrubbers include venturi scrubbers, marble bed scrubbers, or impingement scrubbers. For purposes of this subpart, wet scrubbers do not include dynamic wet scrubbers.


[68 FR 61888, Oct. 30, 2003, as amended at 85 FR 45501, July 28, 2020; 89 FR 16437, Mar. 6, 2024]


Table 1 to Subpart RRRRR of Part 63—Particulate Matter Emission Limits

As required in § 63.9590(a), you must comply with each applicable particulate matter emission limit in the following table:


If your affected source is . . .
and the affected source is categorized as . . .
then you must comply with the flow-weighted mean concentration of particulate matter discharged to the atmosphere from the affected source, as determined using the procedures in § 63.9621(b), such that you must not exceed . . .
1. Ore crushing and handling emission unitsExisting0.008 grains per dry standard cubic foot (gr/dscf).
New0.005 gr/dscf.
2. Straight grate indurating furnace processing magnetiteExisting

New
0.01 gr/dscf.

0.006 gr/dscf.
3. Grate kiln indurating furnace processing magnetiteExisting

New
0.01 gr/dscf.

0.006 gr/dscf.
4. Grate kiln indurating furnace processing hematiteExisting

New
0.03 gr/dscf.

0.018 gr/dscf.
5. Finished pellet handling emission unitsExisting

New
0.008 gr/dscf.

0.005 gr/dscf.
6. Ore dryerExisting

New
0.052 gr/dscf.

0.025 gr/dscf.

[68 FR 61888, Oct. 30, 2003, as amended at 89 FR 16438, Mar. 6, 2024]


Table 2 to Subpart RRRRR of Part 63—Mercury Emission Limits for Indurating Furnaces

Table 2 to Subpart RRRRR of Part 63—Mercury Emission Limits for Indurating Furnaces

[As required in § 63.9590(a), you must comply with each applicable mercury emission limit in the following table:]

For . . .
You must meet the following emission limits . . .
1. Indurating furnaces constructed or reconstructed before May 15, 2023Either:

(1) Mercury emissions from each furnace must not exceed 1.4 × 10−5 lb/LT of taconite pellets produced, or

(2) Production-weighted average mercury emissions for a group of indurating furnaces, calculated according to Equation 6 in § 63.9634(m)(3), must not exceed 1.3 × 10−5 lb/LT.

2. Indurating furnaces constructed or reconstructed on or after May 15, 2023Mercury emissions from each furnace must not exceed 2.6 × 10−6 lb/LT.

[89 FR 16438, Mar. 6, 2024]


Table 3 to Subpart RRRRR of Part 63—Hydrogen Chloride and Hydrogen Fluoride Emission Limits for Indurating Furnaces

Table 3 to Subpart RRRRR of Part 63—Hydrogen Chloride and Hydrogen Fluoride Emission Limits for Indurating Furnaces

[As required in § 63.9590(a), you must comply with each applicable hydrogen chloride and hydrogen fluoride emission limit in the following table:]

For . . .
You must meet the following emission limits . . .
1. Indurating furnaces constructed or reconstructed before May 15, 2023Hydrogen chloride emissions must not exceed 4.6 × 10−2 lb/Long Ton of taconite pellets produced.
Hydrogen fluoride emissions must not exceed 1.2 × 10−2 lb/Long Ton of taconite pellets produced.
2. Indurating furnaces constructed or reconstructed on or after May 15, 2023Hydrogen chloride emissions must not exceed 4.4 × 10−4 lb/Long Ton of taconite pellets produced
Hydrogen fluoride emissions must not exceed 3.3 × 10−4 lb/Long Ton of taconite pellets produced.

[89 FR 16438, Mar. 6, 2024]


Table 4 to Subpart RRRRR of Part 63—Applicability of General Provisions to Subpart RRRRR of Part 63

Table 4 to Subpart RRRRR of Part 63—Applicability of General Provisions to Subpart RRRRR of Part 63

[As required in § 63.9650, you must comply with the requirements of the NESHAP General Provisions (40 CFR part 63, subpart A) shown in the following table:]

Citation
Summary of requirement
Am I subject to this requirement?
Explanations
§ 63.1(a)(1)-(4)ApplicabilityYes
§ 63.1(a)(5)[Reserved]No
§ 63.1(a)(6)ApplicabilityYes
§ 63.1(a)(7)-(9)[Reserved]No
§ 63.1(a)(10)-(14)ApplicabilityYes
§ 63.1(b)(1)Initial Applicability DeterminationYes
§ 63.1(b)(2)[Reserved]No
§ 63.1(b)(3)Initial Applicability DeterminationYes
§ 63.1(c)(1)-(2)Applicability After Standard Established, Permit RequirementsYes
§ 63.1(c)(3)-(4)[Reserved]No
§ 63.1(c)(5)Area Source Becomes MajorYes
§ 63.1(c)(6)ReclassificationYes
§ 63.1(d)[Reserved]No
§ 63.1(e)Equivalency of Permit LimitsYes
§ 63.2DefinitionsYes
§ 63.3(a)-(c)Units and AbbreviationsYes
§ 63.4(a)(1)-(2)Prohibited ActivitiesYes
§ 63.4(a)(3)-(5)[Reserved]No
§ 63.4(b)-(c)Circumvention, FragmentationYes
§ 63.5(a)(1)-(2)Construction/Reconstruction, ApplicabilityYes
§ 63.5(b)(1)Construction/Reconstruction, ApplicabilityYes
§ 63.5(b)(2)[Reserved]No
§ 63.5(b)(3)-(4)Construction/Reconstruction, ApplicabilityYes
§ 63.5(b)(5)[Reserved]No
§ 63.5(b)(6)ApplicabilityYes
§ 63.5(c)[Reserved]No
§ 63.5(d)(1)-(4)Application for Approval of Construction or ReconstructionYes
§ 63.5(e)Approval of Construction or ReconstructionYes
§ 63.5(f)Approval Based on State ReviewYes
§ 63.6(a)Compliance with Standards and Maintenance RequirementsYes
§ 63.6(b)(1)-(5)Compliance Dates for New/Reconstructed SourcesYes
§ 63.6(b)(6)[Reserved]No
§ 63.6(b)(7)Compliance Dates for New/Reconstructed SourcesYes
§ 63.6(c)(1)-(2)Compliance Dates for Existing SourcesYes
§ 63.6(c)(3)-(4)[Reserved]No
§ 63.6(c)(5)Compliance Dates for Existing SourcesYes
§ 63.6(d)[Reserved]No
§ 63.6(e)(1)(i)Operation and Maintenance Requirements—General Duty to Minimize EmissionsYes, on or before the compliance date specified in § 63.9600(a). No, after the compliance date specified in § 63.9600(a)See § 63.9600(a) for general duty requirement.
§ 63.6(e)(1)(ii)Operation and Maintenance Requirements—Requirement to Correct Malfunction as Soon as PossibleNo
§ 63.6(e)(1)(iii)Operation and Maintenance Requirements—EnforceabilityYes
§ 63.6(e)(2)[Reserved]No
§ 63.6(e)(3)Startup, Shutdown, Malfunction (SSM) PlanYes, on or before the compliance date specified in § 63.9610(c). No, after the compliance date specified in § 63.9610(c)
§ 63.6(f)(1)SSM exemptionNoSee § 63.9600(a).
§ 63.6(f)(2)-(3)Methods for Determining ComplianceYes
§ 63.6(g)(1)-(3)Alternative Nonopacity StandardYes
§ 63.6(h), except (h)(1)Compliance with Opacity and Visible Emission (VE) StandardsNoOpacity limits in subpart RRRRR are established as part of performance testing in order to set operating limits for ESPs.
§ 63.6(h)(1)Compliance except during SSMNoSee § 63.9600(a).
§ 63.6(i)(1)-(14)Extension of ComplianceYes
§ 63.6(i)(15)[Reserved]No
§ 63.6(i)(16)Extension of ComplianceYes
§ 63.6(j)Presidential Compliance ExemptionYes
§ 63.7(a)(1)-(2)Applicability and Performance Test DatesNoSubpart RRRRR specifies performance test applicability and dates.
§ 63.7(a)(3)-(4)Performance Testing RequirementsYes
§ 63.7(b)NotificationYes
§ 63.7(c)Quality Assurance/Test PlanYes
§ 63.7(d)Testing FacilitiesYes
§ 63.7(e)(1)Conduct of Performance TestsNoSee § 63.9621.
§ 63.7(e)(2)-(4)Conduct of Performance TestsYes
§ 63.7(f)Alternative Test MethodYes
§ 63.7(g)Data AnalysisYesExcept this subpart specifies how and when the performance test results are reported.
§ 63.7(h)Waiver of TestsYes
§ 63.8(a)(1)-(2)Monitoring RequirementsYes
§ 63.8(a)(3)[Reserved]No
§ 63.8(a)(4)Additional Monitoring Requirements for Control Devices in § 63.11NoSubpart RRRRR does not require flares.
§ 63.8(b)(1)-(3)Conduct of MonitoringYes
§ 63.8(c)(1)(i)Operation and Maintenance of CMSYes, on or before the compliance date specified in § 63.9632(b)(4). No, after the compliance date specified in § 63.9632(b)(4)See § 63.9632 for operation and maintenance requirements for monitoring. See § 63.9600(a) for general duty requirement.
§ 63.8(c)(1)(ii)Spare parts for CMS EquipmentYes
§ 63.8(c)(1)(iii)SSM Plan for CMSYes, on or before the compliance date specified in § 63.9632(b)(4). No, after the compliance date specified in § 63.9632(b)(4)
§ 63.8(c)(2)-(3)CMS Operation/MaintenanceYes
§ 63.8(c)(4)Frequency of Operation for CMSNoSubpart RRRRR specifies requirements for operation of CMS.
§ 63.8(c)(5)-(8)CMS RequirementsYesCMS requirements in § 63.8(c)(5) and (6) apply only to COMS for dry ESPs.
§ 63.8(d)(1)-(2)Monitoring Quality ControlYes
§ 63.8(d)(3)Monitoring Quality ControlNoSee § 63.9632(b)(5).
§ 63.8(e)Performance Evaluation for CMSYes
§ 63.8(f)(1)-(5)Alternative Monitoring MethodYes
§ 63.8(f)(6)Relative Accuracy Test Alternative (RATA)YesOnly if using continuous emission monitoring systems to demonstrate compliance with Table 2 to this subpart.
§ 63.8(g)(1)-(g)(4)Data ReductionYes
§ 63.8(g)(5)Data That Cannot Be UsedNoSubpart RRRRR specifies data reduction requirements.
§ 63.9Notification RequirementsYesAdditional notifications for CMS in § 63.9(g) apply to COMS for dry ESPs.
§ 63.9(k)Electronic reporting proceduresYesOnly as specified in § 63.9(j)
§ 63.10(a)Recordkeeping and Reporting, Applicability and General InformationYes
§ 63.10(b)(1)General Recordkeeping RequirementsYes
§ 63.10(b)(2)(i)Records of SSMNoSee § 63.9642 for recordkeeping when there is a deviation from a standard.
§ 63.10(b)(2)(ii)Recordkeeping of Failures to Meet a StandardNoSee § 63.9642 for recordkeeping of (1) date, time and duration; (2) listing of affected source or equipment, and an estimate of the quantity of each regulated pollutant emitted over the standard; and (3) actions to minimize emissions and correct the failure.
§ 63.10(b)(2)(iii)Maintenance RecordsYes
§ 63.10(b)(2)(iv)Actions Taken to Minimize Emissions During SSMNo
§ 63.10(b)(2)(v)Actions Taken to Minimize Emissions During SSMNo
§ 63.10(b)(2)(vi)Recordkeeping for CMS MalfunctionsYes
§ 63.10(b)(2)(vii)-(xii)Recordkeeping for CMSYes
§ 63.10(b)(2)(xiii)Records for Relative Accuracy TestNo
§ 63.10(b)(2)(xiv)Records for NotificationYes
§ 63.10(b)(3)Applicability DeterminationsYes
§ 63.10(c)(1)-(6)Additional Recordkeeping Requirements for Sources with CMSYes
§ 63.10(c)(7)-(8)Records of Excess Emissions and Parameter Monitoring Exceedances for CMSSubpart RRRRR specifies recordkeeping requirements.
§ 63.10(c)(9)[Reserved]No
§ 63.10(c)(10)-(14)CMS RecordkeepingYes
§ 63.10(c)(15)Use of SSM PlanNo
§ 63.10(d)(1)-(2)General Reporting RequirementsYesExcept this subpart specifies how and when the performance test results are reported.
§ 63.10(d)(3)Reporting opacity or VE observationsNoSubpart RRRRR does not have opacity and VE standards that require the use of EPA Method 9 of appendix A-4 to 40 CFR part 60 or EPA Method 22 of appendix A-7 to 40 CFR part 60.
§ 63.10(d)(5)SSM ReportsYes, on or before the compliance date specified in § 63.9641(b)(4). No, after the compliance date specified in § 63.9641(b)(4)See § 63.9641 for malfunction reporting requirements.
§ 63.10(e)Additional Reporting RequirementsYes, except a breakdown of the total duration of excess emissions due to startup/shutdown in63.10(e)(3)(vi)(I) is not required and when the summary report is submitted through CEDRI, the report is not required to be titled “Summary Report-Gaseous and Opacity Excess Emission and Continuous Monitoring System Performance.”The electronic reporting template combines the information from the summary report and excess emission report with the Subpart RRRRR compliance report.
§ 63.10(f)Waiver for Recordkeeping or ReportingYes
§ 63.11Control Device and Work Practice RequirementsNoSubpart RRRRR does not require flares.
§ 63.12(a)-(c)State Authority and DelegationsYes
§ 63.13(a)-(c)State/Regional AddressesYes
§ 63.14(a)-(t)Incorporation by ReferenceYes
§ 63.15(a)-(b)Availability of Information and ConfidentialityYes
§ 63.16Performance Track ProvisionsYes

[89 FR 16438, Mar. 6, 2024]


Subpart SSSSS—National Emission Standards for Hazardous Air Pollutants for Refractory Products Manufacturing


Source:68 FR 18747, Apr. 16, 2003, unless otherwise noted.

What This Subpart Covers

§ 63.9780 What is the purpose of this subpart?

This subpart establishes national emission standards for hazardous air pollutants (NESHAP) for refractory products manufacturing facilities. This subpart also establishes requirements to demonstrate initial and continuous compliance with the emission limitations.


§ 63.9782 Am I subject to this subpart?

You are subject to this subpart if you own or operate a refractory products manufacturing facility that is, is located at, or is part of, a major source of hazardous air pollutant (HAP) emissions according to the criteria in paragraphs (a) and (b) of this section.


(a) A refractory products manufacturing facility is a plant site that manufactures refractory products (refractory bricks, refractory shapes, monolithics, kiln furniture, crucibles, and other materials used for lining furnaces and other high temperature process units), as defined in § 63.9824. Refractory products manufacturing facilities typically process raw material by crushing, grinding, and screening; mixing the processed raw materials with binders and other additives; forming the refractory mix into shapes; and drying and firing the shapes.


(b) A major source of HAP is a plant site that emits or has the potential to emit any single HAP at a rate of 9.07 megagrams (10 tons) or more per year or any combination of HAP at a rate of 22.68 megagrams (25 tons) or more per year.


§ 63.9784 What parts of my plant does this subpart cover?

(a) This subpart applies to each new, reconstructed, or existing affected source at a refractory products manufacturing facility.


(b) The existing affected sources are shape dryers, curing ovens, and kilns that are used to manufacture refractory products that use organic HAP; shape preheaters, pitch working tanks, defumers, and coking ovens that are used to produce pitch-impregnated refractory products; kilns that are used to manufacture chromium refractory products; and kilns that are used to manufacture clay refractory products.


(c) The new or reconstructed affected sources are shape dryers, curing ovens, and kilns that are used to manufacture refractory products that use organic HAP; shape preheaters, pitch working tanks, defumers, and coking ovens used to produce pitch-impregnated refractory products; kilns that are used to manufacture chromium refractory products; and kilns that are used to manufacture clay refractory products.


(d) Shape dryers, curing ovens, kilns, coking ovens, defumers, shape preheaters, and pitch working tanks that are research and development (R&D) process units are not subject to the requirements of this subpart. (See definition of research and development process unit in § 63.9824).


(e) A source is a new affected source if you began construction of the affected source after June 20, 2002, and you met the applicability criteria at the time you began construction.


(f) An affected source is reconstructed if you meet the criteria as defined in § 63.2.


(g) An affected source is existing if it is not new or reconstructed.


§ 63.9786 When do I have to comply with this subpart?

(a) If you have a new or reconstructed affected source, you must comply with this subpart according to paragraphs (a)(1) and (2) of this section.


(1) If the initial startup of your affected source is before April 16, 2003, then you must comply with the emission limitations for new and reconstructed sources in this subpart no later than April 16, 2003, except as otherwise specified in §§ 63.9792, 63.9812(c) and (e), and 63.9814(b)(6) and Tables 1 through 11 to this subpart.


(2) If the initial startup of your affected source is after April 16, 2003, then you must comply with the emission limitations for new and reconstructed sources in this subpart upon initial startup of your affected source, except as otherwise specified in §§ 63.9792, 63.9812(c) and (e), and 63.9814(b)(6) and Tables 1 through 11 to this subpart.


(b) If you have an existing affected source, you must comply with the emission limitations for existing sources no later than April 17, 2006, except as otherwise specified in §§ 63.9792, 63.9812(c) and (e), and 63.9814(b)(6) and Tables 1 through 11 to this subpart.


(c) You must be in compliance with this subpart when you conduct a performance test on an affected source.


(d) If you have an existing area source that increases its emissions or its potential to emit such that it becomes a major source of HAP, you must be in compliance with this subpart according to paragraphs (d)(1) and (2) of this section.


(1) Any portion of the existing facility that is a new affected source or a new reconstructed source must be in compliance with this subpart upon startup.


(2) All other parts of the existing facility must be in compliance with this subpart by 3 years after the date the area source becomes a major source, except as otherwise specified in §§ 63.9792, 63.9812(c) and (e), and 63.9814(b)(6) and Tables 1 through 11 to this subpart.


(e) If you have a new area source (i.e., an area source for which construction or reconstruction was commenced after June 20, 2002) that increases its emissions or its potential to emit such that it becomes a major source of HAP, you must be in compliance with this subpart upon initial startup of your affected source as a major source.


(f) You must meet the notification requirements in § 63.9812 according to the schedule in § 63.9812 and in 40 CFR part 63, subpart A. Some of the notifications must be submitted before you are required to comply with the emission limitations in this subpart.


[68 FR 18747, Apr. 16, 2003, as amended at 86 FR 66063, Nov. 19, 2021]


Emission Limitations and Work Practice Standards

§ 63.9788 What emission limits, operating limits, and work practice standards must I meet?

(a) You must meet each emission limit in Table 1 to this subpart that applies to you.


(b) You must meet each operating limit in Table 2 to this subpart that applies to you.


(c) You must meet each work practice standard in Table 3 to this subpart that applies to you.


§ 63.9790 What are my options for meeting the emission limits?

To meet the emission limits in Table 1 to this subpart, you must use one or both of the options listed in paragraphs (a) and (b) of this section.


(a) Emissions control system. Use an emissions capture and collection system and an add-on air pollution control device (APCD) and demonstrate that the resulting emissions or emissions reductions meet the applicable emission limits in Table 1 to this subpart, and demonstrate that the capture and collection system and APCD meet the applicable operating limits in Table 2 to this subpart.


(b) Process changes. Use raw materials that have little or no potential to emit HAP during the refractory products manufacturing process or implement manufacturing process changes and demonstrate that the resulting emissions or emissions reductions meet the applicable emission limits in Table 1 to this subpart without an add-on APCD.


General Compliance Requirements

§ 63.9792 What are my general requirements for complying with this subpart?

(a) You must be in compliance with the emission limitations (including operating limits and work practice standards) in this subpart at all times, except during periods specified in paragraphs (a)(1) and (2) of this section before May 19, 2022. You must be in compliance with the emission limitations (including operating limits and work practice standards) in this subpart at all times, on or after May 19, 2022.


(1) Periods of startup, shutdown, and malfunction.


(2) Periods of scheduled maintenance on a control device that is used on an affected continuous kiln, as specified in paragraph (e) of this section.


(b) Except as specified in paragraph (e) of this section, before May 19, 2022, you must always operate and maintain your affected source, including air pollution control and monitoring equipment, according to the provisions in § 63.6(e)(1)(i). During the period between the compliance date specified for your affected source in § 63.9786 and the date upon which continuous monitoring systems have been installed and validated and any applicable operating limits have been established, you must maintain a log detailing the operation and maintenance of the process and emissions control equipment. On and after May 19, 2022, at all times, you must operate and maintain any affected source, including associated air pollution control equipment and monitoring equipment, in a manner consistent with safety and good air pollution control practices for minimizing emissions. The general duty to minimize emissions does not require you to make any further efforts to reduce emissions if levels required by the applicable standard have been achieved. Determination of whether a source is operating in compliance with operation and maintenance requirements will be based on information available to the Administrator that may include, but is not limited to, monitoring results, review of operation and maintenance procedures, review of operation and maintenance records, and inspection of the affected source.


(c) Before May 19, 2022, you must develop a written startup, shutdown, and malfunction plan (SSMP) according to the provisions in § 63.6(e)(3). On or after May 19, 2022, you are not required to develop a written SSMP according to the provisions in § 63.6(e)(3).


(d) You must prepare and implement a written operation, maintenance, and monitoring (OM&M) plan according to the requirements in § 63.9794.


(e) If you own or operate an affected continuous kiln used to manufacture refractory products that use organic HAP and you must perform scheduled maintenance on the THC control device for that kiln, you may bypass the kiln THC control device and continue operating the kiln subject to the alternative standard established in this paragraph upon approval by the Administrator, provided you satisfy the conditions listed in paragraphs (e)(1) through (3) of this section.


(1) You must request approval from the Administrator to bypass the control device while the scheduled maintenance is performed. You must submit a separate request each time you plan to bypass the control device, and your request must include the information specified in paragraphs (e)(1)(i) through (vi) of this section.


(i) Reason for the scheduled maintenance.


(ii) Explanation for why the maintenance cannot be performed when the kiln is shut down.


(iii) Detailed description of the maintenance activities.


(iv) Time required to complete the maintenance.


(v) How you will minimize HAP emissions from the kiln during the period when the control device is out of service.


(vi) How you will minimize the time when the kiln is operating and the control device is out of service for scheduled maintenance.


(2) Before May 19, 2022, you must minimize HAP emissions during the period when the kiln is operating, and the control device is out of service. On and after May 19, 2022, you must minimize HAP emissions during the period when the kiln is operating and the control device is out of service by complying with the applicable standard in Table 3 to this subpart.


(3) You must minimize the time period during which the kiln is operating and the control device is out of service. On and after May 19, 2022, the total time during which the kiln is operating and the control device is out of service for each year on a 12-month rolling basis must not exceed 750 hours.


(f) You must be in compliance with the provisions of subpart A of this part, except as noted in Table 11 to this subpart.


[68 FR 18747, Apr. 16, 2003, as amended at 71 FR 20471, Apr. 20, 2006; 86 FR 66063, Nov. 19, 2021]


§ 63.9794 What do I need to know about operation, maintenance, and monitoring plans?

(a) For each continuous parameter monitoring system (CPMS) required by this subpart, you must develop, implement, make available for inspection, and revise, as necessary, an OM&M plan that includes the information in paragraphs (a)(1) through (13) of this section.


(1) A list and identification of each process and add-on APCD that is required by this subpart to be monitored, the type of monitoring device that will be used, and the operating parameters that will be monitored.


(2) Specifications for the sensor, signal analyzer, and data collection system.


(3) A monitoring schedule that specifies the frequency that the parameter values will be determined and recorded.


(4) The operating limits for each parameter that represent continuous compliance with the emission limitations in § 63.9788, based on values of the monitored parameters recorded during performance tests.


(5) Procedures for installing the CPMS at a measurement location relative to each process unit or APCD such that measurement is representative of control of emissions.


(6) Procedures for the proper operation and routine and long-term maintenance of each process unit and APCD, including a maintenance and inspection schedule that is consistent with the manufacturer’s recommendations.


(7) Before May 19, 2022, procedures for the proper operation and maintenance of monitoring equipment consistent with the requirements in §§ 63.8(c)(1), (3), (4)(ii), (7), and (8), and 63.9804. On or after May 19, 2022, procedures for the proper operation and maintenance of monitoring equipment consistent with the requirements in §§ 63.8(c)(3), (4)(ii), (7), and (8), and 63.9804.


(8) Before May 19, 2022, ongoing data quality assurance procedures in accordance with the general requirements of § 63.8(d). On or after May 19, 2022, ongoing data quality assurance procedures consistent with the requirements in § 63.8(d)(1) and (2). You must keep these written procedures on record for the life of the affected source or until the affected source is no longer subject to the provisions of this part, to be made available for inspection, upon request, by the Administrator. If the performance evaluation plan in § 63.8(d)(2) is revised, you must keep previous (i.e., superseded) versions of the performance evaluation plan on record to be made available for inspection, upon request, by the Administrator, for a period of 5 years after each revision to the plan. The program of corrective action should be included in the plan required under § 63.8(d)(2).


(9) Procedures for evaluating the performance of each CPMS.


(10) Procedures for responding to operating parameter deviations, including the procedures in paragraphs (a)(10)(i) through (iii) of this section:


(i) Procedures for determining the cause of the operating parameter deviation.


(ii) Actions for correcting the deviation and returning the operating parameters to the allowable limits.


(iii) Procedures for recording the times that the deviation began and ended, and when corrective actions were initiated and completed.


(11) Procedures for keeping records to document compliance and reporting in accordance with the requirements of § 63.10(c), (e)(1), and (e)(2)(i).


(12) Before Novermber 19, 2021, if you operate a kiln that is subject to the limits on the type of fuel used, as specified in items 3 and 4 of Table 3 to subpart SSSSS, procedures for using alternative fuels. On and after Novermber 19, 2021, you may not use a fuel other than natural gas or equivalent to fire the affected kiln.


(13) If you operate an affected continuous kiln used to manufacture refractory products that use organic HAP and you plan to take the kiln THC control device out of service for scheduled maintenance, as specified in § 63.9792(e), the procedures specified in paragraphs (a)(13)(i) and (ii) of this section.


(i) Procedures for minimizing HAP emissions from the kiln during periods of scheduled maintenance of the kiln control device when the kiln is operating and the control device is out of service. On or after May 19, 2022, document the average organic HAP processing rate for that kiln (i.e., the average organic HAP processing rate based on (a) the actual production on a 6-month rolling basis (not to include periods of kiln shut down) or (b) the HAP processing rate (lb/hr) that coincides with the lowest hour of the most recent 3-hour performance test, whichever is lower), the mass fraction of organic HAP in the resins, binders, and additives for each product manufactured in the kiln and procedures for ensuring that the actual organic HAP processing rate on an hourly basis does not exceed the average organic HAP processing rate.


(ii) Procedures for minimizing any period of scheduled maintenance on the kiln control device when the kiln is operating and the control device is out of service. On or after May 19, 2022, procedures for ensuring that the total time during which the kiln is operating and the control device is out of service does not exceed 750 hours for each year on a 12-month rolling basis.


(b) Changes to the operating limits in your OM&M plan require a new performance test. If you are revising an operating limit parameter value, you must meet the requirements in paragraphs (b)(1) and (2) of this section.


(1) Submit a Notification of Performance Test to the Administrator as specified in § 63.7(b).


(2) After completing the performance tests to demonstrate that compliance with the emission limits can be achieved at the revised operating limit parameter value, you must submit the summary of the performance test results and the revised operating limits as part of the Notification of Compliance Status required under § 63.9(h) and the complete test report according to § 63.9814(h).


(c) If you are revising the inspection and maintenance procedures in your OM&M plan, you do not need to conduct a new performance test.


[68 FR 18747, Apr. 16, 2003, as amended at 86 FR 66064, Nov. 19, 2021]


Testing and Initial Compliance Requirements

§ 63.9796 By what date must I conduct performance tests?

You must conduct performance tests within 180 calendar days after the compliance date that is specified for your source in § 63.9786 and according to the provisions in § 63.7(a)(2).


§ 63.9798 When must I conduct subsequent performance tests?

(a) You must conduct a performance test every 5 years following the initial performance test, as part of renewing your 40 CFR part 70 or 40 CFR part 71 operating permit.


(b) You must conduct a performance test when you want to change the parameter value for any operating limit specified in your OM&M plan.


(c) If you own or operate a source that is subject to the emission limits specified in items 2 through 9 of Table 1 to this subpart, you must conduct a performance test on the source(s) listed in paragraphs (c)(1) and (2) of this section before you start production of any refractory product for which the organic HAP processing rate is likely to exceed by more than 10 percent the maximum organic HAP processing rate established during the most recent performance test on that same source.


(1) Each affected shape dryer or curing oven that is used to process the refractory product with the higher organic HAP processing rate.


(2) Each affected kiln that follows an affected shape dryer or curing oven and is used to process the refractory product with the higher organic HAP processing rate.


(d) If you own or operate a kiln that is subject to the emission limits specified in item 5 or 9 of Table 1 to this subpart, you must conduct a performance test on the affected kiln following any process changes that are likely to increase organic HAP emissions from the kiln (e.g., a decrease in the curing cycle time for a curing oven that precedes the affected kiln in the process line).


(e) If you own or operate a clay refractory products kiln that is subject to the emission limits specified in item 10 or 11 of Table 1 to this subpart and is controlled with a dry limestone adsorber (DLA), you must conduct a performance test on the affected kiln following any change in the source of limestone used in the DLA.


§ 63.9800 How do I conduct performance tests and establish operating limits?

(a) You must conduct each performance test in Table 4 to this subpart that applies to you.


(b) Before conducting the performance test, you must install and validate all monitoring equipment.


(c) Before May 19, 2022, each performance test must be conducted according to the requirements in § 63.7 and under the specific conditions in Table 4 to this subpart. On or after May 19, 2022, each performance test must be conducted under the specific conditions in Table 4 to this subpart.


(d) Before May 19, 2022, you may not conduct performance tests during periods of startup, shutdown, or malfunction, as specified in § 63.7(e)(1). On or after May 19, 2022, you may not conduct performance tests during periods of malfunction. You also may not conduct performance tests during periods of startup or shutdown. You must record the process information that is necessary to document operating conditions during the test and include in such record an explanation to support that such conditions represent normal operation. You must make available to the Administrator such records as may be necessary to determine the conditions of performance tests.


(e) You must conduct separate test runs for at least the duration specified for each performance test required in this section, as specified in § 63.7(e)(3) and Table 4 to this subpart.


(f) For batch process sources, you must satisfy the requirements specified in paragraphs (f)(1) through (5) of this section.


(1) You must conduct at least two test runs.


(2) Each test run must last an entire batch cycle unless you develop an emissions profile, as specified in items 8(a)(i)(4) and 17(b)(i)(4) of Table 4 to this subpart, or you satisfy the conditions for terminating a test run prior to the completion of a batch cycle as specified in item 8(a)(i)(5) of Table 4 to this subpart.


(3) Each test run must be performed over a separate batch cycle unless you satisfy the conditions for conducting both test runs over a single batch cycle, as described in paragraphs (f)(3)(i) and (ii) of this section.


(i) You do not produce the product that corresponds to the maximum organic HAP processing rate for that batch process source in consecutive batch cycles.


(ii) To produce that product in two consecutive batch cycles would disrupt production of other refractory products.


(4) If you want to conduct a performance test over a single batch cycle, you must include in your Notification of Performance Test the rationale for testing over a single batch cycle.


(5) If you are granted approval to conduct a performance test over a single batch cycle, you must use paired sampling trains and collect two sets of emissions data. Each set of data can be considered a separate test run.


(g) You must use the data gathered during the performance test and the equations in paragraphs (g)(1) through (4) of this section to determine compliance with the emission limitations.


(1) To determine compliance with the total hydrocarbon (THC) emission concentration limit listed in Table 1 to this subpart, you must calculate your emission concentration corrected to 18 percent oxygen for each test run using Equation 1 of this section:





Where:

C THC-C = THC concentration, corrected to 18 percent oxygen, parts per million by volume, dry basis (ppmvd)

C THC = THC concentration (uncorrected), ppmvd

CO2 = oxygen concentration, percent.

(2) To determine compliance with any of the emission limits based on percentage reduction across an emissions control system specified in Table 1 to this subpart, you must calculate the percentage reduction for each test run using Equation 2 of this section:





Where:

PR = percentage reduction, percent

ERi = mass emissions rate of specific HAP or pollutant (THC, HF, or HCl) entering the control device, kilograms (pounds) per hour

ERo = mass emissions rate of specific HAP or pollutant (THC, HF, or HCl) exiting the control device, kilograms (pounds) per hour.

(3) To determine compliance with production-based hydrogen fluoride (HF) and hydrogen chloride (HCl) emission limits in Table 1 to this subpart, you must calculate your mass emissions per unit of uncalcined clay processed for each test run using Equation 3 of this section:





Where:

MP = mass per unit of production, kilograms of pollutant per megagram (pounds per ton) of uncalcined clay processed

ER = mass emissions rate of specific HAP (HF or HCl) during each performance test run, kilograms (pounds) per hour

P = average uncalcined clay processing rate for the performance test, megagrams (tons) of uncalcined clay processed per hour.

(4) To determine compliance with the Hg emission concentration limit listed in Table 1 to this subpart, you must calculate your emission concentration corrected to 18 percent oxygen for each test run using Equation 4 of this section:




Where:

CHg-C = Hg concentration, corrected to 18 percent oxygen, micrograms per dry standard cubic meters (µg/dscm)

CHg = Hg concentration (uncorrected), µg/dscm

CO2 = oxygen concentration, percent.

(h) You must establish each site-specific operating limit in Table 2 to this subpart that applies to you, as specified in Table 4 to this subpart.


(i) For each affected source that is equipped with an add-on APCD that is not addressed in Table 2 to this subpart or that is using process changes as a means of meeting the emission limits in Table 1 to this subpart, you must meet the requirements in § 63.8(f) and paragraphs (i)(1) through (3) of this section.


(1) For sources subject to the THC concentration limit specified in item 3 or 7 of Table 1 to this subpart, you must satisfy the requirements specified in paragraphs (i)(1)(i) through (iii) of this section.


(i) You must install a THC continuous emissions monitoring system (CEMS) at the outlet of the control device or in the stack of the affected source.


(ii) You must meet the requirements specified in Performance Specification (PS) 8 of 40 CFR part 60, appendix B.


(iii) You must meet the requirements specified in Procedure 1 of 40 CFR part 60, appendix F.


(2) For sources subject to the emission limits specified in item 3, 4, 7, or 8 of Table 1 to this subpart, you must submit a request for approval of alternative monitoring methods to the Administrator no later than the submittal date for the Notification of Performance Test, as specified in § 63.9812(d). The request must contain the information specified in paragraphs (i)(2)(i) through (v) of this section.


(i) Description of the alternative add-on APCD or process changes.


(ii) Type of monitoring device or method that will be used, including the sensor type, location, inspection procedures, quality assurance and quality control measures, and data recording device.


(iii) Operating parameters that will be monitored.


(iv) Frequency that the operating parameter values will be determined and recorded to establish continuous compliance with the operating limits.


(v) Averaging time.


(3) You must establish site-specific operating limits during the performance test based on the information included in the approved alternative monitoring methods request and, as applicable, as specified in Table 4 to this subpart.


[68 FR 18747, Apr. 16, 2003, as amended at 86 FR 66064, Nov. 19, 2021]


§ 63.9802 How do I develop an emissions profile?

If you decide to develop an emissions profile for an affected batch process source; as indicated in item 8(a)(i)(4) or 17(b)(i)(4) of Table 4 to this subpart, you must measure and record mass emissions of the applicable pollutant throughout a complete batch cycle of the affected batch process source according to the procedures described in paragraph (a) or (b) of this section.


(a) If your affected batch process source is subject to the THC concentration limit specified in item 6(a), 7(a), 8, or 9 of Table 1 to this subpart or the THC percentage reduction limit specified in item 6(b) or 7(b) of Table 1 to this subpart, you must measure and record the THC mass emissions rate at the inlet to the control device using the test methods, averaging periods, and procedures specified in items 10(a) and (b) of Table 4 to this subpart for each complete hour of the batch process cycle.


(b) If your affected batch process source is subject to the HF and HCl percentage reduction emission limits in item 11 of Table 1 to this subpart, you must measure and record the HF mass emissions rate at the inlet to the control device through a series of 1-hour test runs according to the test method specified in item 14(a) of Table 4 to this subpart for each complete hour of the batch process cycle.


§ 63.9804 What are my monitoring system installation, operation, and maintenance requirements?

(a) You must install, operate, and maintain each CPMS required by this subpart according to your OM&M plan and the requirements in paragraphs (a)(1) through (15) of this section.


(1) You must satisfy all applicable requirements of performance specifications for CPMS specified in 40 CFR part 60, appendix B, upon promulgation of such performance specifications.


(2) You must satisfy all applicable requirements of quality assurance (QA) procedures for CPMS specified in 40 CFR part 60, appendix F, upon promulgation of such QA procedures.


(3) You must install each sensor of your CPMS in a location that provides representative measurement of the appropriate parameter over all operating conditions, taking into account the manufacturer’s guidelines.


(4) You must use a CPMS that is capable of measuring the appropriate parameter over a range that extends from a value of at least 20 percent less than the lowest value that you expect your CPMS to measure, to a value of at least 20 percent greater than the highest value that you expect your CPMS to measure.


(5) You must use a data acquisition and recording system that is capable of recording values over the entire range specified in paragraph (a)(4) of this section.


(6) You must use a signal conditioner, wiring, power supply, and data acquisition and recording system that are compatible with the output signal of the sensors used in your CPMS.


(7) You must perform an initial calibration of your CPMS based on the procedures specified in the manufacturer’s owner’s manual.


(8) You must use a CPMS that is designed to complete a minimum of one cycle of operation for each successive 15-minute period. To have a valid hour of data, you must have at least three of four equally-spaced data values (or at least 75 percent of the total number of values if you collect more than four data values per hour) for that hour (not including startup, shutdown, malfunction, or out-of-control periods).


(9) You must record valid data from at least 90 percent of the hours during which the affected source or process operates.


(10) You must determine and record the 15-minute block averages of all measurements, calculated after every 15 minutes of operation as the average of the previous 15 operating minutes (not including periods of startup, shutdown, or malfunction).


(11) You must determine and record the 3-hour block averages of all 15-minute recorded measurements, calculated after every 3 hours of operation as the average of the previous 3 operating hours (not including periods of startup, shutdown, or malfunction).


(12) You must record the results of each inspection, calibration, initial validation, and accuracy audit.


(13) At all times, you must maintain your CPMS in accordance with § 63.9792(b), including, but not limited to, keeping the necessary parts readily available for routine repairs of the CPMS.


(14) You must perform an initial validation of your CPMS under the conditions specified in paragraphs (14)(i) and (ii) of this section.


(i) Prior to the initial performance test on the affected source for which the CPMS is required.


(ii) Within 180 days of your replacing or relocating one or more of the sensors of your CPMS.


(15) Except for redundant sensors, as defined in § 63.9824, any device that you use to conduct an initial validation or accuracy audit of your CPMS must meet the accuracy requirements specified in paragraphs (15)(i) and (ii) of this section.


(i) The device must have an accuracy that is traceable to National Institute of Standards and Technology (NIST) standards.


(ii) The device must be at least three times as accurate as the required accuracy for the CPMS.


(b) For each temperature CPMS that is used to monitor the combustion chamber temperature of a thermal oxidizer or the catalyst bed inlet temperature of a catalytic oxidizer, you must meet the requirements in paragraphs (a) and (b)(1) through (6) of this section.


(1) Use a temperature CPMS with a minimum accuracy of ±1.0 percent of the temperature value or 2.8 degrees Celsius (°C) (5 degrees Fahrenheit (°F)), whichever is greater.


(2) Use a data recording system with a minimum resolution of one-half or better of the required CPMS accuracy specified in paragraph (b)(1) of this section.


(3) Perform an initial validation of your CPMS according to the requirements in paragraph (3)(i) or (ii) of this section.


(i) Place the sensor of a calibrated temperature measurement device adjacent to the sensor of your temperature CPMS in a location that is subject to the same environment as the sensor of your temperature CPMS. The calibrated temperature measurement device must satisfy the accuracy requirements of paragraph (a)(15) of this section. While the process and control device that is monitored by your CPMS are operating normally, record concurrently and compare the temperatures measured by your temperature CPMS and the calibrated temperature measurement device. Using the calibrated temperature measurement device as the reference, the temperature measured by your CPMS must be within the accuracy specified in paragraph (b)(1) of this section.


(ii) Perform any of the initial validation methods for temperature CPMS specified in performance specifications for CPMS established in 40 CFR part 60, appendix B.


(4) Perform an accuracy audit of your temperature CPMS at least quarterly, according to the requirements in paragraph (b)(4)(i), (ii), or (iii) of this section.


(i) If your temperature CPMS includes a redundant temperature sensor, record three pairs of concurrent temperature measurements within a 24-hour period. Each pair of concurrent measurements must consist of a temperature measurement by each of the two temperature sensors. The minimum time interval between any two such pairs of consecutive temperature measurements is 1 hour. The measurements must be taken during periods when the process and control device that is monitored by your temperature CPMS are operating normally. Calculate the mean of the three values for each temperature sensor. The mean values must agree within the required overall accuracy of the CPMS, as specified in paragraph (b)(1) of this section.


(ii) If your temperature CPMS does not include a redundant temperature sensor, place the sensor of a calibrated temperature measurement device adjacent to the sensor of your temperature CPMS in a location that is subject to the same environment as the sensor of your temperature CPMS. The calibrated temperature measurement device must satisfy the accuracy requirements of paragraph (a)(15) of this section. While the process and control device that is monitored by your temperature CPMS are operating normally, record concurrently and compare the temperatures measured by your CPMS and the calibrated temperature measurement device. Using the calibrated temperature measurement device as the reference, the temperature measured by your CPMS must be within the accuracy specified in paragraph (b)(1) of this section.


(iii) Perform any of the accuracy audit methods for temperature CPMS specified in QA procedures for CPMS established in 40 CFR part 60, appendix F.


(5) Conduct an accuracy audit of your CPMS following any 24-hour period throughout which the temperature measured by your CPMS exceeds the manufacturer’s specified maximum operating temperature range, or install a new temperature sensor.


(6) If your CPMS is not equipped with a redundant temperature sensor, perform at least quarterly a visual inspection of all components of the CPMS for integrity, oxidation, and galvanic corrosion.


(c) For each pressure CPMS that is used to monitor the pressure drop across a DLA or wet scrubber, you must meet the requirements in paragraphs (a) and (c)(1) through (7) of this section.


(1) Use a pressure CPMS with a minimum accuracy of ±5.0 percent or 0.12 kilopascals (kPa) (0.5 inches of water column (in. w.c.)), whichever is greater.


(2) Use a data recording system with a minimum resolution of one-half the required CPMS accuracy specified in paragraph (c)(1) of this section, or better.


(3) Perform an initial validation of your pressure CPMS according to the requirements in paragraph (c)(3)(i) or (ii) of this section.


(i) Place the sensor of a calibrated pressure measurement device adjacent to the sensor of your pressure CPMS in a location that is subject to the same environment as the sensor of your pressure CPMS. The calibrated pressure measurement device must satisfy the accuracy requirements of paragraph (a)(15) of this section. While the process and control device that is monitored by your CPMS are operating normally, record concurrently and compare the pressure measured by your CPMS and the calibrated pressure measurement device. Using the calibrated pressure measurement device as the reference, the pressure measured by your CPMS must be within the accuracy specified in paragraph (c)(1) of this section.


(ii) Perform any of the initial validation methods for pressure CPMS specified in performance specifications for CPMS established in 40 CFR part 60, appendix B.


(4) Perform an accuracy audit of your pressure CPMS at least quarterly, according to the requirements in paragraph (c)(4)(i), (ii), or (iii) of this section.


(i) If your pressure CPMS includes a redundant pressure sensor, record three pairs of concurrent pressure measurements within a 24-hour period. Each pair of concurrent measurements must consist of a pressure measurement by each of the two pressure sensors. The minimum time interval between any two such pairs of consecutive pressure measurements is 1 hour. The measurements must be taken during periods when the process and control device that is monitored by your CPMS are operating normally. Calculate the mean of the three pressure measurement values for each pressure sensor. The mean values must agree within the required overall accuracy of the CPMS, as specified in paragraph (c)(1) of this section.


(ii) If your pressure CPMS does not include a redundant pressure sensor, place the sensor of a calibrated pressure measurement device adjacent to the sensor of your pressure CPMS in a location that is subject to the same environment as the sensor of your pressure CPMS. The calibrated pressure measurement device must satisfy the accuracy requirements of paragraph (a)(15) of this section. While the process and control device that is monitored by your pressure CPMS are operating normally, record concurrently and compare the pressure measured by your CPMS and the calibrated pressure measurement device. Using the calibrated pressure measurement device as the reference, the pressure measured by your CPMS must be within the accuracy specified in paragraph (c)(1) of this section.


(iii) Perform any of the accuracy audit methods for pressure CPMS specified in QA procedures for CPMS established in 40 CFR part 60, appendix F.


(5) Conduct an accuracy audit of your CPMS following any 24-hour period throughout which the pressure measured by your CPMS exceeds the manufacturer’s specified maximum operating pressure range, or install a new pressure sensor.


(6) At least monthly, check all mechanical connections on your CPMS for leakage.


(7) If your CPMS is not equipped with a redundant pressure sensor, perform at least quarterly a visual inspection of all components of the CPMS for integrity, oxidation, and galvanic corrosion.


(d) For each liquid flow rate CPMS that is used to monitor the liquid flow rate in a wet scrubber, you must meet the requirements in paragraphs (a) and (d)(1) through (7) of this section.


(1) Use a flow rate CPMS with a minimum accuracy of ±5.0 percent or 1.9 liters per minute (L/min) (0.5 gallons per minute (gal/min)), whichever is greater.


(2) Use a data recording system with a minimum resolution of one-half the required CPMS accuracy specified in paragraph (d)(1) of this section, or better.


(3) Perform an initial validation of your CPMS according to the requirements in paragraph (3)(i) or (ii) of this section.


(i) Use a calibrated flow rate measurement system to measure the liquid flow rate in a location that is adjacent to the measurement location for your flow rate CPMS and is subject to the same environment as your flow rate CPMS. The calibrated flow rate measurement device must satisfy the accuracy requirements of paragraph (a)(15) of this section. While the process and control device that is monitored by your flow rate CPMS are operating normally, record concurrently and compare the flow rates measured by your flow rate CPMS and the calibrated flow rate measurement device. Using the calibrated flow rate measurement device as the reference, the flow rate measured by your CPMS must be within the accuracy specified in paragraph (d)(1) of this section.


(ii) Perform any of the initial validation methods for liquid flow rate CPMS specified in performance specifications for CPMS established in 40 CFR part 60, appendix B.


(4) Perform an accuracy audit of your flow rate CPMS at least quarterly, according to the requirements in paragraph (d)(4)(i), (ii), or (iii) of this section.


(i) If your flow rate CPMS includes a redundant sensor, record three pairs of concurrent flow rate measurements within a 24-hour period. Each pair of concurrent measurements must consist of a flow rate measurement by each of the two flow rate sensors. The minimum time interval between any two such pairs of consecutive flow rate measurements is 1 hour. The measurements must be taken during periods when the process and control device that is monitored by your flow rate CPMS are operating normally. Calculate the mean of the three flow rate measurement values for each flow rate sensor. The mean values must agree within the required overall accuracy of the CPMS, as specified in paragraph (d)(1) of this section.


(ii) If your flow rate CPMS does not include a redundant flow rate sensor, place the sensor of a calibrated flow rate measurement device adjacent to the sensor of your flow rate CPMS in a location that is subject to the same environment as the sensor of your flow rate CPMS. The calibrated flow rate measurement device must satisfy the accuracy requirements of paragraph (a)(15) of this section. While the process and control device that is monitored by your flow rate CPMS are operating normally, record concurrently and compare the flow rate measured by your pressure CPMS and the calibrated flow rate measurement device. Using the calibrated flow rate measurement device as the reference, the flow rate measured by your CPMS must be within the accuracy specified in paragraph (d)(1) of this section.


(iii) Perform any of the accuracy audit methods for liquid flow rate CPMS specified in QA procedures for CPMS established in 40 CFR part 60, appendix F.


(5) Conduct an accuracy audit of your flow rate CPMS following any 24-hour period throughout which the flow rate measured by your CPMS exceeds the manufacturer’s specified maximum operating range, or install a new flow rate sensor.


(6) At least monthly, check all mechanical connections on your CPMS for leakage.


(7) If your CPMS is not equipped with a redundant flow rate sensor, perform at least quarterly a visual inspection of all components of the CPMS for integrity, oxidation, and galvanic corrosion.


(e) For each pH CPMS that is used to monitor the pH of a wet scrubber liquid, you must meet the requirements in paragraphs (a) and (e)(1) through (5) of this section.


(1) Use a pH CPMS with a minimum accuracy of ±0.2 pH units.


(2) Use a data recording system with a minimum resolution of 0.1 pH units, or better.


(3) Perform an initial validation of your pH CPMS according to the requirements in paragraph (e)(3)(i) or (ii) of this section.


(i) Perform a single-point calibration using an NIST-certified buffer solution that is accurate to within ±0.02 pH units at 25 °C (77 °F). If the expected pH of the liquid that is monitored lies in the acidic range (less than 7 pH), use a buffer solution with a pH value of 4.00. If the expected pH of the liquid that is monitored is neutral or lies in the basic range (equal to or greater than 7 pH), use a buffer solution with a pH value of 10.00. Place the electrode of your pH CPMS in the container of buffer solution. Record the pH measured by your CPMS. Using the certified buffer solution as the reference, the pH measured by your CPMS must be within the accuracy specified in paragraph (e)(1) of this section.


(ii) Perform any of the initial validation methods for pH CPMS specified in performance specifications for CPMS established in 40 CFR part 60, appendix B.


(4) Perform an accuracy audit of your pH CPMS at least weekly, according to the requirements in paragraph (e)(4)(i), (ii), or (iii) of this section.


(i) If your pH CPMS includes a redundant pH sensor, record the pH measured by each of the two pH sensors. The measurements must be taken during periods when the process and control device that is monitored by your pH CPMS are operating normally. The two pH values must agree within the required overall accuracy of the CPMS, as specified in paragraph (e)(1) of this section.


(ii) If your pH CPMS does not include a redundant pH sensor, perform a single point calibration using an NIST-certified buffer solution that is accurate to within ±0.02 pH units at 25 °C (77 °F). If the expected pH of the liquid that is monitored lies in the acidic range (less than 7 pH), use a buffer solution with a pH value of 4.00. If the expected pH of the liquid that is monitored is neutral or lies in the basic range (equal to or greater than 7 pH), use a buffer solution with a pH value of 10.00. Place the electrode of the pH CPMS in the container of buffer solution. Record the pH measured by your CPMS. Using the certified buffer solution as the reference, the pH measured by your CPMS must be within the accuracy specified in paragraph (e)(1) of this section.


(iii) Perform any of the accuracy audit methods for pH CPMS specified in QA procedures for CPMS established in 40 CFR part 60, appendix F.


(5) If your CPMS is not equipped with a redundant pH sensor, perform at least monthly a visual inspection of all components of the CPMS for integrity, oxidation, and galvanic corrosion.


(f) For each bag leak detection system, you must meet the requirements in paragraphs (f)(1) through (11) of this section.


(1) Each triboelectric bag leak detection system must be installed, calibrated, operated, and maintained according to the “Fabric Filter Bag Leak Detection Guidance” (EPA-454/R-98-015, September 1997) (incorporated by reference, see § 63.14). Other types of bag leak detection systems must be installed, operated, calibrated, and maintained in a manner consistent with the manufacturer’s written specifications and recommendations.


(2) The bag leak detection system must be certified by the manufacturer to be capable of detecting particulate matter (PM) emissions at concentrations of 10 milligrams per actual cubic meter (0.0044 grains per actual cubic foot) or less.


(3) The bag leak detection system sensor must provide an output of relative PM loadings.


(4) The bag leak detection system must be equipped with a device to continuously record the output signal from the sensor.


(5) The bag leak detection system must be equipped with an alarm system that will be engaged automatically when an increase in relative PM emissions over a preset level is detected. The alarm must be located where it is easily recognized by plant operating personnel.


(6) For positive pressure fabric filter systems, a bag leak detector must be installed in each baghouse compartment or cell.


(7) For negative pressure or induced air fabric filters, the bag leak detector must be installed downstream of the fabric filter.


(8) Where multiple detectors are required, the system’s instrumentation and alarm may be shared among detectors.


(9) The baseline output must be established by adjusting the range and the averaging period of the device and establishing the alarm set points and the alarm delay time according to section 5.0 of the “Fabric Filter Bag Leak Detection Guidance.”


(10) Following initial adjustment of the system, the owner or operator must not adjust the sensitivity or range, averaging period, alarm set points, or alarm delay time except as detailed in the OM&M plan. In no case may the sensitivity be increased by more than 100 percent or decreased by more than 50 percent over a 365-day period unless such adjustment follows a complete fabric filter inspection that demonstrates that the fabric filter is in good operating condition. You must record each adjustment of your bag leak detection system.


(11) Record the results of each inspection, calibration, and validation check.


(g) For each lime feed rate measurement device that is used to monitor the lime feed rate of a dry injection fabric filter (DIFF) or dry lime scrubber/fabric filter (DLS/FF), or the chemical feed rate of a wet scrubber, you must meet the requirements in paragraph (a) of this section.


(h) For each affected source that is subject to the emission limit specified in item 3, 4, 7, or 8 of Table 1 to this subpart, you must satisfy the requirements of paragraphs (h)(1) through (3) of this section.


(1) Install a THC CEMS at the outlet of the control device or in the stack of the affected source.


(2) Meet the requirements of PS-8 of 40 CFR part 60, appendix B.


(3) Meet the requirements of Procedure 1 of 40 CFR part 60, appendix F.


(i) Requests for approval of alternate monitoring methods must meet the requirements in §§ 63.9800(i)(2) and 63.8(f).


[68 FR 18747, Apr. 16, 2003, as amended at 86 FR 66065, Nov. 19, 2021]


§ 63.9806 How do I demonstrate initial compliance with the emission limits, operating limits, and work practice standards?

(a) You must demonstrate initial compliance with each emission limit that applies to you according to the requirements specified in Table 5 to this subpart.


(b) You must establish each site-specific operating limit in Table 2 to this subpart that applies to you according to the requirements specified in § 63.9800 and Table 4 to this subpart.


(c) You must demonstrate initial compliance with each work practice standard that applies to you according to the requirements specified in Table 6 to this subpart.


(d) You must submit the Notification of Compliance Status containing the results of the initial compliance demonstration according to the requirements in § 63.9812(e). After Novermber 19, 2021 for affected sources that commence construction or reconstruction after January 14, 2021, and on and after May 19, 2022 for all other affected sources, you must submit the Notification of Compliance Status containing the results of the initial compliance demonstration according to the requirements in § 63.9812(e) and 63.9814(j).


[68 FR 18747, Apr. 16, 2003, as amended at 86 FR 66065, Nov. 19, 2021]


Continuous Compliance Requirements

§ 63.9808 How do I monitor and collect data to demonstrate continuous compliance?

(a) You must monitor and collect data according to this section.


(b) At all times, you must maintain your monitoring systems in accordance with § 63.9792(b), including, but not limited to, keeping the necessary parts readily available for routine repairs of the monitoring equipment.


(c) Except for, as applicable, monitoring system malfunctions, associated repairs, and required quality assurance or quality control activities, you must monitor continuously whenever your affected process unit is operating. For purposes of calculating data averages, you must not use data recorded during monitoring system malfunctions, associated repairs, and required quality assurance or quality control activities. You must use all the data collected during all other periods in assessing compliance. A monitoring system malfunction is any sudden, infrequent, not reasonably preventable failure of the monitoring system to provide valid data. Monitoring system malfunctions include out of control continuous monitoring systems (CMS), such as a CPMS. Any averaging period for which you do not have valid monitoring data as a result of a monitoring system malfunction and for which such data are required constitutes a deviation, and you must notify the Administrator in accordance with § 63.9814(e). Monitoring system failures are different from monitoring system malfunctions in that they are caused in part by poor maintenance or careless operation. Any period for which there is a monitoring system failure and data are not available for required calculations constitutes a deviation and you must notify the Administrator in accordance with § 63.9814(e).


[68 FR 18747, Apr. 16, 2003, as amended at 86 FR 66065, Nov. 19, 2021]


§ 63.9810 How do I demonstrate continuous compliance with the emission limits, operating limits, and work practice standards?

(a) You must demonstrate continuous compliance with each emission limit specified in Table 1 to this subpart that applies to you according to the requirements specified in Table 7 to this subpart.


(b) You must demonstrate continuous compliance with each operating limit specified in Table 2 to this subpart that applies to you according to the requirements specified in Table 8 to this subpart.


(c) You must demonstrate continuous compliance with each work practice standard specified in Table 3 to this subpart that applies to you according to the requirements specified in Table 9 to this subpart.


(d) For each affected source that is equipped with an add-on APCD that is not addressed in Table 2 to this subpart or that is using process changes as a means of meeting the emission limits in Table 1 to this subpart, you must demonstrate continuous compliance with each emission limit in Table 1 to this subpart and each operating limit established as required in § 63.9800(i)(3) according to the methods specified in your approved alternative monitoring methods request as described in § 63.9800(i)(2).


(e) Before May 19, 2022, you must report each instance in which you did not meet each emission limit and each operating limit in this subpart that applies to you. This includes periods of SSM. These instances are deviations from the emission limitations in this subpart. These deviations must be reported according to the requirements in § 63.9814. On or after May 19, 2022, you must report each instance in which you did not meet each emission limit and each operating limit in this subpart that applies to you. These instances are deviations from the emission limitations in this subpart. These deviations must be reported according to the requirements in § 63.9814.


(1) [Reserved]


(2) Before May 19, 2022, consistent with §§ 63.6(e) and 63.7(e)(1), deviations that occur during a period of startup, shutdown, or malfunction are not violations if you demonstrate to the Administrator’s satisfaction that you were operating in accordance with § 63.6(e)(1) and your OM&M plan. The Administrator will determine whether deviations that occur during a period of startup, shutdown, or malfunction are violations, according to the provisions in § 63.6(e). On or after May 19, 2022, consistent with §§ 63.9792(b) and 63.9800(d), deviations are not violations if you demonstrate to the Administrator’s satisfaction that you were operating in accordance with § 63.9792(b) and your OM&M plan. The Administrator will determine whether deviations are violations, according to the provisions in § 63.9792(b).


(f) You must demonstrate continuous compliance with the operating limits in Table 2 to this subpart for visible emissions (VE) from clay refractory products kilns that are uncontrolled or equipped with DLA, dry lime injection fabric filter (DIFF), dry lime scrubber/fabric filter (DLS/FF) or other dry control device as described in paragraph (f)(1) or (2) of this section.


(1) VE testing. Monitoring VE at each kiln stack according to the requirements in paragraphs (f)(1)(i) through (v) of this section.


(i) Perform daily VE observations of each kiln stack according to the procedures of EPA Method 22 of 40 CFR part 60, appendix A-7. You must conduct the EPA Method 22 test while the affected source is operating under normal conditions. The duration of each EPA Method 22 test must be at least 15 minutes.


(ii) If VE are observed during any daily test conducted using EPA Method 22 of 40 CFR part 60, appendix A-7, you must promptly conduct an opacity test, according to the procedures of EPA Method 9 of 40 CFR part 60, appendix A-4. If opacity greater than 10 percent is observed, you must initiate and complete corrective actions according to your OM&M plan.


(iii) You may decrease the frequency of EPA Method 22 testing from daily to weekly for a kiln stack if one of the conditions in paragraph (f)(1)(iii)(A) or (B) of this section is met.


(A) No VE are observed in 30 consecutive daily EPA Method 22 tests for any kiln stack; or


(B) No opacity greater than 10 percent is observed during any of the EPA Method 9 tests for any kiln stack.


(iv) If VE are observed during any weekly test and opacity greater than 10 percent is observed in the subsequent EPA Method 9 test, you must promptly initiate and complete corrective actions according to your OM&M plan, resume testing of that kiln stack following EPA Method 22 of 40 CFR part 60, appendix A-7, on a daily basis, as described in paragraph (f)(1)(i) of this section, and maintain that schedule until one of the conditions in paragraph (f)(1)(iii)(A) or (B) of this section is met, at which time you may again decrease the frequency of EPA Method 22 testing to a weekly basis.


(v) If greater than 10 percent opacity is observed during any test conducted using EPA Method 9 of 40 CFR part 60, appendix A-4, you must report these deviations by following the requirements in § 63.9814.


(2) Alternative to VE testing. In lieu of meeting the requirements under paragraph (f)(1) of this section, you may conduct a PM test at least once every year following the initial performance test, according to the procedures of EPA Method 5 of 40 CFR part 60, appendix A-3, and the provisions of § 63.9800(e) and (f).


[68 FR 18747, Apr. 16, 2003, as amended at 71 FR 20471, Apr. 20, 2006; 86 FR 66065, Nov. 19, 2021]


Notifications, Reports, and Records

§ 63.9812 What notifications must I submit and when?

(a) You must submit all of the notifications in §§ 63.7(b) and (c), 63.8(f)(4), and 63.9 (b) through (e) and (h) that apply to you by the dates specified.


(b) As specified in § 63.9(b)(2) and (3), if you start up your affected source before April 16, 2003, you must submit an Initial Notification not later than 120 calendar days after April 16, 2003, or no later than 120 days after the source becomes subject to this subpart, whichever is later.


(c) As specified in § 63.9(b)(3), if you start up your new or reconstructed affected source on or after April 16, 2003, you must submit an Initial Notification not later than 120 calendar days after you become subject to this subpart. Initial Notifications required to be submitted after November 19, 2021 for affected sources that commence construction or reconstruction after January 14, 2021, and on and after May 19, 2022 for all other affected sources submitting initial notifications required in § 63.9(b) must be submitted following the procedure specified in § 63.9814(h) through (l).


(d) If you are required to conduct a performance test, you must submit a Notification of Performance Test at least 60 calendar days before the performance test is scheduled to begin, as required in § 63.7(b)(1).


(e) If you are required to conduct a performance test, you must submit a Notification of Compliance Status as specified in § 63.9(h) and paragraphs (e)(1) and (2) of this section. After November 19, 2021 for affected sources that commence construction or reconstruction after January 14, 2021, and on and after May 19, 2022 for all other affected sources, submit all subsequent Notifications of Compliance Status following the procedure specified in § 63.9814(h) through (l).


(1) For each compliance demonstration that includes a performance test conducted according to the requirements in Table 4 to this subpart, you must submit the Notification of Compliance Status, including the summary of the performance test results, before the close of business on the 60th calendar day following the completion of the performance test.


(2) In addition to the requirements in § 63.9(h)(2)(i), you must include the information in paragraphs (e)(2)(i) through (iv) of this section in your Notification of Compliance Status.


(i) The operating limit parameter values established for each affected source with supporting documentation and a description of the procedure used to establish the values.


(ii) Design information and analysis with supporting documentation demonstrating conformance with requirements for capture/collection systems in Table 2 to this subpart.


(iii) A description of the methods used to comply with any applicable work practice standard.


(iv) For each APCD that includes a fabric filter, analysis and supporting documentation demonstrating conformance with EPA guidance and specifications for bag leak detection systems in § 63.9804(f).


(f) Before November 19, 2021, if you operate a clay refractory products kiln or a chromium refractory products kiln that is subject to the work practice standard specified in item 3 or 4 of Table 3 to this subpart, and you intend to use a fuel other than natural gas or equivalent to fire the affected kiln, you must submit a notification of alternative fuel use within 48 hours of the declaration of a period of natural gas curtailment or supply interruption, as defined in § 63.9824. The notification must include the information specified in paragraphs (f)(1) through (5) of this section. On and after November 19, 2021, you may not use a fuel other than natural gas or equivalent to fire the affected kiln.


(1) Company name and address.


(2) Identification of the affected kiln.


(3) Reason you are unable to use natural gas or equivalent fuel, including the date when the natural gas curtailment was declared or the natural gas supply interruption began.


(4) Type of alternative fuel that you intend to use.


(5) Dates when the alternative fuel use is expected to begin and end.


(g) If you own or operate an affected continuous kiln used to manufacture refractory products that use organic HAP and must perform scheduled maintenance on the THC control device for that kiln, you must request approval from the Administrator before bypassing the control device, as specified in § 63.9792(e). You must submit a separate request for approval each time you plan to bypass the kiln control device.


[68 FR 58620, Oct. 10, 2003, as amended at 85 FR 73918, Nov. 19, 2020; 86 FR 66065, Nov. 19, 2021]


§ 63.9814 What reports must I submit and when?

(a) You must submit each report in Table 10 to this subpart that applies to you.


(b) Unless the Administrator has approved a different schedule for submission of reports under § 63.10(a), you must submit each report by the date in Table 10 to this subpart and as specified in paragraphs (b)(1) through (5) of this section.


(1) The first compliance report must cover the period beginning on the compliance date that is specified for your affected source in § 63.9786 and ending on June 30 or December 31 and lasting at least 6 months but less than 12 months. For example, if your compliance date is March 1, then the first semiannual reporting period would begin on March 1 and end on December 31.


(2) The first compliance report must be postmarked or delivered no later than July 31 or January 31 for compliance periods ending on June 30 and December 31, respectively.


(3) Each subsequent compliance report must cover the semiannual reporting period from January 1 through June 30 or the semiannual reporting period from July 1 through December 31.


(4) Each subsequent compliance report must be postmarked or delivered no later than July 31 or January 31 for compliance periods ending on June 30 and December 31, respectively.


(5) For each affected source that is subject to permitting regulations pursuant to 40 CFR part 70 or 40 CFR part 71 and, if the permitting authority has established dates for submitting semiannual reports pursuant to 40 CFR 70.6(a)(3)(iii)(A) or 40 CFR 71.6(a)(3)(iii)(A), you may submit the first and subsequent compliance reports according to the dates the permitting authority has established instead of according to the dates in paragraphs (b)(1) through (4) of this section. In such cases, you must notify the Administrator of this change.


(c) The compliance report must contain the information in paragraphs (c)(1) through (7) of this section.


(1) Company name and address.


(2) Statement by a responsible official with that official’s name, title, and signature, certifying that, based on information and belief formed after reasonable inquiry, the statements and information in the report are true, accurate, and complete.


(3) Date of report and beginning and ending dates of the reporting period.


(4) Before May 19, 2022, if you had a startup, shutdown, or malfunction during the reporting period, and you took actions consistent with your SSMP and OM&M plan, the compliance report must include the information specified in § 63.10(d)(5)(i). On or after May 19, 2022, if you had a deviation from any emission limitations (emission limit, operating limit, or work practice standard) during the reporting period that apply to you, and you took actions consistent with your OM&M plan, the compliance report must include the information specified in (d) and (e) of this section.


(5) If there are no deviations from any emission limitations (emission limit, operating limit, or work practice standard) that apply to you, the compliance report must include a statement that there were no deviations from the emission limitations during the reporting period.


(6) If there were no periods during which any affected CPMS was out of control as specified in § 63.8(c)(7), the compliance report must include a statement that there were no periods during which the CPMS was out of control during the reporting period.


(7) For each period when an affected continuous kiln used to manufacture refractory products that use organic HAP was operating while the THC control device was out of service, the compliance report must include a description of the control device maintenance performed, including the information specified in paragraphs (c)(7)(i) through (vi) of this section.


(i) The date and time when the control device was shut down and restarted.


(ii) Identification of the kiln that was operating and the number of hours that the kiln operated while the control device was out of service.


(iii) A statement of whether or not the control device maintenance was included in your approved request to bypass the control device while scheduled maintenance is performed, developed as specified in § 63.9792(e).


(iv) Before May 19, 2022, a statement of whether emissions were minimized while the control device was out of service in accordance with your OM&M plan. After May 19, 2022, a statement of whether emissions were minimized while the control device was out of service in accordance with your OM&M plan and the information specified in paragraphs (c)(7)(iv)(A) through (C) of this section.


(A) The average organic HAP processing rate based on actual production on a 6-month rolling basis (not to include periods of kiln shut down) or the lowest hourly organic HAP processing rate from the most recent performance test on that kiln, whichever is lower.


(B) The actual hourly organic HAP processing rate for the kiln while the control device was out of service.


(C) The amount of product manufactured and the mass of organic HAP in the product manufactured in the kiln while the control device was out of service.


(v) After May 19, 2022, an estimate of the THC emissions from the continuous kiln stack while the control device was out of service.


(vi) After May 19, 2022, the total number of hours that the kiln has operated while the control device was out of service during the last year on a 12-month rolling basis.


(d) Before May 19, 2022, for each deviation from an emission limitation (emission limit, operating limit, or work practice standard) that occurs at an affected source where you are not using a CPMS to comply with the emission limitations in this subpart, the compliance report must contain the information in paragraphs (c)(1) through (4) and (d)(1) and (2) of this section. This includes periods of SSM. On or after May 19, 2022, for each deviation from an emission limitation (emission limit, operating limit, or work practice standard) that occurs at an affected source where you are not using a CPMS to comply with the emission limitations in this subpart, the compliance report must contain the information in paragraphs (c)(1) through (4) and (d)(1) through (3) of this section.


(1) The compliance report must include the total operating time of each affected source during the reporting period.


(2) The compliance report must include information on the number, duration in hours, and cause of deviations (including unknown cause, if applicable) and the corrective action taken.


(3) The compliance report must include the date and time of each deviation, a list of the affected sources or equipment, and an estimate of each regulated pollutant emitted over the emission limit and a description of the method used to estimate the emissions.


(e) Before May 19, 2022, for each deviation from an emission limitation (emission limit, operating limit, or work practice standard) occurring at an affected source where you are using a CPMS to comply with the emission limitation in this subpart, the compliance report must include the information in paragraphs (c)(1) through (4) and (e)(1) through (13) of this section. This includes periods of SSM. On or after May 19, 2022, for each deviation from an emission limitation (emission limit, operating limit, or work practice standard) occurring at an affected source where you are using a CPMS to comply with the emission limitation in this subpart, the compliance report must include the information in paragraphs (c)(1) through (4) and (e)(1) through (13) of this section.


(1) The total operating time of each affected source during the reporting period.


(2) Before May 19, 2022, the date and time that each startup, shutdown, or malfunction started and stopped. On or after May 19, 2022, the date and time that each startup, shutdown, or malfunction started and stopped is not required.


(3) The date, time, and duration in hours that each CPMS was inoperative.


(4) The date, time and duration in hours that each CPMS was out of control, including the information in § 63.8(c)(8), as required by your OM&M plan.


(5) Before May 19, 2022, the date and time that each deviation from an emission limitation (emission limit, operating limit, or work practice standard) started and stopped, and whether each deviation occurred during a period of startup, shutdown, or malfunction. On or after May 19, 2022, for each deviation from an emission limitation (emission limit, operating limit, or work practice standard), the date and time that each deviation started and stopped, the duration in hours, a list of the affected sources or equipment, an estimate of each regulated pollutant emitted over the emission limit, and a description of the method used to estimate the emissions.


(6) A description of corrective action taken in response to a deviation.


(7) The total number of deviations during the reporting period, a summary of the total duration in hours of the deviations during the reporting period, and the total duration as a percentage of the total source operating time during that reporting period.


(8) Before May 19, 2022, a breakdown of the total duration of the deviations during the reporting period into those that are due to startup, shutdown, control equipment problems, process problems, other known causes, and other unknown causes. On or after May 19, 2022, a breakdown of the total duration of the deviations during the reporting period into those that are due to control equipment problems, process problems, other known causes, and other unknown causes.


(9) A summary of the total duration in hours of CPMS downtime during the reporting period and the total duration of CPMS downtime as a percentage of the total source operating time during that reporting period.


(10) A brief description of the process units.


(11) A brief description of the CPMS.


(12) The date of the latest CPMS initial validation or accuracy audit.


(13) A description of any changes in CPMS, processes, or controls since the last reporting period.


(f) If you have obtained a title V operating permit pursuant to 40 CFR part 70 or 40 CFR part 71, you must report all deviations as defined in this subpart in the semiannual monitoring report required by 40 CFR 70.6(a)(3)(iii)(A) or 40 CFR 71.6(a)(3)(iii)(A). If you submit a compliance report according to Table 10 to this subpart along with, or as part of, the semiannual monitoring report required by 40 CFR 70.6(a)(3)(iii)(A) or 40 CFR 71.6(a)(3)(iii)(A), and the compliance report includes all required information concerning deviations from any emission limitation (including any operating limit), then submitting the compliance report will satisfy any obligation to report the same deviations in the semiannual monitoring report. However, submitting a compliance report will not otherwise affect any obligation you may have to report deviations from permit requirements to the permit authority.


(g) Before November 19, 2021, if you operate a clay refractory products kiln or a chromium refractory products kiln that is subject to the work practice standard specified in item 3 or 4 of Table 3 to this subpart, and you use a fuel other than natural gas or equivalent to fire the affected kiln, you must submit a report of alternative fuel use within 10 working days after terminating the use of the alternative fuel. The report must include the information in paragraphs (g)(1) through (6) of this section. On and after November 19, 2021, you may not use a fuel other than natural gas or equivalent to fire the affected kiln.


(1) Company name and address.


(2) Identification of the affected kiln.


(3) Reason for using the alternative fuel.


(4) Type of alternative fuel used to fire the affected kiln.


(5) Dates that the use of the alternative fuel started and ended.


(6) Amount of alternative fuel used.


(h) Beginning on May 19, 2022, within 60 days after the date of completing each performance test required by this subpart, you must submit the results of the performance test following the procedures specified in paragraphs (h)(1) through (3) of this section.


(1) Data collected using test methods supported by the EPA’s Electronic Reporting Tool (ERT) as listed on the EPA’s ERT website (https://www.epa.gov/electronic-reporting-air-emissions/electronic-reporting-tool-ert) at the time of the test. Submit the results of the performance test to the EPA via the Compliance and Emissions Data Reporting Interface (CEDRI), which can be accessed through the EPA’s CDX (https://cdx.epa.gov/). The data must be submitted in a file format generated using the EPA’s ERT. Alternatively, you may submit an electronic file consistent with the extensible markup language (XML) schema listed on the EPA’s ERT website.


(2) Data collected using test methods that are not supported by the EPA’s ERT as listed on the EPA’s ERT website at the time of the test. The results of the performance test must be included as an attachment in the ERT or an alternate electronic file consistent with the XML schema listed on the EPA’s ERT website. Submit the ERT generated package or alternative file to the EPA via CEDRI.


(3) Confidential business information (CBI). Do not use CEDRI to submit information you claim as CBI. Anything submitted using CEDRI cannot later be claimed CBI. Although we do not expect persons to assert a claim of CBI, if you wish to assert a CBI claim for some of the information submitted under paragraph (h)(1) or (2) of this section, you must submit a complete file, including information claimed to be CBI, to the EPA. The file must be generated using the EPA’s ERT or an alternate electronic file consistent with the XML schema listed on the EPA’s ERT website. Submit the file on a compact disc, flash drive, or other commonly used electronic storage medium and clearly mark the medium as CBI. Mail the electronic medium to U.S. EPA/OAPQS/CORE CBI Office, Attention: Group Leader, Measurement Policy Group, MD C404-02, 4930 Old Page Rd., Durham, NC 27703. The same file with the CBI omitted must be submitted to the EPA via the EPA’s CDX as described in paragraphs (h)(1) and (2) of this section. All CBI claims must be asserted at the time of submission. Furthermore, under CAA section 114(c), emissions data is not entitled to confidential treatment, and the EPA is required to make emissions data available to the public. Thus, emissions data will not be protected as CBI and will be made publicly available.


(i) Beginning on May 19, 2022, within 60 days after the date of completing each continuous emissions monitoring system (CEMS) performance evaluation (as defined in § 63.2), you must submit the results of the performance evaluation following the procedures specified in paragraphs (i)(1) through (3) of this section.


(1) Performance evaluations of CEMS measuring relative accuracy test audit (RATA) pollutants that are supported by the EPA’s ERT as listed on the EPA’s ERT website at the time of the evaluation. Submit the results of the performance evaluation to the EPA via CEDRI, which can be accessed through the EPA’s CDX. The data must be submitted in a file format generated using the EPA’s ERT. Alternatively, you may submit an electronic file consistent with the XML schema listed on the EPA’s ERT website.


(2) Performance evaluations of CEMS measuring RATA pollutants that are not supported by the EPA’s ERT as listed on the EPA’s ERT website at the time of the evaluation. The results of the performance evaluation must be included as an attachment in the ERT or an alternate electronic file consistent with the XML schema listed on the EPA’s ERT website. Submit the ERT generated package or alternative file to the EPA via CEDRI.


(3) CBI. Do not use CEDRI to submit information you claim as CBI. Anything submitted using CEDRI cannot later be claimed CBI. Although we do not expect persons to assert a claim of CBI, if you wish to assert a CBI claim for some of the information submitted under paragraph (i)(1) or (2) of this section, you must submit a complete file, including information claimed to be CBI, to the EPA. The file must be generated using the EPA’s ERT or an alternate electronic file consistent with the XML schema listed on the EPA’s ERT website. Submit the file on a compact disc, flash drive, or other commonly used electronic storage medium and clearly mark the medium as CBI. Mail the electronic medium to U.S. EPA/OAQPS/CORE CBI Office, Attention: Group Leader, Measurement Policy Group, MD C404-02, 4930 Old Page Rd., Durham, NC 27703. The same file with the CBI omitted must be submitted to the EPA via the EPA’s CDX as described in paragraphs (h)(1) and (2) of this section. All CBI claims must be asserted at the time of submission. Furthermore, under CAA section 114(c), emissions data is not entitled to confidential treatment, and the EPA is required to make emissions data available to the public. Thus, emissions data will not be protected as CBI and will be made publicly available.


(j) Beginning May 19, 2022, you must submit all subsequent Notification of Compliance Status reports in PDF format to the EPA via CEDRI, which can be accessed through EPA’s CDX (https://cdx.epa.gov/).The EPA will make all the information submitted through CEDRI available to the public without further notice to you. Do not use CEDRI to submit information you claim as CBI. Anything submitted using CEDRI cannot later be claimed CBI. Although we do not expect persons to assert a claim of CBI, if you wish to assert a CBI claim, submit a complete report, including information claimed to be CBI, to the EPA. Submit the file on a compact disc, flash drive, or other commonly used electronic storage medium and clearly mark the medium as CBI. Mail the electronic medium to U.S. EPA/OAQPS/CORE CBI Office, Attention: Refractory Lead MD C404-02, 4930 Old Page Rd., Durham, NC 27703. The same file with the CBI omitted must be submitted to the EPA via the EPA’s CDX as described earlier in this paragraph (j). All CBI claims must be asserted at the time of submission. Furthermore, under CAA section 114(c), emissions data is not entitled to confidential treatment, and the EPA is required to make emissions data available to the public. Thus, emissions data will not be protected as CBI and will be made publicly available.


(k) If you are required to electronically submit a report through CEDRI in the EPA’s CDX, you may assert a claim of EPA system outage for failure to timely comply with that reporting requirement. To assert a claim of EPA system outage, you must meet the requirements outlined in paragraphs (k)(1) through (7) of this section.


(1) You must have been or will be precluded from accessing CEDRI and submitting a required report within the time prescribed due to an outage of either the EPA’s CEDRI or CDX systems.


(2) The outage must have occurred within the period of time beginning five business days prior to the date that the submission is due.


(3) The outage may be planned or unplanned.


(4) You must submit notification to the Administrator in writing as soon as possible following the date you first knew, or through due diligence should have known, that the event may cause or has caused a delay in reporting.


(5) You must provide to the Administrator a written description identifying:


(i) The date(s) and time(s) when CDX or CEDRI was accessed and the system was unavailable;


(ii) A rationale for attributing the delay in reporting beyond the regulatory deadline to EPA system outage;


(iii) A description of measures taken or to be taken to minimize the delay in reporting; and


(iv) The date by which you propose to report, or if you have already met the reporting requirement at the time of the notification, the date you reported.


(6) The decision to accept the claim of EPA system outage and allow an extension to the reporting deadline is solely within the discretion of the Administrator.


(7) In any circumstance, the report must be submitted electronically as soon as possible after the outage is resolved.


(l) If you are required to electronically submit a report through CEDRI in the EPA’s CDX, you may assert a claim of force majeure for failure to timely comply with that reporting requirement. To assert a claim of force majeure, you must meet the requirements outlined in paragraphs (l)(1) through (5) of this section.


(1) You may submit a claim if a force majeure event is about to occur, occurs, or has occurred or there are lingering effects from such an event within the period of time beginning five business days prior to the date the submission is due. For the purposes of this section, a force majeure event is defined as an event that will be or has been caused by circumstances beyond the control of the affected facility, its contractors, or any entity controlled by the affected facility that prevents you from complying with the requirement to submit a report electronically within the time period prescribed. Examples of such events are acts of nature (e.g., hurricanes, earthquakes, or floods), acts of war or terrorism, or equipment failure or safety hazard beyond the control of the affected facility (e.g., large scale power outage).


(2) You must submit notification to the Administrator in writing as soon as possible following the date you first knew, or through due diligence should have known, that the event may cause or has caused a delay in reporting.


(3) You must provide to the Administrator:


(i) A written description of the force majeure event;


(ii) A rationale for attributing the delay in reporting beyond the regulatory deadline to the force majeure event;


(iii) A description of measures taken or to be taken to minimize the delay in reporting; and


(iv) The date by which you propose to report, or if you have already met the reporting requirement at the time of the notification, the date you reported.


(4) The decision to accept the claim of force majeure and allow an extension to the reporting deadline is solely within the discretion of the Administrator.


(5) In any circumstance, the reporting must occur as soon as possible after the force majeure event occurs.


[68 FR 18747, Apr. 16, 2003, as amended at 86 FR 66066, Nov. 19,2021]


§ 63.9816 What records must I keep?

(a) You must keep the records listed in paragraphs (a)(1) through (3) of this section.


(1) A copy of each notification and report that you submitted to comply with this subpart, including all documentation supporting any Initial Notification or Notification of Compliance Status that you submitted, according to the requirements in § 63.10(b)(2)(xiv).


(2) Before May 19, 2022, the records in § 63.6(e)(3)(iii) through (v) related SSM.


(3) Records of performance tests as required in § 63.10(b)(2)(viii).


(b) You must keep the records required in Tables 7 through 9 to this subpart to show continuous compliance with each emission limitation that applies to you.


(c) You must also maintain the records listed in paragraphs (c)(1) through (10) of this section.


(1) Records of emission data used to develop an emissions profile, as indicated in items 8(a)(i)(4) and 17(b)(i)(4) of Table 4 to this subpart.


(2) Records that document how you comply with any applicable work practice standard.


(3) For each bag leak detection system, records of each alarm, the time of the alarm, the time corrective action was initiated and completed, and a brief description of the cause of the alarm and the corrective action taken.


(4) For each kiln controlled with a DLA, records that document the source of limestone used.


(5) For each deviation of an operating limit parameter value, record the information in paragraphs (c)(5)(i) through (iv) of this section.


(i) The date, time, and duration in hours of the deviation.


(ii) On or after May 19, 2022, a list of the affected sources or equipment.


(iii) On or after May 19, 2022, an estimate of the quantity in pounds of each regulated pollutant over any emission limit and a description of the method used to estimate emissions.


(iv) Actions taken to minimize emissions in accordance with § 63.9792(b), a brief explanation of the cause of the deviation, and the corrective action taken to return the affected unit to its normal or usual manner of operation.


(6) For each affected source, records of production rate on a process throughput basis (either feed rate to the process unit or discharge rate from the process unit).


(7) Records of any approved alternative monitoring method(s) or test procedure(s).


(8) Records of maintenance activities and inspections performed on control devices, including all records associated with the scheduled maintenance of the THC control devices on continuous kilns used to manufacture refractory products that use organic HAP, as specified in § 63.9792(e).


(9) If you operate a source that is subject to the THC emission limits specified in item 2, 3, 6, or 7 of Table 1 to this subpart and is controlled with a catalytic oxidizer, records of annual checks of catalyst activity levels and subsequent corrective actions.


(10) Current copies of the OM&M plan, including any revisions and records documenting conformance with those revisions.


[68 FR 18747, Apr. 16, 2003, as amended at 86 FR 66069, Nov. 19, 2021]


§ 63.9818 In what form and how long must I keep my records?

(a) Your records must be in a form suitable and readily available for expeditious review, according to § 63.10(b)(1).


(b) As specified in § 63.10(b)(1), you must keep each record for 5 years following the date of each occurrence, measurement, maintenance, corrective action, report, or record.


(c) You must keep each record onsite for at least 2 years after the date of each occurrence, measurement, maintenance, corrective action, report, or record, according to § 63.10(b)(1). You may keep the records offsite for the remaining 3 years.


Other Requirements and Information

§ 63.9820 What parts of the General Provisions apply to me?

Table 11 to this subpart shows which parts of the General Provisions specified in §§ 63.1 through 63.16 apply to you.


[86 FR 66069, Nov. 19, 2021]


§ 63.9822 Who implements and enforces this subpart?

(a) This subpart can be implemented and enforced by us, the U.S. Environmental Protection Agency (U.S. EPA), or a delegated authority such as your State, local, or tribal agency. If the U.S. EPA Administrator has delegated authority to your State, local, or tribal agency, then that agency, in addition to the U.S. EPA, has the authority to implement and enforce this subpart. You should contact your U.S. EPA Regional Office to find out if implementation and enforcement to this subpart is delegated to your State, local, or tribal agency.


(b) In delegating implementation and enforcement authority to this subpart to a State, local, or tribal agency under 40 CFR part 63, subpart E, the authorities contained in paragraph (c) of this section are retained by the Administrator of the U.S. EPA and are not transferred to the State, local, or tribal agency.


(c) The authorities that cannot be delegated to state, local, or tribal agencies are as specified in paragraphs (c)(1) through (5) of this section.


(1) Approval of alternatives to the applicability requirements in §§ 63.9782 and 63.9784, the compliance date requirements in § 63.9786, and the emission limitations in § 63.9788.


(2) Approval of major changes to test methods under § 63.7(e)(2)(ii) and (f) and as defined in § 63.90.


(3) Approval of major changes to monitoring under § 63.8(f) and as defined in § 63.90.


(4) Approval of major changes to recordkeeping and reporting under § 63.10(f) and as defined in § 63.90.


(5) Approval of an alternative to any electronic reporting to the EPA required by this subpart.


[68 FR 18747, Apr. 16, 2003, as amended at 86 FR 66069, Nov. 19, 2021]


§ 63.9824 What definitions apply to this subpart?

Terms used in this subpart are defined in the Clean Air Act, in 40 CFR 63.2, the General Provisions of this part, and in this section as follows:


Additive means a minor addition of a chemical, mineral, or metallic substance that is added to a refractory mixture to facilitate processing or impart specific properties to the final refractory product.


Add-on air pollution control device (APCD) means equipment installed on a process vent that reduces the quantity of a pollutant that is emitted to the air.


Autoclave means a vessel that is used to impregnate fired and/or unfired refractory shapes with pitch to form pitch-impregnated refractory products. Autoclaves also can be used as defumers following the impregnation process.


Bag leak detection system means an instrument that is capable of monitoring particulate matter loadings in the exhaust of a fabric filter in order to detect bag failures. A bag leak detection system includes, but is not limited to, an instrument that operates on triboelectric, light-scattering, light-transmittance, or other effects to monitor relative PM loadings.


Basket means the metal container used to hold refractory shapes for pitch impregnation during the shape preheating, impregnation, defuming, and, if applicable, coking processes.


Batch process means a process in which a set of refractory shapes is acted upon as a single unit according to a predetermined schedule, during which none of the refractory shapes being processed are added or removed. A batch process does not operate continuously.


Binder means a substance added to a granular material to give it workability and green or dry strength.


Catalytic oxidizer means an add-on air pollution control device that is designed specifically to destroy organic compounds in a process exhaust gas stream by catalytic incineration. A catalytic oxidizer includes a bed of catalyst media through which the process exhaust stream passes to promote combustion and incineration at a lower temperature than would be possible without the catalyst.


Chromium refractory product means a refractory product that contains at least 1 percent chromium by weight.


Clay refractory product means a refractory product that contains at least 10 percent uncalcined clay by weight prior to firing in a kiln. In this definition, the term “clay” means any of the following six classifications of clay defined by the U.S. Geologic Survey: ball clay, bentonite, common clay and shale, fire clay, fuller’s earth, and kaolin.


Coking oven means a thermal process unit that operates at a peak temperature typically between 540° and 870 °C (1000° and 1600 °F) and is used to drive off the volatile constituents of pitch-impregnated refractory shapes under a reducing or oxygen-deprived atmosphere.


Continuous parameter monitoring system (CPMS) means the total equipment that is used to measure and record temperature, pressure, liquid flow rate, gas flow rate, or pH on a continuous basis in one or more locations. “Total equipment” includes the sensor, mechanical components, electronic components, data acquisition system, data recording system, electrical wiring, and other components of a CPMS.


Continuous process means a process that operates continuously. In a continuous process unit, the materials or shapes that are processed are either continuously charged (fed) to and discharged from the process unit, or are charged and discharged at regular time intervals without the process unit being shut down. Continuous thermal process units, such as tunnel kilns, generally include temperature zones that are maintained at relatively constant temperature and through which the materials or shapes being processed are conveyed continuously or at regular time intervals.


Curing oven means a thermal process unit that operates at a peak temperature typically between 90° and 340 °C (200° and 650 °F) and is used to activate a thermosetting resin, pitch, or other binder in refractory shapes. Curing ovens also perform the same function as shape dryers in removing the free moisture from refractory shapes.


Defumer means a process unit that is used for holding pitch-impregnated refractory shapes as the shapes defume or cool immediately following the impregnation process. This definition includes autoclaves that are opened and exhausted to the atmosphere following an impregnation cycle and used for holding pitch-impregnated refractory shapes while the shapes defume or cool.


Deviation means any instance in which an affected source subject to this subpart, or an owner or operator of such a source:


(1) Fails to meet any requirement or obligation established by this subpart including, but not limited to, any emission limitation (emission limit, operating limit, or work practice standard);


(2) Fails to meet any term or condition that is adopted to implement an applicable requirement in this subpart for any affected source required to obtain such a permit; or


(3) Fails to meet any emission limitation (emission limit, operating limit, or work practice standard) in this subpart during startup, shutdown, or malfunction, regardless of whether or not such failure is permitted by this subpart.


Dry injection fabric filter (DIFF) means an add-on air pollution control device that includes continuous injection of hydrated lime or other sorbent into a duct or reaction chamber followed by a fabric filter.


Dry lime scrubber/fabric filter (DLS/FF) means an add-on air pollution control device that includes continuous injection of humidified hydrated lime or other sorbent into a reaction chamber followed by a fabric filter. These systems may include recirculation of some of the sorbent.


Dry limestone adsorber (DLA) means an air pollution control device that includes a limestone storage bin, a reaction chamber that is essentially a packed-tower filled with limestone, and may or may not include a peeling drum that mechanically scrapes reacted limestone to regenerate the stone for reuse.


Emission limitation means any restriction on the emissions a process unit may discharge.


Fabric filter means an add-on air pollution control device used to capture particulate matter by filtering a process exhaust stream through a filter or filter media; a fabric filter is also known as a baghouse.


Fired refractory shape means a refractory shape that has been fired in a kiln.


HAP means any hazardous air pollutant that appears in section 112(b) of the Clean Air Act.


Kiln means a thermal process unit that operates at a peak temperature greater than 820 °C (1500 °F) and is used for firing or sintering refractory, ceramic, or other shapes.


Kiln furniture means any refractory shape that is used to hold, support, or position ceramic or refractory products in a kiln during the firing process.


Maximum organic HAP processing rate means the combination of process and refractory product formulation that has the greatest potential to emit organic HAP. The maximum organic HAP processing rate is a function of the organic HAP processing rate, process operating temperature, and other process operating parameters that affect emissions of organic HAP. (See also the definition of organic HAP processing rate.)


Organic HAP processing rate means the rate at which the mass of organic HAP materials contained in refractory shapes are processed in an affected thermal process unit. The organic HAP processing rate is a function of the amount of organic HAP contained in the resins, binders, and additives used in a refractory mix; the amounts of those resins, binders, and additives in the refractory mix; and the rate at which the refractory shapes formed from the refractory mix are processed in an affected thermal process unit. For continuous process units, the organic HAP processing rate is expressed in units of mass of organic HAP per unit of time (e.g., pounds per hour). For batch process units, the organic HAP processing rate is expressed in units of mass of organic HAP per unit mass of refractory shapes processed during the batch process cycle (e.g., pounds per ton).


Particulate matter (PM) means, for the purposes of this subpart, emissions of particulate matter that serve as a measure of total particulate emissions as measured by EPA Method 5 of 40 CFR part 60, appendix A-3.


Peak emissions period means the period of consecutive hourly mass emissions of the applicable pollutant that is greater than any other period of consecutive hourly mass emissions for the same pollutant over the course of a specified batch process cycle, as defined in paragraphs (1) and (2) of this definition. The peak emissions period is a function of the rate at which the temperature of the refractory shapes is increased, the mass and loading configuration of the shapes in the process unit, the constituents of the refractory mix, and the type of pollutants emitted.


(1) The 3-hour peak THC emissions period is the period of 3 consecutive hours over which the sum of the hourly THC mass emissions rates is greater than the sum of the hourly THC mass emissions rates for any other period of 3 consecutive hours during the same batch process cycle.


(2) The 3-hour peak HF emissions period is the period of 3 consecutive hours over which the sum of the hourly HF mass emissions rates is greater than the sum of the hourly HF mass emissions rates for any other period of 3 consecutive hours during the same batch process cycle.


Period of natural gas curtailment or supply interruption means a period of time during which the supply of natural gas to an affected facility is halted for reasons beyond the control of the facility. An increase in the cost or unit price of natural gas does not constitute a period of natural gas curtailment or supply interruption.


Pitch means the residue from the distillation of petroleum or coal tar.


Pitch-bonded refractory product means a formed refractory product that is manufactured using pitch as a bonding agent. Pitch-bonded refractory products are manufactured by mixing pitch with magnesium oxide, graphite, alumina, silicon carbide, silica, or other refractory raw materials, and forming the mix into shapes. After forming, pitch-bonded refractory products are cured in a curing oven and may be subsequently fired in a kiln.


Pitch-impregnated refractory product means a refractory shape that has been fired in a kiln, then impregnated with heated coal tar or petroleum pitch under pressure. After impregnation, pitch-impregnated refractory shapes may undergo the coking process in a coking oven. The total carbon content of a pitch-impregnated refractory product is less than 50 percent.


Pitch working tank means a tank that is used for heating pitch to the impregnation temperature, typically between 150° and 260 °C (300° and 500 °F); temporarily storing heated pitch between impregnation cycles; and transferring pitch to and from the autoclave during the impregnation step in manufacturing pitch-impregnated refractory products.


Plant site means all contiguous or adjoining property that is under common control, including properties that are separated only by a road or other public right-of-way. Common control includes properties that are owned, leased, or operated by the same entity, parent entity, subsidiary, or any combination thereof.


Redundant sensor means a second sensor or a back-up sensor that is integrated into a CPMS and is used to check the parameter value (e.g., temperature, pressure) measured by the primary sensor of the CPMS.


Refractory product means nonmetallic materials containing less than 50 percent carbon by weight and having those chemical and physical properties that make them applicable for structures, or as components of systems, that are exposed to environments above 538 °C (1000 °F). This definition includes, but is not limited to: refractory bricks, kiln furniture, crucibles, refractory ceramic fiber, and other materials used as linings for boilers, kilns, and other processing units and equipment where extremes of temperature, corrosion, and abrasion would destroy other materials.


Refractory products that use organic HAP means resin-bonded refractory products, pitch-bonded refractory products, and other refractory products that are produced using a substance that is an organic HAP, that releases an organic HAP during production of the refractory product, or that contains an organic HAP, such as methanol or ethylene glycol.


Refractory shape means any refractory piece forming a stable mass with specific dimensions.


Research and development process unit means any process unit whose purpose is to conduct research and development for new processes and products and is not engaged in the manufacture of products for commercial sale, except in a de minimis manner.


Resin-bonded refractory product means a formed refractory product that is manufactured using a phenolic resin or other type of thermosetting resin as a bonding agent. Resin-bonded refractory products are manufactured by mixing resin with alumina, magnesium oxide, graphite, silica, zirconia, or other refractory raw materials, and forming the mix into shapes. After forming, resin-bonded refractory products are cured in a curing oven and may be subsequently fired in a kiln.


Responsible official means one of the following:


(1) For a corporation: a president, secretary, treasurer, or vice-president of the corporation in charge of a principal business function, or any other person who performs similar policy or decisionmaking functions for the corporation, or a duly authorized representative of such person if the representative is responsible for the overall operation of one or more manufacturing, production, or operating facilities applying for or subject to a permit and either:


(i) The facilities employ more than 250 persons or have gross annual sales or expenditures exceeding $25 million (in second quarter 1980 dollars); or


(ii) The delegation of authority to such representatives is approved in advance by the Administrator;


(2) For a partnership or sole proprietorship: a general partner or the proprietor, respectively;


(3) For a municipality, State, Federal, or other public agency: either a principal executive officer or ranking elected official. For the purposes of this part, a principal executive officer of a Federal agency includes the chief executive officer having responsibility for the overall operations of a principal geographic unit of the agency (e.g., a Regional Administrator of EPA); or


(4) For affected sources (as defined in this subpart) applying for or subject to a title V permit: “responsible official” shall have the same meaning as defined in part 70 or Federal title V regulations in this chapter (42 U.S.C. 7661), whichever is applicable.


Shape dryer means a thermal process unit that operates at a peak temperature typically between 40° and 700 °C (100° and 1300 °F) and is used exclusively to reduce the free moisture content of a refractory shape. Shape dryers generally are the initial thermal process step following the forming step in refractory products manufacturing. (See also the definition of a curing oven.)


Shape preheater means a thermal process unit that operates at a peak temperature typically between 180° and 320 °C (350° and 600 °F) and is used to heat fired refractory shapes prior to the impregnation step in manufacturing pitch-impregnated refractory products.


Thermal oxidizer means an add-on air pollution control device that includes one or more combustion chambers and is designed specifically to destroy organic compounds in a process exhaust gas stream by incineration.


Uncalcined clay means clay that has not undergone thermal processing in a calciner.


Wet scrubber means an add-on air pollution control device that removes pollutants from a gas stream by bringing them into contact with a liquid, typically water.


Work practice standard means any design, equipment, work practice, or operational standard, or combination thereof, that is promulgated pursuant to section 112(h) of the Clean Air Act.


[68 FR 18747, Apr. 16, 2003, as amended at 86 FR 66069, Nov. 19, 2021]


Table 1 to Subpart SSSSS of Part 63—Emission Limits

As stated in § 63.9788, you must comply with the emission limits for affected sources in the following table:


For . . .
You must meet the following emission limits . . .
1. Each new or existing curing oven, shape dryer, and kiln that is used to process refractory products that use organic HAP; each new or existing coking oven and defumer that is used to produce pitch-impregnated refractory products; each new shape preheater that is used to produce pitch-impregnated refractory products; AND each new or existing process unit that is exhausted to a thermal or catalytic oxidizer that also controls emissions from an affected shape preheater or pitch working tankAs specified in items 2 through 9 of this table.
2. Continuous process units that are controlled with a thermal or catalytic oxidizera. The 3-hour block average THC concentration must not exceed 20 parts per million by volume, dry basis (ppmvd), corrected to 18 percent oxygen, at the outlet of the control device; or

b. The 3-hour block average THC mass emissions rate must be reduced by at least 95 percent.
3. Continuous process units that are equipped with a control device other than a thermal or catalytic oxidizera. The 3-hour block average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygen, at the outlet of the control device; or

b. The 3-hour block average THC mass emissions rate must be reduced by at least 95 percent.
4. Continuous process units that use process changes to reduce organic HAP emissionsThe 3-hour block average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygen, at the outlet of the process gas stream.
5. Continuous kilns that are not equipped with a control deviceThe 3-hour block average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygen, at the outlet of the process gas stream.
6. Batch process units that are controlled with a thermal or catalytic oxidizera. The 2-run block average THC concentration for the 3-hour peak emissions period must not exceed 20 ppmvd, corrected to 18 percent oxygen, at the outlet of the control device; or

b. The 2-run block average THC mass emissions rate for the 3-hour peak emissions period must be reduced by at least 95 percent.
7. Batch process units that are equipped with a control device other than a thermal or catalytic oxidizera. The 2-run block average THC concentration for the 3-hour peak emissions period must not exceed 20 ppmvd, corrected to 18 percent oxygen, at the outlet of the control device; or

b. The 2-run block average THC mass emissions rate for the 3-hour peak emissions period must be reduced by at least 95 percent.
8. Batch process units that use process changes to reduce organic HAP emissionsThe 2-run block average THC concentration for the 3-hour peak emissions period must not exceed 20 ppmvd, corrected to 18 percent oxygen, at the outlet of the process gas stream.
9. Batch process kilns that are not equipped with a control deviceThe 2-run block average THC concentration for the 3-hour peak emissions period must not exceed 20 ppmvd, corrected to 18 percent oxygen, at the outlet of the process gas stream.
10. Each new continuous kiln that is used to produce clay refractory productsa. The 3-hour block average HF emissions must not exceed 0.019 kilograms per megagram (kg/Mg) (0.038 pounds per ton (lb/ton)) of uncalcined clay processed, OR the 3-hour block average HF mass emissions rate must be reduced by at least 90 percent; and
b. The 3-hour block average HCl emissions must not exceed 0.091 kg/Mg (0.18 lb/ton) of uncalcined clay processed, OR the 3-hour block average HCl mass emissions rate must be reduced by at least 30 percent; and
c. The 3-hour block average PM emissions must not exceed 1.4 kg/Mg (3.1 lb/hr); and
d. The 3-hour block average Hg concentration must not exceed 6.1 micrograms per dry standard cubic meter (µg/dscm), corrected to 18 percent oxygen, at the outlet of the control device or the process gas stream.
11. Each new batch process kiln that is used to produce clay refractory productsa. The 2-run block average HF mass emissions rate for the 3-hour peak emissions period must be reduced by at least 90 percent; and

b. The 2-run block average HCl mass emissions rate for the 3-hour peak emissions period must be reduced by at least 30 percent; and
c. The 2-run block average PM emissions for the 3-hour peak emissions period must not exceed 1.4 kg/Mg (3.1 lb/hr); and
d. The 2-run block average Hg concentration for the 3-hour peak emissions period must not exceed 6.1 µg/dscm, corrected to 18 percent oxygen, at the outlet of the control device or the process gas stream.
12. Each existing continuous kiln that is used to produce clay refractory products on and after November 20, 2022a. The 3-hour block average PM emissions must not exceed 4.3 kg/Mg (9.5 lb/hr); and

b. The 3-hour block average Hg concentration must not exceed 18 µg/dscm, corrected to 18 percent oxygen, at the outlet of the control device or the process gas stream.
13. Each existing batch kiln that is used to produce clay refractory products on and after November 20, 2022a. The 2-run block average PM emissions for the 3-hour peak emissions period must not exceed 4.3 kg/Mg (9.5 lb/hr); and

b. The 2-run block average Hg concentration for the 3-hour peak emissions period must not exceed 18 µg/dscm, corrected to 18 percent oxygen, at the outlet of the control device or the process gas stream.

[86 FR 66069, Nov. 19, 2021]


Table 2 to Subpart SSSSS of Part 63—Operating Limits

As stated in § 63.9788, you must comply with the operating limits for affected sources in the following table:


For . . .
You must . . .
1. Each affected source listed in Table 1 to this subparta. Operate all affected sources according to the requirements to this subpart on and after the date on which the initial performance test is conducted or required to be conducted, whichever date is earlier; and
b. Capture emissions and vent them through a closed system; and
c. Operate each control device that is required to comply with this subpart on each affected source during all periods that the source is operating, except where specified in § 63.9792(e), item 2 of this table, item 5 of Table 3 to this subpart, item 13 of Table 4 to this subpart, and item 6 of Table 9 to this subpart for THC control devices on continuous kilns used to manufacture refractory products that use organic HAP; and
d. Record all operating parameters specified in Table 8 to this subpart for the affected source; and
e. Prepare and implement a written OM&M plan as specified in § 63.9792(d).
2. Each affected continuous kiln used to manufacture refractory products that use organic HAP that is equipped with an emission control device for THCa. Receive approval from the Administrator before taking the control device on the affected kiln out of service for scheduled maintenance, as specified in § 63.9792(e); and

b. Before May 19, 2022, minimize HAP emissions from the affected kiln during all periods of scheduled maintenance of the kiln control device when the kiln is operating and the control device is out of service; on and after May 19, 2022, you must minimize HAP emissions during the period when the kiln is operating and the control device is out of service by complying with the applicable standard in Table 3 to this subpart; and
c. Minimize the duration of all periods of scheduled maintenance of the kiln control device when the kiln is operating and the control device is out of service. On and after May 19, 2022, the total time during which the kiln is operating and the control device is out of service for the each year on a 12-month rolling basis must not exceed 750 hours.
3. Each new or existing curing oven, shape dryer, and kiln that is used to process refractory products that use organic HAP; each new or existing coking oven and defumer that is used to produce pitch-impregnated refractory products; each new shape preheater that is used to produce pitch-impregnated refractory products; AND each new or existing process unit that is exhausted to a thermal or catalytic oxidizer that also controls emissions from an affected shape preheater or pitch working tankSatisfy the applicable operating limits specified in items 4 through 9 of this table.
4. Each affected continuous process unitMaintain the 3-hour block average organic HAP processing rate (pounds per hour) at or below the maximum organic HAP processing rate established during the most recent performance test.
5. Continuous process units that are equipped with a thermal oxidizerMaintain the 3-hour block average operating temperature in the thermal oxidizer combustion chamber at or above the minimum allowable operating temperature for the oxidizer established during the most recent performance test.
6. Continuous process units that are equipped with a catalytic oxidizera. Maintain the 3-hour block average operating temperature at the inlet of the catalyst bed of the oxidizer at or above the minimum allowable operating temperature for the oxidizer established during the most recent performance test; and
b. Check the activity level of the catalyst at least every 12 months.
7. Each affected batch process unitFor each batch cycle, maintain the organic HAP processing rate (pounds per batch) at or below the maximum organic HAP processing rate established during the most recent performance test.
8. Batch process units that are equipped with a thermal oxidizera. From the start of each batch cycle until 3 hours have passed since the process unit reached maximum temperature, maintain the hourly average operating temperature in the thermal oxidizer combustion chamber at or above the minimum allowable operating temperature established for the corresponding period during the most recent performance test, as determined according to item 11 of Table 4 to this subpart; and
b. For each subsequent hour of the batch cycle, maintain the hourly average operating temperature in the thermal oxidizer combustion chamber at or above the minimum allowable operating temperature established for the corresponding hour during the most recent performance test, as specified in item 13 of Table 4 to this subpart.
9. Batch process units that are equipped with a catalytic oxidizera. From the start of each batch cycle until 3 hours have passed since the process unit reached maximum temperature, maintain the hourly average operating temperature at the inlet of the catalyst bed at or above the minimum allowable operating temperature established for the corresponding period during the most recent performance test, as determined according to item 12 of Table 4 to this subpart; and
b. For each subsequent hour of the batch cycle, maintain the hourly average operating temperature at the inlet of the catalyst bed at or above the minimum allowable operating temperature established for the corresponding hour during the most recent performance test, as specified in item 13 of Table 4 to this subpart; and
c. Check the activity level of the catalyst at least every 12 months.
10. Each new kiln that is used to process clay refractory productsSatisfy the applicable operating limits specified in items 11 through 13 of this table.
11. Each affected kiln that is equipped with a DLAa. Maintain the 3-hour block average pressure drop across the DLA at or above the minimum levels established during the most recent performance test; and
b. Maintain free-flowing limestone in the feed hopper, silo, and DLA at all times; and
c. Maintain the limestone feeder at or above the level established during the most recent performance test; and
d. Use the same grade of limestone from the same source as was used during the most recent performance test and maintain records of the source and type of limestone used; and
e. Maintain no VE from the stack.
12. Each affected kiln that is equipped with a DIFF or DLS/FFa. Initiate corrective action within 1 hour of a bag leak detection system alarm and complete corrective actions in accordance with the OM&M plan; and
b. Verify at least once each 8-hour shift that lime is free-flowing by means of a visual check, checking the output of a load cell, carrier gas/lime flow indicator, or carrier gas pressure drop measurement system; and
c. Record the lime feeder setting daily to verify that the feeder setting is at or above the level established during the most recent performance test.
13. Each affected kiln that is equipped with a wet scrubbera. Maintain the 3-hour block average pressure drop across the scrubber, liquid pH, and liquid flow rate at or above the minimum levels established during the most recent performance test; and
b. If chemicals are added to the scrubber liquid, maintain the 3-hour block average chemical feed rate at or above the minimum chemical feed rate established during the most recent performance test.
14. Each new and existing kiln used to process clay refractory products that is equipped with an activated carbon injection systemMaintain the average carbon flow rate for each 3-hour block period at or above the average carbon flow rate established during the Hg performance test in which compliance was demonstrated.
15. Each new and existing kiln that is used to process clay refractory products with no add-on control and each existing kiln that is equipped with a DLAMaintain no VE from the stack.
16. Each existing kiln used to process clay refractory products that is equipped with a FFInitiate corrective action within 1 hour of a bag leak detection system alarm and complete corrective actions in accordance with the OM&M plan OR maintain no VE from the stack.
17. Each existing kiln used to process clay refractory products that is equipped with a wet scrubberMaintain the 3-hour block average pressure drop across the scrubber and liquid flow rate at or above the minimum levels established during the most recent performance test.

[86 FR 66070, Nov. 19, 2021]


Table 3 to Subpart SSSSS of Part 63—Work Practice Standards

As stated in § 63.9788, you must comply with the work practice standards for affected sources in the following table:


For . . .
You must . . .
According to one of the following requirements . . .
1. Each basket or container that is used for holding fired refractory shapes in an existing shape preheater and autoclave during the pitch impregnation processa. Control POM emissions from any affected shape preheateri. At least every 10 preheating cycles, clean the residual pitch from the surfaces of the basket or container by abrasive blasting prior to placing the basket or container in the affected shape preheater; or

ii. At least every 10 preheating cycles, subject the basket or container to a thermal process cycle that meets or exceeds the operating temperature and cycle time of the affected preheater, AND is conducted in a process unit that is exhausted to a thermal or catalytic oxidizer that is comparable to the control device used on an affected defumer or coking oven; or

iii. Capture emissions from the affected shape preheater and vent them to the control device that is used to control emissions from an affected defumer or coking oven, or to a comparable thermal or catalytic oxidizer.
2. Each new or existing pitch working tankControl POM emissionsCapture emissions from the affected pitch working tank and vent them to the control device that is used to control emissions from an affected defumer or coking oven, OR to a comparable thermal or catalytic oxidizer.
3. Each new or existing chromium refractory products kilnMinimize fuel-based HAP emissionsBefore May 19, 2022, use natural gas, or equivalent, as the kiln fuel, except during periods of natural gas curtailment or supply interruption, as defined in § 63.9824. On and after May 19, 2022, use natural gas, or equivalent, as the kiln fuel at all times.
4. Each existing clay refractory products kilnMinimize fuel-based HAP emissionsBefore May 19, 2022, use natural gas, or equivalent, as the kiln fuel, except during periods of natural gas curtailment or supply interruption, as defined in § 63.9824. On and after May 19, 2022, use natural gas, or equivalent, as the kiln fuel at all times.
5. Each affected continuous kiln used to manufacture refractory products that use organic HAP that is equipped with an emission control device for THC with Administrator approval to take the control device out of service for scheduled maintenance, as specified in § 63.9792(e)Minimize HAP emissionsi. Before May 19, 2022, minimize HAP emissions from the affected kiln during all periods of scheduled maintenance of the kiln control device when the kiln is operating and the control device is out of service consistent with your OM&M plan and minimize the time period during which the kiln is operating and the control device is out of service; or

ii. On and after May 19, 2022, minimize HAP emissions during the period when the kiln is operating and the control device is out of service by maintaining the organic HAP processing rate (lb/hr) below the average organic HAP processing rate based on actual production on a 6-month rolling basis (not to include periods of kiln shut down) or below the organic HAP processing rate (lb/hr) that coincides with the lowest hour of the most recent 3-hour performance test, whichever is lower); and minimize the time period during which the kiln is operating and the control device is out of service, not to exceed 750 hours for the year (on a 12-month rolling basis).
6. Each new or existing curing oven, shape dryer, and kiln that is used to process refractory products that use organic HAP, on and after Novermber 19, 2021Minimize fuel-based HAP emissionsUse natural gas, or equivalent, as the kiln fuel, at all times.

[86 FR 66072, Nov. 19, 2021]


Table 4 to Subpart SSSSS to Part 63—Requirements for Performance Tests

As stated in § 63.9800, you must comply with the requirements for performance tests for affected sources in the following table:


For . . .
You must . . .
Using . . .
According to the following requirements . . .
1. Each affected source listed in Table 1 to this subparta. Conduct performance testsi. The requirements of the general provisions in subpart A of this part and the requirements to this subpart(1) Record the date of the test; and

(2) Identify the emission source that is tested; and

(3) Collect and record the corresponding operating parameter and emission test data listed in this table for each run of the performance test; and
(4) Repeat the performance test at least every 5 years; and
(5) Repeat the performance test before changing the parameter value for any operating limit specified in your OM&M plan; and
(6) If complying with the THC concentration or THC percentage reduction limits specified in items 2 through 9 of Table 1 to this subpart, repeat the performance test under the conditions specified in items 2.a.2. and 2.a.3. of this table; and
(7) If complying with the emission limits for new clay refractory products kilns specified in items 10 and 11 of Table 1 to this subpart, repeat the performance test under the conditions specified in items 14.a.i.4. and 17.a.i.4. of this table.
b. Select the locations of sampling ports and the number of traverse pointsi. Method 1 or 1A of 40 CFR part 60, appendix A-1(1) To demonstrate compliance with the percentage reduction limits specified in items 2.b., 3.b., 6.b., 7.b., 10, and 11 of Table 1 to this subpart, locate sampling sites at the inlet of the control device and at either the outlet of the control device or at the stack prior to any releases to the atmosphere; and
(2) To demonstrate compliance with any other emission limit specified in Table 1 to this subpart, locate all sampling sites at the outlet of the control device or at the stack prior to any releases to the atmosphere.
c. Determine gas velocity and volumetric flow rateMethod 2, 2A, 2C, 2D, 2F, or 2G of 40 CFR part 60, appendix A-1 and A-2Measure gas velocities and volumetric flow rates at 1-hour intervals throughout each test run.
d. Conduct gas molecular weight analysisi. Method 3, 3A, or 3B of 40 CFR part 60, appendix A-2; or

ii. ASME PTC 19.10-1981—Part 10
a
As specified in the applicable test method.

You may use the manual procedures (but not instrumental procedures) of ASME PTC 19.10-1981—Part 10
a as an alternative to EPA Method 3B.
e. Measure gas moisture contentMethod 4 of 40 CFR part 60, appendix A-3As specified in the applicable test method.
2. Each new or existing curing oven, shape dryer, and kiln that is used to process refractory products that use organic HAP; each new or existing coking oven and defumer that is used to produce pitch-impregnated refractory products; each new shape preheater that is used to produce pitch-impregnated refractory products; AND each new or existing process unit that is exhausted to a thermal or catalytic oxidizer that also controls emissions from an affected shape preheater or pitch working tanka. Conduct performance tests(1) Conduct the performance test while the source is operating at the maximum organic HAP processing rate, as defined in § 63.9824, reasonably expected to occur; and

(2) Repeat the performance test before starting production of any product for which the organic HAP processing rate is likely to exceed the maximum organic HAP processing rate established during the most recent performance test by more than 10 percent, as specified in § 63.9798(c); and

(3) Repeat the performance test on any affected uncontrolled kiln following process changes (e.g., shorter curing oven cycle time) that could increase organic HAP emissions from the affected kiln, as specified in § 63.9798(d).
b. Satisfy the applicable requirements listed in items 3 through 13 of this table
3. Each affected continuous process unita. Perform a minimum of 3 test runsThe appropriate test methods specified in items 1, 4, and 5 of this tableEach test run must be at least 1 hour in duration.
b. Establish the operating limit for the maximum organic HAP processing ratei. Method 311 of 40 CFR part 63, appendix A, OR material safety data sheets (MSDS), OR product labels to determine the mass fraction of organic HAP in each resin, binder, or additive; and(1) Calculate and record the organic HAP content of all refractory shapes that are processed during the performance test, based on the mass fraction of organic HAP in the resins, binders, or additives; the mass fraction of each resin, binder, or additive, in the product; and the process feed rate; and
ii. Product formulation data that specify the mass fraction of each resin, binder, and additive in the products that are processed during the performance test; and(2) Calculate and record the organic HAP processing rate (pounds per hour) for each test run; and
iii. Process feed rate data (tons per hour)(3) Calculate and record the maximum organic HAP processing rate as the average of the organic HAP processing rates for the three test runs.
c. Record the operating temperature of the affected sourceProcess dataDuring each test run and at least once per hour, record the operating temperature in the highest temperature zone of the affected source.
4. Each continuous process unit that is subject to the THC emission limit listed in item 2.a., 3.a., 4, or 5 of Table 1 to this subparta. Measure THC concentrations at the outlet of the control device or in the stacki. Method 25A of 40 CFR part 60, appendix A-7(1) Each minute, measure and record the concentrations of THC in the exhaust stream; and

(2) Provide at least 50 1-minute measurements for each valid hourly average THC concentration.
b. Measure oxygen concentrations at the outlet of the control device or in the stacki. Method 3A of 40 CFR part 60, appendix A-2(1) Each minute, measure and record the concentrations of oxygen in the exhaust stream; and

(2) Provide at least 50 1-minute measurements for each valid hourly average THC concentration.
c. Determine the hourly average THC concentration, corrected to 18 percent oxygeni. Equation 1 of § 63.9800(g)(1); and

ii. The 1-minute THC and oxygen concentration data
(1) Calculate the hourly average THC concentration for each hour of the performance test as the average of the 1-minute THC measurements; and

(2) Calculate the hourly average oxygen concentration for each hour of the performance test as the average of the 1-minute oxygen measurements; and
(3) Correct the hourly average THC concentrations to 18 percent oxygen using Equation 1 of § 63.9800(g)(1).
d. Determine the 3-hour block average THC emission concentration, corrected to 18 percent oxygenThe hourly average concentration of THC, corrected to 18 percent oxygen, for each test runCalculate the 3-hour block average THC emission concentration, corrected to 18 percent oxygen, as the average of the hourly average THC emission concentrations, corrected to 18 percent oxygen.
5. Each continuous process unit that is subject to the THC percentage reduction limit listed in item 2.b. or 3.b. of Table 1 to this subparta. Measure THC concentrations at the inlet and outlet of the control devicei. Method 25A of 40 CFR part 60, appendix A-7(1) Each minute, measure and record the concentrations of THC at the inlet and outlet of the control device; and

(2) Provide at least 50 1-minute measurements for each valid hourly average THC concentration at the control device inlet and outlet.
b. Determine the hourly THC mass emissions rates at the inlet and outlet of the control devicei. The 1-minute THC concentration data at the control device inlet and outlet; and

ii. The volumetric flow rates at the control device inlet and outlet
Calculate the hourly THC mass emissions rates at the control device inlet and outlet for each hour of the performance test.
c. Determine the 3-hour block average THC percentage reductioni. The hourly THC mass emissions rates at the inlet and outlet of the control device(1) Calculate the hourly THC percentage reduction for each hour of the performance test using Equation 2 of § 63.9800(g)(1); and

(2) Calculate the 3-hour block average THC percentage reduction.
6. Each continuous process unit that is equipped with a thermal oxidizera. Establish the operating limit for the minimum allowable thermal oxidizer combustion chamber temperaturei. Continuous recording of the output of the combustion chamber temperature measurement device(1) At least every 15 minutes, measure and record the thermal oxidizer combustion chamber temperature; and

(2) Provide at least one measurement during at least three 15-minute periods per hour of testing; and

(3) Calculate the hourly average thermal oxidizer combustion chamber temperature for each hour of the performance test; and
(4) Calculate the minimum allowable combustion chamber temperature as the average of the combustion chamber temperatures for the three test runs, minus 14 °C (25 °F).
7. Each continuous process unit that is equipped with a catalytic oxidizera. Establish the operating limit for the minimum allowable temperature at the inlet of the catalyst bedi. Continuous recording of the output of the temperature measurement device(1) At least every 15 minutes, measure and record the temperature at the inlet of the catalyst bed; and

(2) Provide at least one catalyst bed inlet temperature measurement during at least three 15-minute periods per hour of testing; and

(3) Calculate the hourly average catalyst bed inlet temperature for each hour of the performance test; and
(4) Calculate the minimum allowable catalyst bed inlet temperature as the average of the catalyst bed inlet temperatures for the three test runs, minus 14 °C (25 °F).
8. Each affected batch process unita. Perform a minimum of two test runsi. The appropriate test methods specified in items 1, 9, and 10 of this table(1) Each test run must be conducted over a separate batch cycle unless you satisfy the requirements of § 63.9800(f)(3) and (4); and
(2) Each test run must begin with the start of a batch cycle, except as specified in item 8.a.i.4. of this table; and
(3) Each test run must continue until the end of the batch cycle, except as specified in items 8.a.i.4. and 8.a.i.5. of this table; and
(4) If you develop an emissions profile, as described in § 63.9802(a), AND for sources equipped with a thermal or catalytic oxidizer, you do not reduce the oxidizer operating temperature, as specified in item 13 of this table, you can limit each test run to the 3-hour peak THC emissions period; and
(5) If you do not develop an emissions profile, a test run can be stopped, and the results of that run considered complete, if you measure emissions continuously until at least 3 hours after the affected process unit has reached maximum temperature, AND the hourly average THC mass emissions rate has not increased during the 3-hour period since maximum process temperature was reached, and the hourly average concentrations of THC at the inlet of the control device have not exceeded 20 ppmvd, corrected to 18 percent oxygen, during the 3-hour period since maximum process temperature was reached or the hourly average THC percentage reduction has been at least 95 percent during the 3-hour period since maximum process temperature was reached, AND, for sources equipped with a thermal or catalytic oxidizer, at least 1 hour has passed since any reduction in the operating temperature of the oxidizer, as specified in item 13 of this table.
b. Establish the operating limit for the maximum organic HAP processing ratei. Method 311 of 40 CFR part 63, appendix A, OR MSDS, OR product labels to determine the mass fraction of organic HAP in each resin, binder, or additive; and(1) Calculate and record the organic HAP content of all refractory shapes that are processed during the performance test, based on the mass fraction of HAP in the resins, binders, or additives; the mass fraction of each resin, binder, or additive, in the product, and the batch weight prior to processing; and
ii. Product formulation data that specify the mass fraction of each resin, binder, and additive in the products that are processed during the performance test; and

iii. Batch weight (tons)
(2) Calculate and record the organic HAP processing rate (pounds per batch) for each test run; and

(3) Calculate and record the maximum organic HAP processing rate as the average of the organic HAP processing rates for the two test runs.
c. Record the batch cycle timeProcess dataRecord the total elapsed time from the start to the completion of the batch cycle.
d. Record the operating temperature of the affected sourceProcess dataRecord the operating temperature of the affected source at least once every hour from the start to the completion of the batch cycle.
9. Each batch process unit that is subject to the THC emission limit listed in item 6.a., 7.a., 8, or 9 of Table 1 to this subparta. Measure THC concentrations at the outlet of the control device or in the stacki. Method 25A of 40 CFR part 60, appendix A-7(1) Each minute, measure and record the concentrations of THC in the exhaust stream; and

(2) Provide at least 50 1-minute measurements for each valid hourly average THC concentration.
b. Measure oxygen concentrations at the outlet of the control device or in the stacki. Method 3A of 40 CFR part 60, appendix A-2(1) Each minute, measure and record the concentrations of oxygen in the exhaust stream; and

(2) Provide at least 50 1-minute measurements for each valid hourly average oxygen concentration.
c. Determine the hourly average THC concentration, corrected to 18 percent oxygeni. Equation 1 of § 63.9800(g)(1); and

ii. The 1-minute THC and oxygen concentration data
(1) Calculate the hourly average THC concentration for each hour of the performance test as the average of the 1-minute THC measurements; and

(2) Calculate the hourly average oxygen concentration for each hour of the performance test as the average of the 1-minute oxygen measurements; and

(3) Correct the hourly average THC concentrations to 18 percent oxygen using Equation 1 of § 63.9800(g)(1).
d. Determine the 3-hour peak THC emissions period for each test runThe hourly average THC concentrations, corrected to 18 percent oxygenSelect the period of 3 consecutive hours over which the sum of the hourly average THC concentrations, corrected to 18 percent oxygen, is greater than the sum of the hourly average THC emission concentrations, corrected to 18 percent oxygen, for any other period of 3 consecutive hours during the test run.
e. Determine the average THC concentration, corrected to 18 percent oxygen, for each test runThe hourly average THC emission concentrations, corrected to 18 percent oxygen, for the 3-hour peak THC emissions periodCalculate the average of the hourly average THC concentrations, corrected to 18 percent oxygen, for the 3 hours of the peak emissions period for each test run.
f. Determine the 2-run block average THC concentration, corrected to 18 percent oxygen, for the emission testThe average THC concentration, corrected to 18 percent oxygen, for each test runCalculate the average of the average THC concentrations, corrected to 18 percent oxygen, for each run.
10. Each batch process unit that is subject to the THC percentage reduction limit listed in item 6.b. or 7.b. of Table 1 to this subparta. Measure THC concentrations at the inlet and outlet of the control devicei. Method 25A of 40 CFR part 60, appendix A-7(1) Each minute, measure and record the concentrations of THC at the control device inlet and outlet; and

(2) Provide at least 50 1-minute measurements for each valid hourly average THC concentration at the control device inlet and outlet.
b. Determine the hourly THC mass emissions rates at the control device inlet and outleti. The 1-minute THC concentration data at the control device inlet and outlet; and

ii. The volumetric flow rates at the control device inlet and outlet
(1) Calculate the hourly mass emissions rates at the control device inlet and outlet for each hour of the performance test.
c. Determine the 3-hour peak THC emissions period for each test runThe hourly THC mass emissions rates at the control device inletSelect the period of 3 consecutive hours over which the sum of the hourly THC mass emissions rates at the control device inlet is greater than the sum of the hourly THC mass emissions rates at the control device inlet for any other period of 3 consecutive hours during the test run.
d. Determine the average THC percentage reduction for each test runi. Equation 2 of § 63.9800(g)(2); and

ii. The hourly THC mass emissions rates at the control device inlet and outlet for the 3-hour peak THC emissions period
Calculate the average THC percentage reduction for each test run using Equation 2 of § 63.9800(g)(2).
e. Determine the 2-run block average THC percentage reduction for the emission testThe average THC percentage reduction for each test runCalculate the average of the average THC percentage reductions for each test run.
11. Each batch process unit that is equipped with a thermal oxidizera. Establish the operating limit for the minimum thermal oxidizer combustion chamber temperaturei. Continuous recording of the output of the combustion chamber temperature measurement device(1) At least every 15 minutes, measure and record the thermal oxidizer combustion chamber temperature; and

(2) Provide at least one temperature measurement during at least three 15-minute periods per hour of testing; and

(3) Calculate the hourly average combustion chamber temperature for each hour of the 3-hour peak emissions period, as defined in item 9.d. or 10.c. of this table, whichever applies; and
(4) Calculate the minimum allowable thermal oxidizer combustion chamber operating temperature as the average of the hourly combustion chamber temperatures for the 3-hour peak emissions period, minus 14 °C (25 °F).
12. Each batch process unit that is equipped with a catalytic oxidizera. Establish the operating limit for the minimum temperature at the inlet of the catalyst bedi. Continuous recording of the output of the temperature measurement device(1) At least every 15 minutes, measure and record the temperature at the inlet of the catalyst bed; and

(2) Provide at least one catalyst bed inlet temperature measurement during at least three 15-minute periods per hour of testing; and

(3) Calculate the hourly average catalyst bed inlet temperature for each hour of the 3-hour peak emissions period, as defined in item 9.d. or 10.c. of this table, whichever applies; and
(4) Calculate the minimum allowable catalytic oxidizer catalyst bed inlet temperature as the average of the hourly catalyst bed inlet temperatures for the 3-hour peak emissions period, minus 14 °C (25 °F).
13. Each batch process unit that is equipped with a thermal or catalytic oxidizera. During each test run, maintain the applicable operating temperature of the oxidizer until emission levels allow the oxidizer to be shut off or the operating temperature of the oxidizer to be reduced(1) The oxidizer can be shut off or the oxidizer operating temperature can be reduced if you do not use an emission profile to limit testing to the 3-hour peak emissions period, as specified in item 8.a.i.4. of this table; and

(2) At least 3 hours have passed since the affected process unit reached maximum temperature; and

(3) The applicable emission limit specified in item 6.a. or 6.b. of Table 1 to this subpart was met during each of the previous three 1-hour periods; and

(4) The hourly average THC mass emissions rate did not increase during the 3-hour period since maximum process temperature was reached; and

(5) The applicable emission limit specified in item 6.a. and 6.b. of Table 1 to this subpart was met during each of the four 15-minute periods immediately following the oxidizer temperature reduction; and
(6) If the applicable emission limit specified in item 6.a. or 6.b. of Table 1 to this subpart was not met during any of the four 15-minute periods immediately following the oxidizer temperature reduction, you must return the oxidizer to its normal operating temperature as soon as possible and maintain that temperature for at least 1 hour; and
(7) Continue the test run until the applicable emission limit specified in items 6.a. and 6.b. of Table 1 to this subpart is met for at least four consecutive 15-minute periods that immediately follow the temperature reduction; and
(8) Calculate the hourly average oxidizer operating temperature for each hour of the performance test since the affected process unit reached maximum temperature.
14. Each new continuous kiln that is used to process clay refractory productsa. Measure emissions of HF and HCli. Method 26A of 40 CFR part 60, appendix A-8; or

ii. Method 26 of 40 CFR part 60, appendix A-8; or

iii. Method 320 of 40 CFR part 63, appendix A
(1) Conduct the test while the kiln is operating at the maximum production level; and

(2) You may use EPA Method 26 of 40 CFR part 60, appendix A-8, only if no acid PM (e.g., HF or HCl dissolved in water droplets emitted by sources controlled by a wet scrubber) is present; and
(3) If you use EPA Method 320 of 40 CFR part 63, appendix A, you must follow the analyte spiking procedures of Section 13 of EPA Method 320 unless you can demonstrate that the complete spiking procedure has been conducted at a similar source. ASTM D6348-12e1
a may be used as an alternative to EPA Method 320 if the test plan preparation and implementation in Annexes A1-A8 are mandatory and the %R in Annex A5 is determined for each target analyte and is equal or greater than 70 percent and less than or equal to 130 percent; and
(4) Repeat the performance test if the affected source is controlled with a DLA and you change the source of the limestone used in the DLA.
b. Perform a minimum of 3 test runsThe appropriate test methods specified in items 1 and 14.a. of this tableEach test run must be at least 1 hour in duration.
15. Each new continuous kiln that is subject to the production-based HF and HCl emission limits specified in items 10.a. and 10.b. of Table 1 to this subparta. Record the uncalcined clay processing ratei. Production data; and

ii. Product formulation data that specify the mass fraction of uncalcined clay in the products that are processed during the performance test
(1) Record the production rate (tons per hour of fired product); and

(2) Calculate and record the average rate at which uncalcined clay is processed (tons per hour) for each test run; and

(3) Calculate and record the 3-run average uncalcined clay processing rate as the average of the average uncalcined clay processing rates for each test run.
b. Determine the HF mass emissions rate at the outlet of the control device or in the stacki. Method 26A of 40 CFR part 60, appendix A-8; or

ii. Method 26 of 40 CFR part 60, appendix A-8; or

iii. Method 320 of 40 CFR part 63, appendix A
Calculate the HF mass emissions rate for each test.

ASTM D6348-12e1
a may be used as an alternative to EPA Method 320 if the test plan preparation and implementation in Annexes A1-A8 are mandatory and the %R in Annex A5 is determined for each target analyte and is equal or greater than 70 percent and less than or equal to 130 percent.
c. Determine the 3-hour block average production-based HF emissions ratei. The HF mass emissions rate for each test run; and

ii. The average uncalcined clay processing rate
(1) Calculate the hourly production-based HF emissions rate for each test run using Equation 3 of § 63.9800(g)(3); and

(2) Calculate the 3-hour block average production-based HF emissions rate as the average of the hourly production-based HF emissions rates for each test run.
d. Determine the HCl mass emissions rate at the outlet of the control device or in the stacki. Method 26A of 40 CFR part 60, appendix A-8; or

ii. Method 26 of 40 CFR part 60, appendix A-8; or

iii. Method 320 of 40 CFR part 63, appendix A
Calculate the HCl mass emissions rate for each test run.

ASTM D6348-12e1
a may be used as an alternative to EPA Method 320 if the test plan preparation and implementation in Annexes A1-A8 are mandatory and the %R in Annex A5 is determined for each target analyte and is equal or greater than 70 percent and less than or equal to 130 percent.
e. Determine the 3-hour block average production-based HCl emissions ratei. The HCl mass emissions rate for each test run; and

ii. The average uncalcined clay processing rate
(1) Calculate the hourly production-based HCl emissions rate for each test run using Equation 3 of § 63.9800(g)(3); and

(2) Calculate the 3-hour block average production-based HCl emissions rate as the average of the production-based HCl emissions rates for each test run.
16. Each new continuous kiln that is subject to the HF and HCl percentage reduction limits specified in items 10.a. and 10.b. of Table 1 to this subparta. Measure the HF mass emissions rates at the inlet and outlet of the control devicei. Method 26A of 40 CFR part 60, appendix A-8; or

ii. Method 26 of 40 CFR part 60, appendix A-8; or

iii. Method 320 of 40 CFR part 63, appendix A
Calculate the HF mass emissions rates at the control device inlet and outlet for each test run.

ASTM D6348-12e1
a may be used as an alternative to EPA Method 320 if the test plan preparation and implementation in Annexes A1-A8 are mandatory and the %R in Annex A5 is determined for each target analyte and is equal or greater than 70 percent and less than or equal to 130 percent.
b. Determine the 3-hour block average HF percentage reductioni. The HF mass emissions rates at the inlet and outlet of the control device for each test run(1) Calculate the hourly HF percentage reduction using Equation 2 of § 63.9800(g)(2); and

(2) Calculate the 3-hour block average HF percentage reduction as the average of the HF percentage reductions for each test run.
c. Measure the HCl mass emissions rates at the inlet and outlet of the control devicei. Method 26A of 40 CFR part 60, appendix A-8; or

ii. Method 26 of 40 CFR part 60, appendix A-8; or

iii. Method 320 of 40 CFR part 63, appendix A
Calculate the HCl mass emissions rates at the control device inlet and outlet for each test run.

ASTM D6348-12e1
a may be used as an alternative to EPA Method 320 if the test plan preparation and implementation in Annexes A1-A8 are mandatory and the %R in Annex A5 is determined for each target analyte and is equal or greater than 70 percent and less than or equal to 130 percent.
d. Determine the 3-hour block average HCl percentage reduction.i. The HCl mass emissions rates at the inlet and outlet of the control device for each test run(1) Calculate the hourly HCl percentage reduction using Equation 2 of § 63.9800(g)(2); and

(2) Calculate the 3-hour block average HCl percentage reduction as the average of HCl percentage reductions for each test run.
17. Each new batch process kiln that is used to process clay refractory productsa. Measure emissions of HF and HCl at the inlet and outlet of the control devicei. Method 26A of 40 CFR part 60, appendix A-8; or

ii. Method 26 of 40 CFR part 60, appendix A-8; or

iii. Method 320 of 40 CFR part 63, appendix A
(1) Conduct the test while the kiln is operating at the maximum production level; and

(2) You may use EPA Method 26 of 40 CFR part 60, appendix A, only if no acid PM (e.g., HF or HCl dissolved in water droplets emitted by sources controlled by a wet scrubber) is present; and

(3) If you use EPA Method 320 of 40 CFR part 63, you must follow the analyte spiking procedures of Section 13 of EPA Method 320 unless you can demonstrate that the complete spiking procedure has been conducted at a similar source

ASTM D6348-12e1
a may be used as an alternative to EPA Method 320 if the test plan preparation and implementation in Annexes A1-A8 are mandatory and the %R in Annex A5 is determined for each target analyte and is equal or greater than 70 percent and less than or equal to 130 percent.; and
(4) Repeat the performance test if the affected source is controlled with a DLA and you change the source of the limestone used in the DLA.
b. Perform a minimum of 2 test runsi. The appropriate test methods specified in items 1 and 17.a. of this table(1) Each test run must be conducted over a separate batch cycle unless you satisfy the requirements of § 63.9800(f)(3) and (4); and
(2) Each test run must consist of a series of 1-hour runs at the inlet and outlet of the control device, beginning with the start of a batch cycle, except as specified in item 17.b.i.4. of this table; and
(3) Each test run must continue until the end of the batch cycle, except as specified in item 17.b.i.4. of this table; and
(4) If you develop an emissions profile, as described in § 63.9802(b), you can limit each test run to the 3-hour peak HF emissions period.
c. Determine the hourly HF and HCl mass emissions rates at the inlet and outlet of the control devicei. The appropriate test methods specified in items 1 and 17.a. of this tableDetermine the hourly mass HF and HCl emissions rates at the inlet and outlet of the control device for each hour of each test run.
d. Determine the 3-hour peak HF emissions periodThe hourly HF mass emissions rates at the inlet of the control deviceSelect the period of 3 consecutive hours over which the sum of the hourly HF mass emissions rates at the control device inlet is greater than the sum of the hourly HF mass emissions rates at the control device inlet for any other period of 3 consecutive hours during the test run.
e. Determine the 2-run block average HF percentage reduction for the emissions testi. The hourly average HF emissions rates at the inlet and outlet of the control device(1) Calculate the HF percentage reduction for each hour of the 3-hour peak HF emissions period using Equation 2 of § 63.9800(g)(2); and

(2) Calculate the average HF percentage reduction for each test run as the average of the hourly HF percentage reductions for the 3-hour peak HF emissions period for that run; and
(3) Calculate the 2-run block average HF percentage reduction for the emission test as the average of the average HF percentage reductions for the two test runs.
f. Determine the 2-run block average HCl percentage reduction for the emission testi. The hourly average HCl emissions rates at the inlet and outlet of the control device(1) Calculate the HCl percentage reduction for each hour of the 3-hour peak HF emissions period using Equation 2 § 63.9800(g)(2); and

(2) Calculate the average HCl percentage reduction for each test run as the average of the hourly HCl percentage reductions for the 3-hour peak HF emissions period for that run; and
(3) Calculate the 2-run block average HCl percentage reduction for the emission test as the average of the average HCl percentage reductions for the two test runs.
18. Each new kiln that is used to process clay refractory products and is equipped with a DLAa. Establish the operating limit for the minimum pressure drop across the DLAData from the pressure drop measurement device during the performance test(1) At least every 15 minutes, measure the pressure drop across the DLA; and

(2) Provide at least one pressure drop measurement during at least three 15-minute periods per hour of testing; and

(3) Calculate the hourly average pressure drop across the DLA for each hour of the performance test; and
(4) Calculate and record the minimum pressure drop as the average of the hourly average pressure drops across the DLA for the two or three test runs, whichever applies.
b. Establish the operating limit for the limestone feeder settingData from the limestone feeder during the performance test(1) Ensure that limestone in the feed hopper, silo, and DLA is free-flowing at all times during the performance test; and

(2) Establish the limestone feeder setting 1 week prior to the performance test; and
(3) Record and maintain the feeder setting for the 1-week period that precedes the performance test and during the performance test.
19. Each new kiln that is used to process clay refractory products and is equipped with a DIFF or DLS/FFa. Document conformance with specifications and requirements of the bag leak detection systemData from the installation and calibration of the bag leak detection systemSubmit analyses and supporting documentation demonstrating conformance with EPA guidance and specifications for bag leak detection systems as part of the Notification of Compliance Status.
b. Establish the operating limit for the lime feeder settingi. Data from the lime feeder during the performance test(1) For continuous lime injection systems, ensure that lime in the feed hopper or silo is free-flowing at all times during the performance test; and

(2) Record the feeder setting for the three test runs; and

(3) If the feed rate setting varies during the three test runs, calculate and record the average feed rate for the two or three test runs, whichever applies.
20. Each new kiln that is used to process clay refractory products and is equipped with a wet scrubbera. Establish the operating limit for the minimum scrubber pressure dropi. Data from the pressure drop measurement device during the performance test(1) At least every 15 minutes, measure the pressure drop across the scrubber; and

(2) Provide at least one pressure drop measurement during at least three 15-minute periods per hour of testing; and

(3) Calculate the hourly average pressure drop across the scrubber for each hour of the performance test; and
(4) Calculate and record the minimum pressure drop as the average of the hourly average pressure drops across the scrubber for the two or three test runs, whichever applies.
b. Establish the operating limit for the minimum scrubber liquid pHi. Data from the pH measurement device during the performance test(1) At least every 15 minutes, measure scrubber liquid pH; and

(2) Provide at least one pH measurement during at least three 15-minute periods per hour of testing; and
(3) Calculate the hourly average pH values for each hour of the performance test; and
(4) Calculate and record the minimum liquid pH as the average of the hourly average pH measurements for the two or three test runs, whichever applies.
c. Establish the operating limit for the minimum scrubber liquid flow ratei. Data from the flow rate measurement device during the performance test(1) At least every 15 minutes, measure the scrubber liquid flow rate; and

(2) Provide at least one flow rate measurement during at least three 15-minute periods per hour of testing; and

(3) Calculate the hourly average liquid flow rate for each hour of the performance test; and
(4) Calculate and record the minimum liquid flow rate as the average of the hourly average liquid flow rates for the two or three test runs, whichever applies.
d. If chemicals are added to the scrubber liquid, establish the operating limit for the minimum scrubber chemical feed ratei. Data from the chemical feed rate measurement device during the performance test(1) At least every 15 minutes, measure the scrubber chemical feed rate; and

(2) Provide at least one chemical feed rate measurement during at least three 15-minute periods per hour of testing; and

(3) Calculate the hourly average chemical feed rate for each hour of the performance test; and
(4) Calculate and record the minimum chemical feed rate as the average of the hourly average chemical feed rates for the two or three test runs, whichever applies.
21. Each new and existing kiln that is used to process clay refractory products that is subject to the PM limits specified in items 10.c. 11.c, 12.a, and 13.a of Table 1 to this subpartMeasure PM emissionsMethod 5 of 40 CFR part 60, appendix A-3
22. Each new and existing kiln that is used to process clay refractory products that is subject to the Hg limits specified in items 10.d. 11.d, 12.b, and 13.b of Table 1 to this subpartMeasure Hg emissionsMethod 29 of 40 CFR part 60, appendix A-8ASTM D6784-16
a may be used as an alternative to EPA Method 29 (portion for Hg only).
23. Each new and existing kiln that is used to process clay refractory products and is equipped with an activated carbon injection systemEstablish the operating limit for the average carbon flow rateData from the carbon flow rate measurement conducted during the Hg performance testYou must measure the carbon flow rate during each test run, determine and record the block average carbon flow rate values for the three test runs, and determine and record the 3-hour block average of the recorded carbon flow rate measurements for the three test runs. The average of the three test runs establishes your minimum site-specific activated carbon flow rate operating limit.
24. Each existing kiln that is used to process clay refractory products and is equipped with a FF and a bag leak detection systemDocument conformance with specifications and requirements of the bag leak detection systemData from the installation and calibration of the bag leak detection systemSubmit analyses and supporting documentation demonstrating conformance with EPA guidance and specifications for bag leak detection systems as part of the Notification of Compliance Status.
25. Each existing kiln that is used to process clay refractory products and is equipped with a wet scrubbera. Establish the operating limit for the minimum scrubber pressure dropi. Data from the pressure drop measurement device during the performance test(1) At least every 15 minutes, measure the pressure drop across the scrubber; and

(2) Provide at least one pressure drop measurement during at least three 15-minute periods per hour of testing; and

(3) Calculate the hourly average pressure drop across the scrubber for each hour of the performance test; and
(4) Calculate and record the minimum pressure drop as the average of the hourly average pressure drops across the scrubber for the two or three test runs, whichever applies.
b. Establish the operating limit for the minimum scrubber liquid flow ratei. Data from the flow rate measurement device during the performance test(1) At least every 15 minutes, measure the scrubber liquid flow rate; and

(2) Provide at least one flow rate measurement during at least three 15-minute periods per hour of testing; and
(3) Calculate the hourly average liquid flow rate for each hour of the performance test; and
(4) Calculate and record the minimum liquid flow rate as the average of the hourly average liquid flow rates for the two or three test runs, whichever applies.


a Incorporated by reference, see § 63.14.


[86 FR 66073, Nov. 19, 2021]


Table 5 to Subpart SSSSS of Part 63—Initial Compliance With Emission Limits

As stated in § 63.9806, you must show initial compliance with the emission limits for affected sources according to the following table:


For . . .
For the following emission limit . . .
You have demonstrated compliance if . . .
1. Each affected source listed in Table 1 to this subparta. Each applicable emission limit listed in Table 1 to this subparti. Emissions measured using the test methods specified in Table 4 to this subpart satisfy the applicable emission limits specified in Table 1 to this subpart; and
ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the performance test period; and
iii. You report the results of the performance test in the Notification of Compliance Status, as specified by § 63.9812(e)(1) and (2).
2. Each new or existing curing oven, shape dryer, and kiln that is used to process refractory products that use organic HAP; each new or existing coking oven and defumer that is used to produce pitch-impregnated refractory products; each new shape preheater that is used to produce pitch-impregnated refractory products; AND each new or existing process unit that is exhausted to a thermal or catalytic oxidizer that also controls emissions from an affected shape preheater or pitch working tankAs specified in items 3 through 8 of this tableYou have satisfied the applicable requirements specified in items 3 through 8 of this table.
3. Each affected continuous process unit that is subject to the THC emission concentration limit listed in item 2.a., 3.a., 4, or 5 of Table 1 to this subpartThe average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygenThe 3-hour block average THC emission concentration measured during the performance test using EPA Methods 25A and 3A is equal to or less than 20 ppmvd, corrected to 18 percent oxygen.
4. Each affected continuous process unit that is subject to the THC percentage reduction limit listed in item 2.b. or 3.b. of Table 1 to this subpartThe average THC percentage reduction must equal or exceed 95 percentThe 3-hour block average THC percentage reduction measured during the performance test using EPA Method 25A is equal to or greater than 95 percent.
5. Each affected batch process unit that is subject to the THC emission concentration limit listed in item 6.a., 7.a., 8, or 9 of Table 1 to this subpartThe average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygenThe 2-run block average THC emission concentration for the 3-hour peak emissions period measured during the performance test using EPA Methods 25A and 3A is equal to or less than 20 ppmvd, corrected to 18 percent oxygen.
6. Each affected batch process unit that is subject to the THC percentage reduction limit listed in item 6.b. or 7.b. of Table 1 to this subpartThe average THC percentage reduction must equal or exceed 95 percentThe 2-run block average THC percentage reduction for the 3-hour peak emissions period measured during the performance test using EPA Method 25A is equal to or exceeds 95 percent.
7. Each affected continuous or batch process unit that is equipped with a control device other than a thermal or catalytic oxidizer and is subject to the emission limit listed in item 3 or 7 of Table 1 to this subparta. The average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygen; or

b. The average THC percentage reduction must equal or exceed 95 percent
i. You have installed a THC CEMS at the outlet of the control device or in the stack of the affected source; and

ii. You have satisfied the requirements of PS-8 of 40 CFR part 60, appendix B.
8. Each affected continuous or batch process unit that uses process changes to reduce organic HAP emissions and is subject to the emission limit listed in item 4 or 8 of Table 1 to this subpartThe average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygeni. You have installed a THC CEMS at the outlet of the control device or in the stack of the affected source; and

ii. You have satisfied the requirements of PS-8 of 40 CFR part 60, appendix B.
9. Each new continuous kiln that is used to process clay refractory productsa. The average HF emissions must not exceed 0.019 kg/Mg (0.038 lb/ton) of uncalcined clay processed; OR the average uncontrolled HF emissions must be reduced by at least 90 percenti. The 3-hour block average production-based HF emissions rate measured during the performance test using one of the methods specified in item 14.a.i. of Table 4 to this subpart is equal to or less than 0.019 kg/Mg (0.038 lb/ton) of uncalcined clay processed; or

The 3-hour block average HF emissions reduction measured during the performance test is equal to or greater than 90 percent.
b. The average HCl emissions must not exceed 0.091 kg/Mg (0.18 lb/ton) of uncalcined clay processed; OR the average uncontrolled HCl emissions must be reduced by at least 30 percenti. The 3-hour block average production-based HCl emissions rate measured during the performance test using one of the methods specified in item 14.a.i. of Table 4 to this subpart is equal to or less than 0.091 kg/Mg (0.18 lb/ton) of uncalcined clay processed; or

ii. The 3-hour block average HCl emissions reduction measured during the performance test is equal to or greater than 30 percent.
c. The average PM emissions must not exceed 1.4 kg/Mg (3.1 lb/hr)i. The 3-hour block average PM emissions measured during the performance test using one of the methods specified in item 21 of Table 4 to this subpart is equal to or less than 1.4 kg/Mg (3.1 lb/hr).
d. The average Hg emissions must not exceed 6.1 µg/dscm at 18 percent oxygeni. The 3-hour block average Hg emissions measured during the performance test using one of the methods specified in item 22 of Table 4 to this subpart is equal to or less than 6.1 µg/dscm at 18 percent oxygen.
10. Each new batch process kiln that is used to process clay refractory productsa. The average uncontrolled HF emissions must be reduced by at least 90 percentThe 2-run block average HF emission reduction measured during the performance test is equal to or greater than 90 percent.
b. The average uncontrolled HCl emissions must be reduced by at least 30 percentThe 2-run block average HCl emissions reduction measured during the performance test is equal to or greater than 30 percent.
c. The average PM emissions must not exceed 1.4 kg/Mg (3.1 lb/hr)i. The 2-run block average PM emissions measured during the performance test using one of the methods specified in item 21 of Table 4 to this subpart is equal to or less than 1.4 kg/Mg (3.1 lb/hr).
d. The average Hg emissions must not exceed 6.1 µg/dscm at 18 percent oxygeni. The 2-run block average Hg emissions measured during the performance test using one of the methods specified in item 22 of Table 4 to this subpart is equal to or less than 6.1 µg/dscm at 18 percent oxygen.
11. Each existing continuous kiln that is used to produce clay refractory products on and after November 20, 2022a. The average PM emissions must not exceed 4.3 kg/Mg (9.5 lb/hr)i. The 3-hour block average PM emissions measured during the performance test using one of the methods specified in item 21 of Table 4 to this subpart is equal to or less than 4.3 kg/Mg (9.5 lb/hr).
b. The average Hg emissions must not exceed 18 µg/dscm at 18 percent oxygeni. The 3-hour block average Hg emissions measured during the performance test using one of the methods specified in item 22 of Table 4 to this subpart is equal to or less than 18 µg/dscm at 18 percent oxygen.
12. Each existing batch kiln that is used to produce clay refractory products on and after November 20, 2022a. The average PM emissions must not exceed 4.3 kg/Mg (9.5 lb/hr)i. The 2-run block average PM emissions measured during the performance test using one of the methods specified in item 21 of Table 4 to this subpart is equal to or less than 4.3 kg/Mg (9.5 lb/hr).
b. The average Hg emissions must not exceed 18 µg/dscm at 18 percent oxygeni. The 2-run block average Hg emissions measured during the performance test using one of the methods specified in item 22 of Table 4 to this subpart is equal to or less than 18 µg/dscm at 18 percent oxygen.

[86 FR 66082, Nov. 19, 2021]


Table 6 to Subpart SSSSS of Part 63—Initial Compliance With Work Practice Standards

As stated in § 63.9806, you must show initial compliance with the work practice standards for affected sources according to the following table:


For each . . .
For the following standard . . .
You have demonstrated initial compliance if . . .
1. Each affected source listed in Table 3 to this subparta. Each applicable work practice standard listed in Table 3 to this subparti. You have selected a method for performing each of the applicable work practice standards listed in Table 3 to this subpart; and
ii. You have included in your Initial Notification a description of the method selected for complying with each applicable work practice standard, as required by § 63.9(b); and
iii. You submit a signed statement with the Notification of Compliance Status that you have implemented the applicable work practice standard listed in Table 3 to this subpart; and
iv. You have described in your OM&M plan the method for complying with each applicable work practice standard specified in Table 3 to this subpart.
2. Each basket or container that is used for holding fired refractory shapes in an existing shape preheater and autoclave during the pitch impregnation processa. Control POM emissions from any affected shape preheateri. You have implemented at least one of the work practice standards listed in item 1 of Table 3 to this subpart; and

ii. You have established a system for recording the date and cleaning method for each time you clean an affected basket or container.
3. Each affected new or existing pitch working tankControl POM emissionsYou have captured and vented emissions from the affected pitch working tank to the device that is used to control emissions from an affected defumer or coking oven, or to a thermal or catalytic oxidizer that is comparable to the control device used on an affected defumer or coking oven.
4. Each new or existing chromium refractory products kilnMinimize fuel-based HAP emissionsYou use natural gas, or equivalent, as the kiln fuel.
5. Each existing clay refractory products kilnMinimize fuel-based HAP emissionsYou use natural gas, or equivalent, as the kiln fuel.
6. Each new or existing curing oven, shape dryer, and kiln that is used to process refractory products that use organic HAP, on and after November 19, 2021Minimize fuel-based HAP emissionsYou use natural gas, or equivalent, as the kiln fuel.

[86 FR 66084, Nov. 19, 2021]


Table 7 to Subpart SSSSS of Part 63—Continuous Compliance with Emission Limits

As stated in § 63.9810, you must show continuous compliance with the emission limits for affected sources according to the following table:


For . . .
For the following emission limit . . .
You must demonstrate continuous compliance by . . .
1. Each affected source listed in Table 1 to this subparta. Each applicable emission limit listed in Table 1 to this subparti. Collecting and recording the monitoring and process data listed in Table 2 (operating limits) to this subpart; and
ii. Reducing the monitoring and process data associated with the operating limits specified in Table 2 to this subpart; and
iii. Recording the results of any control device inspections; and
iv. Reporting, in accordance with § 63.9814(e), any deviation from the applicable operating limits specified in Table 2 to this subpart.
2. Each new or existing curing oven, shape dryer, and kiln that is used to process refractory products that use organic HAP; each new or existing coking oven and defumer that is used to produce pitch-impregnated refractory products; each new shape preheater that is used to produce pitch-impregnated refractory products; AND each new or existing process unit that is exhausted to a thermal or catalytic oxidizer that also controls emissions from an affected shape preheater or pitch working tankAs specified in items 3 through 7 of this tableSatisfying the applicable requirements specified in items 3 through 7 of this table.
3. Each affected process unit that is equipped with a thermal or catalytic oxidizera. The average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygen; OR the average THC percentage reduction must equal or exceed 95 percenti. Collecting the applicable data measured by the control device temperature monitoring system, as specified in items 5, 6, 8, and 9 of Table 8 to this subpart; and

ii. Reducing the applicable data measured by the control device temperature monitoring system, as specified in items 5, 6, 8, and 9 of Table 8 to this subpart; and
iii. Maintaining the average control device operating temperature for the applicable averaging period specified in items 5, 6, 8, and 9 of Table 2 to this subpart at or above the minimum allowable operating temperature established during the most recent performance test.
4. Each affected process unit that is equipped with a control device other than a thermal or catalytic oxidizerThe average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygen; OR the average THC performance reduction must equal or exceed 95 percentOperating and maintaining a THC CEMS at the outlet of the control device or in the stack of the affected source, according to the requirements of Procedure 1 of 40 CFR part 60, appendix F.
5. Each affected process unit that uses process changes to meet the applicable emission limitThe average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygenOperating and maintaining a THC CEMS at the outlet of the control device or in the stack of the affected source, according to the requirements of Procedure 1 of 40 CFR part 60, appendix F.
6. Each affected continuous process unitThe average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygen; OR the average THC percentage reduction must equal or exceed 95 percentRecording the organic HAP processing rate (pounds per hour) and the operating temperature of the affected source, as specified in items 3.b. and 3.c. of Table 4 to this subpart.
7. Each affected batch process unitThe average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygen; OR the average THC percentage reduction must equal or exceed 95 percentRecording the organic HAP processing rate (pounds per batch); and process cycle time for each batch cycle; and hourly average operating temperature of the affected source, as specified in items 8.b. through 8.d. of Table 4 to this subpart.
8. Each new kiln that is used to process clay refractory productsAs specified in items 9 through 11 of this tableSatisfying the applicable requirements specified in items 9 through 11 of this table.
9. Each new affected kiln that is equipped with a DLAa. The average HF emissions must not exceed 0.019 kg/Mg (0.038 lb/ton) of uncalcined clay processed, OR the average uncontrolled HF emissions must be reduced by at least 90 percent; and

b. The average HCl emissions must not exceed 0.091 kg/Mg (0.18 lb/ton) of uncalcined clay processed, or the average uncontrolled HCl emissions must be reduced by at least 30 percent
i. Maintaining the pressure drop across the DLA at or above the minimum levels established during the most recent performance test; and

ii. Verifying that the limestone hopper contains an adequate amount of free-flowing limestone by performing a daily visual check of the limestone in the feed hopper; and

iii. Recording the limestone feeder setting daily to verify that the feeder setting is at or above the level established during the most recent performance test; and

iv. Using the same grade of limestone as was used during the most recent performance test and maintaining records of the source and grade of limestone.
c. The average PM emissions must not exceed 1.4 kg/Mg (3.1 lb/hr); and

d. The average Hg emissions must not exceed 6.1 µg/dscm, corrected to 18 percent oxygen
i. Performing VE observations of the stack at the frequency specified in § 63.9810(f) using EPA Method 22 of 40 CFR part 60, appendix A-7; maintaining no VE from the stack.
10. Each new affected kiln that is equipped with a DIFF or DLS/FFa. The average HF emissions must not exceed 0.019 kg/Mg (0.038 lb/ton) of uncalcined clay processed; OR the average uncontrolled HF emissions must be reduced by at least 90 percent; and

b. The average HCl emissions must not exceed 0.091 kg/Mg (0.18 lb/ton) of uncalcined clay processed; OR the average uncontrolled HCl emissions must be reduced by at least 30 percent; and

c. The average PM emissions must not exceed 1.4 kg/Mg (3.1 lb/hr); and

d. The average Hg emissions must not exceed 6.1 µg/dscm, corrected to 18 percent oxygen
i. Verifying at least once each 8-hour shift that lime is free-flowing by means of a visual check, checking the output of a load cell, carrier gas/lime flow indicator, or carrier gas pressure drop measurement system; and

ii. Recording feeder setting daily to verify that the feeder setting is at or above the level established during the most recent performance test; and

iii. Initiating corrective action within 1 hour of a bag leak detection system alarm AND completing corrective actions in accordance with the OM&M plan, AND operating and maintaining the fabric filter such that the alarm does not engage for more than 5 percent of the total operating time in a 6-month block reporting period.
11. Each new affected kiln that is equipped with a wet scrubbera. The average HF emissions must not exceed 0.019 kg/Mg (0.038 lb/ton) of uncalcined clay processed; OR the average uncontrolled HF emissions must be reduced by at least 90 percent; and

b. The average HCl emissions must not exceed 0.091 kg/Mg (0.18 lb/ton) of uncalcined clay processed; OR the average uncontrolled HCl emissions must be reduced by at least 30 percent; and

c. The average PM emissions must not exceed 1.4 kg/Mg (3.1 lb/hr); and

d. The average Hg emissions must not exceed 6.1 µg/dscm, corrected to 18 percent oxygen
i. Maintaining the pressure drop across the scrubber, liquid pH, and liquid flow rate at or above the minimum levels established during the most recent performance test; and

ii. If chemicals are added to the scrubber liquid, maintaining the average chemical feed rate at or above the minimum chemical feed rate established during the most recent performance test.
12. Each new affected kiln that is equipped with an activated carbon injection systemThe average Hg emissions must not exceed 6.1 µg/dscm, corrected to 18 percent oxygenCollecting the carbon flow rate data according to § 63.9804(a); reducing the carbon flow rate data to 3-hour block averages according to § 63.9804(a); maintaining the average carbon flow rate for each 3-hour block period at or above the average carbon flow rate established during the Hg performance test in which compliance was demonstrated.
13. Each existing affected kiln that is equipped with a DLA or no add-on controla. The average PM emissions must not exceed 4.3 kg/Mg (9.5 lb/hr); and

b. The average Hg emissions must not exceed 18 µg/dscm, corrected to 18 percent oxygen
i. Performing VE observations of the stack at the frequency specified in § 63.9810(f) using EPA Method 22 of 40 CFR part 60, appendix A-7; maintaining no VE from the stack.
14. Each existing affected kiln that is equipped with a DIFF or DLS/FFa. The average PM emissions must not exceed 4.3 kg/Mg (9.5 lb/hr)i. If you use a bag leak detection system, as prescribed in § 63.9804(f), initiating corrective action within 1 hour of a bag leak detection system alarm AND completing corrective actions in accordance with the OM&M plan, AND operating and maintaining the fabric filter such that the alarm does not engage for more than 5 percent of the total operating time in a 6-month block reporting period; OR
ii. Performing VE observations of the stack at the frequency specified in § 63.9810(f) using EPA Method 22 of 40 CFR part 60, appendix A-7; maintaining no VE from the stack.
15. Each existing affected kiln that is equipped with a wet scrubbera. The average PM emissions must not exceed 4.3 kg/Mg (9.5 lb/hr); and

b. The average Hg emissions must not exceed 18 µg/dscm, corrected to 18 percent oxygen

i. Maintaining the pressure drop across the scrubber and liquid flow rate at or above the minimum levels established during the most recent performance test.
16. Each existing affected kiln that is equipped with an activated carbon injection systemThe average Hg emissions must not exceed 18 µg/dscm, corrected to 18 percent oxygenCollecting the carbon flow rate data according to § 63.9804(a); reducing the carbon flow rate data to 3-hour block averages according to § 63.9804(a); maintaining the average carbon flow rate for each 3-hour block period at or above the average carbon flow rate established during the Hg performance test in which compliance was demonstrated.

[86 FR 66084, Nov. 19, 2021]


Table 8 to Subpart SSSSS of Part 63—Continuous Compliance with Operating Limits

As stated in § 63.9810, you must show continuous compliance with the operating limits for affected sources according to the following table:


For . . .
For the following operating limit . . .
You must demonstrate continuous compliance by . . .
1. Each affected source listed in Table 2 to this subparta. Each applicable operating limit listed in Table 2 to this subparti. Maintaining all applicable process and control device operating parameters within the limits established during the most recent performance test; and
ii. Conducting annually an inspection of all duct work, vents, and capture devices to verify that no leaks exist and that the capture device is operating such that all emissions are properly vented to the control device in accordance with the OM&M plan.
2. Each affected continuous kiln used to manufacture refractory products that use organic HAP that is equipped with a THC control devicea. The operating limits specified in items 2.a. through 2.c. of Table 2 to this subparti. Operating the control device on the affected kiln during all times except during periods of approved scheduled maintenance, as specified in § 63.9792(e); and

ii. Before May 19, 2022, minimizing HAP emissions from the affected kiln during all periods of scheduled maintenance of the kiln control device when the kiln is operating and the control device is out of service; on and after May 19, 2022, minimizing HAP emissions during the period when the kiln is operating and the control device is out of service by complying with the applicable standard in Table 3 to this subpart; and
iii. Minimizing the duration of all periods of scheduled maintenance of the kiln control device when the kiln is operating and the control device is out of service; on and after May 19, 2022, the total time during which the kiln is operating and the control device is out of service for the each year on a 12-month rolling basis must not exceed 750 hours.
3. Each new or existing curing oven, shape dryer, and kiln that is used to process refractory products that use organic HAP; each new or existing coking oven and defumer that is used to produce pitch-impregnated refractory products; each new shape preheater that is used to produce pitch-impregnated refractory products; AND each new or existing process unit that is exhausted to a thermal or catalytic oxidizer that also controls emissions from an affected shape preheater or pitch working tankAs specified in items 4 through 9 of this tableSatisfying the applicable requirements specified in items 4 through 9 of this table.
4. Each affected continuous process unitMaintain process operating parameters within the limits established during the most recent performance testi. Recording the organic HAP processing rate (pounds per hour); and

ii. Recording the operating temperature of the affected source at least hourly; and
iii. Maintaining the 3-hour block average organic HAP processing rate at or below the maximum organic HAP processing rate established during the most recent performance test.
5. Continuous process units that are equipped with a thermal oxidizerMaintain the 3-hour block average operating temperature in the thermal oxidizer combustion chamber at or above the minimum allowable operating temperature established during the most recent performance testi. Measuring and recording the thermal oxidizer combustion chamber temperature at least every 15 minutes; and

ii. Calculating the hourly average thermal oxidizer combustion chamber temperature; and
iii. Maintaining the 3-hour block average thermal oxidizer combustion chamber temperature at or above the minimum allowable operating temperature established during the most recent performance test; and
iv. Reporting, in accordance with § 63.9814(e), any 3-hour block average operating temperature measurements below the minimum allowable thermal oxidizer combustion chamber operating temperature established during the most recent performance test.
6. Continuous process units that are equipped with a catalytic oxidizera. Maintain the 3-hour block average temperature at the inlet of the catalyst bed at or above the minimum allowable catalyst bed inlet temperature established during the most recent performance testi. Measuring and recording the temperature at the inlet of the catalyst bed at least every 15 minutes; and

ii. Calculating the hourly average temperature at the inlet of the catalyst bed; and
iii. Maintaining the 3-hour block average temperature at the inlet of the catalyst bed at or above the minimum allowable catalyst bed inlet temperature established during the most recent performance test; and
iv. Reporting, in accordance with § 63.9814(e), any 3-hour block average catalyst bed inlet temperature measurements below the minimum allowable catalyst bed inlet temperature established during the most recent performance; and
v. Checking the activity level of the catalyst at least every 12 months and taking any necessary corrective action, such as replacing the catalyst, to ensure that the catalyst is performing as designed.
7. Each affected batch process unitMaintain process operating parameters within the limits established during the most recent performance testi. Recording the organic HAP processing rate (pounds per batch); and

ii. Recording the hourly average operating temperature of the affected source; and
iii. Recording the process cycle time for each batch cycle; and
iv. Maintaining the organic HAP processing rate at or below the maximum organic HAP processing rate established during the most recent performance test.
8. Batch process units that are equipped with a thermal oxidizerMaintain the hourly average temperature in the thermal oxidizer combustion chamber at or above the hourly average temperature established for the corresponding 1-hour period of the cycle during the most recent performance testi. Measuring and recording the thermal oxidizer combustion chamber temperature at least every 15 minutes; and

ii. Calculating the hourly average thermal oxidizer combustion chamber temperature; and
iii. From the start of each batch cycle until 3 hours have passed since the process unit reached maximum temperature, maintaining the hourly average operating temperature in the thermal oxidizer combustion chamber at or above the minimum allowable operating temperature established for the corresponding period during the most recent performance test, as determined according to item 11 of Table 4 to this subpart; and
iv. For each subsequent hour of the batch cycle, maintaining the hourly average operating temperature in the thermal oxidizer combustion chamber at or above the minimum allowable operating temperature established for the corresponding hour during the most recent performance test, as specified in item 13 of Table 4 to this subpart; and
v. Reporting, in accordance with § 63.9814(e), any temperature measurements below the minimum allowable thermal oxidizer combustion chamber temperature measured during the most recent performance test.
9. Batch process units that are equipped with a catalytic oxidizerMaintain the hourly average temperature at the inlet of the catalyst bed at or above the corresponding hourly average temperature established for the corresponding 1-hour period of the cycle during the most recent performance testi. Measuring and recording temperatures at the inlet of the catalyst bed at least every 15 minutes; and

ii. Calculating the hourly average temperature at the inlet of the catalyst bed; and
iii. From the start of each batch cycle until 3 hours have passed since the process unit reached maximum temperature, maintaining the hourly average operating temperature at the inlet of the catalyst bed at or above the minimum allowable bed inlet temperature established for the corresponding period during the most recent performance test, as determined according to item 12 of Table 4 to this subpart; and
iv. For each subsequent hour of the batch cycle, maintaining the hourly average operating temperature at the inlet of the catalyst bed at or above the minimum allowable bed inlet temperature established for the corresponding hour during the most recent performance test, as specified in item 13 of Table 4 to this subpart; and
v. Reporting, in accordance with § 63.9814(e), any catalyst bed inlet temperature measurements below the minimum allowable bed inlet temperature measured during the most recent performance test; and
vi. Checking the activity level of the catalyst at least every 12 months and taking any necessary corrective action, such as replacing the catalyst, to ensure that the catalyst is performing as designed.
10. Each new kiln that is used to process clay refractory productsAs specified in items 11 through 13 of this tableSatisfying the applicable requirements specified in items 11 through 13 of this table.
11. Each new kiln that is equipped a DLAa. Maintain the average pressure drop across the DLA for each 3-hour block period at or above the minimum pressure drop established during the most recent performance testi. Collecting the DLA pressure drop data, as specified in item 18.a. of Table 4 to this subpart; and

ii. Reducing the DLA pressure drop data to 1-hour and 3-hour block averages; and
iii. Maintaining the 3-hour block average pressure drop across the DLA at or above the minimum pressure drop established during the most recent performance test.
b. Maintain free-flowing limestone in the feed hopper, silo, and DLAVerifying that the limestone hopper has an adequate amount of free-flowing limestone by performing a daily visual check of the limestone hopper.
c. Maintain the limestone feeder setting at or above the level established during the most recent performance testRecording the limestone feeder setting at least daily to verify that the feeder setting is being maintained at or above the level established during the most recent performance test.
d. Use the same grade of limestone from the same source as was used during the most recent performance testUsing the same grade of limestone as was used during the most recent performance test and maintaining records of the source and grade of limestone.
e. Maintain no VE from the stacki. Performing VE observations of the stack at the frequency specified in § 63.9810(f) using EPA Method 22 of 40 CFR part 60, appendix A-7; and
ii. Maintaining no VE from the stack.
12. Each new kiln that is equipped with a DIFF or DLS/FFa. Initiate corrective action within 1 hour of a bag leak detection system alarm and complete corrective actions in accordance with the OM&M plan; AND operate and maintain the fabric filter such that the alarm does not engage for more than 5 percent of the total operating time in a 6-month block reporting periodi. Initiating corrective action within 1 hour of a bag leak detection system alarm and completing corrective actions in accordance with the OM&M plan; and

ii. Operating and maintaining the fabric filter such that the alarm does not engage for more than 5 percent of the total operating time in a 6-month block reporting period; in calculating this operating time fraction, if inspection of the fabric filter demonstrates that no corrective action is required, no alarm time is counted; if corrective action is required, each alarm shall be counted as a minimum of 1 hour; if you take longer than 1 hour to initiate corrective action, the alarm time shall be counted as the actual amount of time taken by you to initiate corrective action.

b. Maintain free-flowing lime in the feed hopper or silo at all times for continuous injection systems; AND maintain feeder setting at or above the level established during the most recent performance test for continuous injection systemsi. Verifying at least once each 8-hour shift that lime is free-flowing via a load cell, carrier gas/lime flow indicator, carrier gas pressure drop measurement system, or other system; recording all monitor or sensor output, and if lime is found not to be free flowing, promptly initiating and completing corrective actions; and

ii. Recording the feeder setting once each day of operation to verify that the feeder setting is being maintained at or above the level established during the most recent performance test.
13. Each new kiln that is used to process clay refractory products and is equipped with a wet scrubbera. Maintain the average pressure drop across the scrubber for each 3-hour block period at or above the minimum pressure drop established during the most recent performance testi. Collecting the scrubber pressure drop data, as specified in item 20.a. of Table 4 to this subpart; and

ii. Reducing the scrubber pressure drop data to 1-hour and 3-hour block averages; and
iii. Maintaining the 3-hour block average scrubber pressure drop at or above the minimum pressure drop established during the most recent performance test.
b. Maintain the average scrubber liquid pH for each 3-hour block period at or above the minimum scrubber liquid pH established during the most recent performance testi. Collecting the scrubber liquid pH data, as specified in item 20.b. of Table 4 to this subpart; and

ii. Reducing the scrubber liquid pH data to 1-hour and 3-hour block averages; and
iii. Maintaining the 3-hour block average scrubber liquid pH at or above the minimum scrubber liquid pH established during the most recent performance test.
c. Maintain the average scrubber liquid flow rate for each 3-hour block period at or above the minimum scrubber liquid flow rate established during the most recent performance testi. Collecting the scrubber liquid flow rate data, as specified in item 20.c. of Table 4 to this subpart; and

ii. Reducing the scrubber liquid flow rate data to 1-hour and 3-hour block averages; and
iii. Maintaining the 3-hour block average scrubber liquid flow rate at or above the minimum scrubber liquid flow rate established during the most recent performance test.
d. If chemicals are added to the scrubber liquid, maintain the average scrubber chemical feed rate for each 3-hour block period at or above the minimum scrubber chemical feed rate established during the most recent performance testi. Collecting the scrubber chemical feed rate data, as specified in item 20.d. of Table 4 to this subpart; and

ii. Reducing the scrubber chemical feed rate data to 1-hour and 3-hour block averages; and
iii. Maintaining the 3-hour block average scrubber chemical feed rate at or above the minimum scrubber chemical feed rate established during the most recent performance test.
14. Each new and existing affected kiln that is equipped with an activated carbon injection systema. Maintain the average carbon flow rate for each 3-hour block period at or above the average carbon flow rate established during the Hg performance test in which compliance was demonstratedi. Collecting the carbon flow rate data, as specified in item 23 of Table 4 to this subpart; and

ii. Reducing the carbon flow rate data to 3-hour block averages; and
iii. Maintaining the average carbon flow rate for each 3-hour block period at or above the average carbon flow rate established during the Hg performance test in which compliance was demonstrated.
15. Each existing affected kiln that is equipped with a DLA or no add-on controla. Maintain no VE from the stacki. Performing VE observations of the stack at the frequency specified in § 63.9810(f) using EPA Method 22 of 40 CFR part 60, appendix A-7; and
ii. Maintaining no VE from the stack.
16. Each existing affected kiln that is equipped with a FFa. Maintain no VE from the stack; ORi. Performing VE observations of the stack at the frequency specified in § 63.9810(f) using EPA Method 22 of 40 CFR part 60, appendix A-7; and
ii. Maintaining no VE from the stack.
b. Initiate corrective action within 1 hour of a bag leak detection system alarm and complete corrective actions in accordance with the OM&M plan; AND operate and maintain the fabric filter such that the alarm does not engage for more than 5 percent of the total operating time in a 6-month block reporting periodi. Initiating corrective action within 1 hour of a bag leak detection system alarm and completing corrective actions in accordance with the OM&M plan; and

ii. Operating and maintaining the fabric filter such that the alarm does not engage for more than 5 percent of the total operating time in a 6-month block reporting period; in calculating this operating time fraction, if inspection of the fabric filter demonstrates that no corrective action is required, no alarm time is counted; if corrective action is required, each alarm shall be counted as a minimum of 1 hour; if you take longer than 1 hour to initiate corrective action, the alarm time shall be counted as the actual amount of time taken by you to initiate corrective action.
17. Each existing affected kiln that is equipped with a wet scrubbera. Maintain the average pressure drop across the scrubber for each 3-hour block period at or above the minimum pressure drop established during the most recent performance testi. Collecting the scrubber pressure drop data, as specified in item 25.a of Table 4 to this subpart; and

ii. Reducing the scrubber pressure drop data to 1-hour and 3-hour block averages; and
iii. Maintaining the 3-hour block average scrubber pressure drop at or above the minimum pressure drop established during the most recent performance test.
b. Maintain the average scrubber liquid flow rate for each 3-hour block period at or above the minimum scrubber liquid flow rate established during the most recent performance testi. Collecting the scrubber liquid flow rate data, as specified in item 25.b. of Table 4 to this subpart; and

ii. Reducing the scrubber liquid flow rate data to 1-hour and 3-hour block averages; and
iii. Maintaining the 3-hour block average scrubber liquid flow rate at or above the minimum scrubber liquid flow rate established during the most recent performance test.

[86 FR 66087, Nov. 19, 2021]


Table 9 to Subpart SSSSS of Part 63—Continuous Compliance with Work Practice Standards

As stated in § 63.9810, you must show continuous compliance with the work practice standards for affected sources according to the following table:


For . . .
For the following work practice standard . . .
You must demonstrate continuous compliance by . . .
1. Each affected source listed in Table 3 to this subpartEach applicable work practice requirement listed in Table 3 to this subparti. Performing each applicable work practice standard listed in Table 3 to this subpart; and

ii. Maintaining records that document the method and frequency for complying with each applicable work practice standard listed in Table 3 to this subpart, as required by §§ 63.10(b) and 63.9816(c)(2).
2. Each basket or container that is used for holding fired refractory shapes in an existing shape preheater and autoclave during the pitch impregnation processControl POM emissions from any affected shape preheateri. Controlling emissions from the volatilization of residual pitch by implementing one of the work practice standards listed in item 1 of Table 3 to this subpart; and

ii. Recording the date and cleaning method each time you clean an affected basket or container.
3. Each new or existing pitch working tankControl POM emissionsCapturing and venting emissions from the affected pitch working tank to the control device that is used to control emissions from an affected defumer or coking oven, or to a thermal or catalytic oxidizer that is comparable to the control device used on an affected defumer or coking oven.
4. Each new or existing chromium refractory products kilnMinimize fuel-based HAP emissionsi. Before November 19, 2021, using natural gas, or equivalent, as the kiln fuel at all times except during periods of natural gas curtailment or supply interruption; on and after November 19, 2021, using natural gas, or equivalent, as the kiln fuel at all times; and
ii. Before November 19, 2021, if you intend to use an alternative fuel, submitting a notification of alternative fuel use within 48 hours of the declaration of a period of natural gas curtailment or supply interruption, as defined in § 63.9824; and
iii. Before November 19, 2021, submitting a report of alternative fuel use within 10 working days after terminating the use of the alternative fuel, as specified in § 63.9814(g).
5. Each existing clay refractory products kilnMinimize fuel-based HAP emissionsi. Before November 19, 2021, using natural gas, or equivalent, as the kiln fuel at all times except during periods of natural gas curtailment or supply interruption; on and after November 19, 2021, using natural gas, or equivalent, as the kiln fuel at all times; and
ii. Before November 19, 2021, if you intend to use an alternative fuel, submitting a notification of alternative fuel use within 48 hours of the declaration of a period of natural gas curtailment or supply interruption, as defined in § 63.9824; and
iii. Before November 19, 2021, submitting a report of alternative fuel use within 10 working days after terminating the use of the alternative fuel, as specified in § 63.9814(g).
6. Each affected continuous kiln used to manufacture refractory products that use organic HAP that is equipped with an emission control device for THCMinimize organic HAP emissionsi. Operating the control device at all times unless you receive Administrator approval to take the control device out of service for scheduled maintenance, as specified in § 63.9792(e); and
ii. Minimizing HAP emissions during the period when the kiln is operating and the control device is out of service as specified in item 5 of Table 3 to this subpart; and
iii. On and after November 19, 2021, recording the actual hourly organic HAP processing rate for the kiln while the control device was out of service and the amount of product manufactured in the kiln while the control device was out of service; and
iv. Recording the duration of each period when the kiln is operating and the control device is out of service and, on and after November 19, 2021, the total amount of time per year on a 12-month rolling basis that the kiln has operated and the control device has been out of service.
7. Each new or existing curing oven, shape dryer, and kiln that is used to process refractory products that use organic HAP, on and after November 19, 2021Minimize fuel-based HAP emissionsUsing natural gas, or equivalent, as the kiln fuel at all times.

[86 FR 66091, Nov. 19, 2021]


Table 10 to Subpart SSSSS of Part 63—Requirements for Reports

As stated in § 63.9814, you must comply with the requirements for reports in the following table:


You must submit a(n) . . .
The report must contain . . .
You must submit the report . . .
1. Compliance reportThe information in § 63.9814(c) through (f)Semiannually according to the requirements in § 63.9814(a) through (f).
2. Before May 19, 2022, immediate SSM report if you had a startup, shutdown, or malfunction during the reporting period that is not consistent with your SSMP, on and after May 19, 2022, immediate SSM report is not requireda. Actions taken for the eventBy fax or telephone within 2 working days after starting actions inconsistent with the plan.
b. The information in § 63.10(d)(5)(ii)By letter within 7 working days after the end of the event unless you have made alternative arrangements with the permitting authority.
3. Before May 19, 2022, report of alternative fuel useThe information in § 63.9814(g) and items 4 and 5 of Table 9 to this subpartIf you are subject to the work practice standard specified in item 3 or 4 of Table 3 to this subpart, and you use an alternative fuel in the affected kiln, by letter within 10 working days after terminating the use of the alternative fuel.
4. Performance test reportThe information in § 63.7(g)According to the requirements of § 63.9814(h).
5. CMS performance evaluation, as required for CEMSThe information in § 63.7(g)According to the requirements of § 63.9814(i).

[86 FR 66092, Nov. 19, 2021]


Table 11 to Subpart SSSSS of Part 63—Applicability of General Provisions to Subpart SSSSS

As stated in § 63.9820, you must comply with the applicable General Provisions requirements according to the following table:


Citation
Subject
Brief description
Applies to subpart SSSSS
§ 63.1ApplicabilityYes.
§ 63.2DefinitionsYes.
§ 63.3Units and AbbreviationsYes.
§ 63.4Prohibited ActivitiesCompliance date; circumvention, severabilityYes.
§ 63.5Construction/ReconstructionApplicability; applications; approvalsYes.
§ 63.6(a)ApplicabilityGeneral Provisions (GP) apply unless compliance extension; GP apply to area sources that become majorYes.
§ 63.6(b)(1)-(4)Compliance Dates for New and Reconstructed SourcesStandards apply at effective date; 3 years after effective date; upon startup; 10 years after construction or reconstruction commences for section 112(f)Yes.
§ 63.6(b)(5)NotificationYes.
§ 63.6(b)(6)[Reserved]
§ 63.6(b)(7)Compliance Dates for New and Reconstructed Area Sources That Become MajorArea sources that become major must comply with major source standards immediately upon becoming major, regardless of whether required to comply when they were area sourcesYes.
§ 63.6(c)(1)-(2)Compliance Dates for Existing SourcesComply according to date in subpart, which must be no later than 3 years after effective date; for section 112(f) standards, comply within 90 days of effective date unless compliance extensionYes.
§ 63.6(c)(3)-(4)[Reserved]
§ 63.6(c)(5)Compliance Dates for Existing Area Sources That Become MajorArea sources that become major must comply with major source standards by date indicated in subpart or by equivalent time period (for example, 3 years)Yes.
§ 63.6(d)[Reserved]
§ 63.6(e)(1)-(2)Operation & MaintenanceOperate to minimize emissions at all times; correct malfunctions as soon as practicable; requirements independently enforceable; information Administrator will use to determine if operation and maintenance requirements were met; see § 63.9792(b) for general duty requirement.Yes before May 19, 2022. No on and after May 19, 2022.
§ 63.6(e)(3)SSMP requirementsYes before May 19, 2022. No on and after May 19, 2022.
§ 63.6(f)(1)Compliance Except During SSMYou must comply with emission standards at all times except during SSMNo.
§ 63.6(f)(2)-(3)Methods for Determining ComplianceCompliance based on performance test, operation and maintenance plans, records, inspectionYes.
§ 63.6(g)(1)-(3)Alternative StandardProcedures for getting an alternative standard.Yes.
§ 63.6(h)(1)-(9)Opacity/Visible Emission (VE) StandardsNot applicable.
§ 63.6(i)(1)-(14)Compliance ExtensionProcedures and criteria for Administrator to grant compliance extensionYes.
§ 63.6(j)Presidential Compliance ExemptionPresident may exempt source categoryYes.
§ 63.7(a)(1)-(2)Performance Test DatesDates for conducting initial performance testing and other compliance demonstrations; must conduct 180 days after first subject to ruleYes.
§ 63.7(a)(3)Section 114 AuthorityAdministrator may require a performance test under CAA section 114 at any timeYes.
§ 63.7(b)(1)Notification of Performance TestMust notify Administrator 60 days before the testYes.
§ 63.7(b)(2)Notification of ReschedulingMust notify Administrator 5 days before scheduled date and provide rescheduled dateYes.
§ 63.7(c)Quality Assurance/Test PlanRequirements; test plan approval procedures; performance audit requirements; internal and external QA procedures for testingYes.
§ 63.7(d)Testing FacilitiesYes.
§ 63.7(e)(1)Conditions for Conducting Performance TestsSee § 63.9800.No, § 63.9800 specifies requirements.
§ 63.7(e)(2)Conditions for Conducting Performance TestsMust conduct according to subpart and EPA test methods unless Administrator approves alternativeYes.
§ 63.7(e)(3)Test Run DurationMust have three test runs of at least 1 hour each; compliance is based on arithmetic mean of three runs; conditions when data from an additional test run can be usedYes; Yes, except where specified in § 63.9800 for batch process sources; Yes.
§ 63.7(f)Alternative Test MethodYes.
§ 63.7(g)Performance Test Data AnalysisYes, except this subpart specifies how and when the performance test and performance evaluation results are reported.
§ 63.7(h)Waiver of TestYes.
§ 63.8(a)(1)Applicability of Monitoring RequirementsYes.
§ 63.8(a)(2)Performance SpecificationsPerformance Specifications in appendix B of 40 CFR part 60 applyYes.
§ 63.8(a)(3)[Reserved]
§ 63.8(a)(4)Monitoring with FlaresNot applicable.
§ 63.8(b)(1)MonitoringMust conduct monitoring according to standard unless Administrator approves alternativeYes.
§ 63.8(b)(2)-(3)Multiple Effluents and Multiple Monitoring SystemsSpecific requirements for installing and reporting on monitoring systemsYes.
§ 63.8(c)(1)Continuous Monitoring System Operation and MaintenanceMaintenance consistent with good air pollution control practicesYes before May 19, 2022. No on and after May 19, 2022.
§ 63.8(c)(2)-(3)Monitoring System InstallationMust install to get representative emission and parameter measurementsYes.
§ 63.8(c)(4)CMS RequirementsNo, § 63.9808 specifies requirements.
§ 63.8(c)(5)COMS Minimum Procedures