Collapse to view only § 63.8515 - What definitions apply to this subpart?
What This Subpart Covers
Emission Limitations and Work Practice Standards
General Compliance Requirements
Testing and Initial Compliance Requirements
- SECTION § 63.8435 - By what date must I conduct performance tests?
- SECTION § 63.8440 - When must I conduct subsequent performance tests?
- SECTION § 63.8445 - How do I conduct performance tests and establish operating limits?
- SECTION § 63.8450 - What are my monitoring installation, operation, and maintenance requirements?
- SECTION § 63.8455 - How do I demonstrate initial compliance with the emission limitations and work practice standards?
Continuous Compliance Requirements
Notifications, Reports, and Records
Other Requirements and Information
- APPENDIX - Table 1 to Subpart JJJJJ of Part 63—Emission Limits
- APPENDIX - Table 2 to Subpart JJJJJ of Part 63—Operating Limits
- APPENDIX - Table 3 to Subpart JJJJJ of Part 63—Work Practice Standards
- APPENDIX - Table 4 to Subpart JJJJJ of Part 63—Requirements for Performance Tests
- APPENDIX - Table 5 to Subpart JJJJJ of Part 63—Initial Compliance With Emission Limitations and Work Practice Standards
- APPENDIX - Table 6 to Subpart JJJJJ of Part 63—Continuous Compliance With Emission Limitations and Work Practice Standards
- APPENDIX - Table 7 to Subpart JJJJJ of Part 63—Compliance Dates
- APPENDIX - Table 8 to Subpart JJJJJ of Part 63—Deadlines for Submitting Notifications
- APPENDIX - Table 9 to Subpart JJJJJ of Part 63—Requirements for Reports
- APPENDIX - Table 10 to Subpart JJJJJ of Part 63—Applicability of General Provisions to Subpart JJJJJ
What This Subpart Covers
§ 63.8380 - What is the purpose of this subpart?
This subpart establishes national emission limitations for hazardous air pollutants (HAP) emitted from brick and structural clay products (BSCP) manufacturing facilities. This subpart also establishes requirements to demonstrate initial and continuous compliance with the emission limitations.
§ 63.8385 - Am I subject to this subpart?
You are subject to this subpart if you own or operate a BSCP manufacturing facility that is, is located at, or is part of, a major source of HAP emissions according to the criteria in paragraphs (a) and (b) of this section.
(a) A BSCP manufacturing facility is a plant site that manufactures brick (including, but not limited to, face brick, structural brick, and brick pavers); clay pipe; roof tile; extruded floor and wall tile; and/or other extruded, dimensional clay products. Brick and structural clay products manufacturing facilities typically process raw clay and shale, form the processed materials into bricks or shapes, and dry and fire the bricks or shapes. A plant site that manufactures refractory products, as defined in § 63.9824, or clay ceramics, as defined in § 63.8665, is not a BSCP manufacturing facility.
(b) 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.
§ 63.8390 - What parts of my plant does this subpart cover?
(a) This subpart applies to each existing, new, or reconstructed affected source at a BSCP manufacturing facility.
(b) For the purposes of this subpart, the affected sources are described in paragraphs (b)(1) and (2) of this section.
(1) All tunnel kilns at a BSCP manufacturing facility are an affected source. For the remainder of this subpart, a tunnel kiln with a design capacity equal to or greater than 9.07 megagrams per hour (Mg/hr) (10 tons per hour (tph)) of fired product will be called a large tunnel kiln, and a tunnel kiln with a design capacity less than 9.07 Mg/hr (10 tph) of fired product will be called a small tunnel kiln.
(2) Each periodic kiln is an affected source.
(c) Process units not subject to the requirements of this subpart are listed in paragraphs (c)(1) through (4) of this section.
(1) Kilns that are used exclusively for setting glazes on previously fired products are not subject to the requirements of this subpart.
(2) Raw material processing and handling.
(3) Dryers.
(4) Sources covered by subparts KKKKK and SSSSS of this part.
(d) A source is a new affected source if construction of the affected source began after December 18, 2014, and you met the applicability criteria at the time you began construction.
(e) An affected source is reconstructed if you meet the criteria as defined in § 63.2.
(f) An affected source is existing if it is not new or reconstructed.
§ 63.8395 - When do I have to comply with this subpart?
(a) You must comply with this subpart no later than the compliance dates in Table 7 to this subpart.
(b) You must meet the notification requirements in § 63.8480 according to the schedule in § 63.8480 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
§ 63.8405 - What emission limitations 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.
§ 63.8410 - What are my options for meeting the emission limitations and work practice standards?
(a) To meet the emission limitations in Tables 1 and 2 to this subpart, you must use one or more of the options listed in paragraphs (a)(1) and (2) of this section.
(1) Emissions control system. Use an emissions capture and collection system and an air pollution control device (APCD) and demonstrate that the resulting emissions meet the emission limits in Table 1 to this subpart, and that the capture and collection system and APCD meet the applicable operating limits in Table 2 to this subpart.
(2) Process changes. Use low-HAP raw materials or implement manufacturing process changes and demonstrate that the resulting emissions or emissions reductions meet the emission limits in Table 1 to this subpart.
(b) To meet the work practice standards for affected periodic kilns, you must comply with the requirements listed in Table 3 to this subpart.
(c) To meet the work practice standards for dioxins/furans for affected tunnel kilns, you must comply with the requirements listed in Table 3 to this subpart.
(d) To meet the work practice standards for affected tunnel kilns during periods of startup and shutdown, you must comply with the requirements listed in Table 3 to this subpart.
General Compliance Requirements
§ 63.8420 - What are my general requirements for complying with this subpart?
(a) You must be in compliance with the emission limitations (including operating limits) in this subpart at all times, except during periods that you are approved for and in compliance with the alternative standard for routine control device maintenance as specified in paragraph (d) of this section, and except during periods of start-up and shutdown, at which time you must comply with the applicable work practice standard specified in Table 3 to this subpart.
(b) 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. During the period between the compliance date specified for your affected source in § 63.8395 and the date upon which continuous monitoring systems (CMS) (e.g., continuous parameter monitoring systems) have been installed and verified 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.
(c) For each affected kiln that is subject to the emission limits specified in Table 1 to this subpart, you must prepare and implement a written operation, maintenance, and monitoring (OM&M) plan according to the requirements in § 63.8425.
(d) If you own or operate an affected kiln that is subject to the emission limits specified in Table 1 to this subpart and must perform routine maintenance on the control device for that kiln, you may bypass the kiln control device and continue operating the kiln subject to the alternative standard established in this paragraph upon approval by the Administrator and provided you satisfy the conditions listed in paragraphs (d)(1) through (5) of this section.
(1) You must request to use the routine control device maintenance alternative standard from the Administrator no later than 120 calendar days before the compliance date specified in § 63.8395. Your request must justify the need for the routine maintenance on the control device and the time required to accomplish the maintenance activities, describe the maintenance activities and the frequency of the maintenance activities, explain why the maintenance cannot be accomplished during kiln shutdowns, provide information stating whether the continued operation of the affected source will result in fewer emissions than shutting the source down while the maintenance is performed, describe how you plan to comply with paragraph (b) of this section during the maintenance, and provide any other documentation required by the Administrator.
(2) The routine control device maintenance must not exceed 4 percent of the annual operating uptime for each kiln.
(3) The request for the routine control device maintenance alternative standard, if approved by the Administrator, must be incorporated by reference in and attached to the affected source's title V permit.
(4) You must minimize HAP emissions during the period when the kiln is operating and the control device is offline by complying with the applicable standard in Table 3 to this subpart.
(5) You must minimize the time period during which the kiln is operating and the control device is offline.
(e) You must be in compliance with the work practice standards in this subpart at all times.
(f) You must be in compliance with the provisions of subpart A of this part, except as noted in Table 10 to this subpart.
§ 63.8425 - What do I need to know about operation, maintenance, and monitoring plans?
(a) For each affected kiln that is subject to the emission limits specified in Table 1 to this subpart, you must prepare, implement, and revise as necessary an OM&M plan that includes the information in paragraph (b) of this section. Your OM&M plan must be available for inspection by the delegated authority upon request.
(b) Your OM&M plan must include, as a minimum, the information in paragraphs (b)(1) through (13) of this section.
(1) Each process and APCD to be monitored, the type of monitoring device that will be used, and the operating parameters that will be monitored.
(2) A monitoring schedule that specifies the frequency that the parameter values will be determined and recorded.
(3) The limits for each parameter that represent continuous compliance with the emission limitations in § 63.8405. The limits must be based on values of the monitored parameters recorded during performance tests.
(4) Procedures for the proper operation and routine and long-term maintenance of each APCD, including a maintenance and inspection schedule that is consistent with the manufacturer's recommendations.
(5) Procedures for installing the 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 APCD).
(6) Performance and equipment specifications for the sample interface, the pollutant concentration or parametric signal analyzer, and the data collection and reduction system.
(7) Continuous monitoring system performance evaluation procedures and acceptance criteria (e.g., calibrations).
(8) Procedures for the proper operation and maintenance of monitoring equipment consistent with the requirements in §§ 63.8450 and 63.8(c)(1), (3), (7), and (8).
(9) Continuous monitoring system data quality assurance procedures consistent with the requirements in § 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 in § 63.8(d)(2) 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).
(10) Continuous monitoring system recordkeeping and reporting procedures consistent with the requirements in §§ 63.8485 and 63.8490.
(11) Procedures for responding to operating parameter deviations, including the procedures in paragraphs (b)(11)(i) through (iii) of this section.
(i) Procedures for determining the cause of the operating parameter deviation.
(ii) Actions necessary 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 corrective actions were initiated and completed.
(12) Procedures for keeping records to document compliance.
(13) If you operate an affected kiln and you plan to take the kiln control device out of service for routine maintenance, as specified in § 63.8420(d), the procedures specified in paragraphs (b)(13)(i) and (ii) of this section.
(i) Procedures for minimizing HAP emissions from the kiln during periods of routine maintenance of the kiln control device when the kiln is operating and the control device is offline.
(ii) Procedures for minimizing the duration of any period of routine maintenance on the kiln control device when the kiln is operating and the control device is offline.
(c) 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 (c)(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 performance test results and the revised operating limits as part of the Notification of Compliance Status required under § 63.9(h).
(d) If you are revising the inspection and maintenance procedures in your OM&M plan, you do not need to conduct a new performance test.
Testing and Initial Compliance Requirements
§ 63.8435 - By what date must I conduct performance tests?
For each affected kiln that is subject to the emission limits specified in Table 1 to this subpart, you must conduct performance tests within 180 calendar days after the compliance date that is specified for your source in § 63.8395 and according to the provisions in § 63.7(a)(2).
§ 63.8440 - When must I conduct subsequent performance tests?
(a) For each affected kiln that is subject to the emission limits specified in Table 1 to this subpart, you must conduct a performance test before renewing your 40 CFR part 70 operating permit or at least every 5 years following the initial performance test.
(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.
§ 63.8445 - 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 calibrate all monitoring equipment.
(c) Each performance test must be conducted according to the requirements in § 63.7 and under the specific conditions in Table 4 to this subpart.
(d) Performance tests shall be conducted under such conditions as the Administrator specifies to you based on representative performance of the affected source for the period being tested. Representative conditions exclude periods of startup and shutdown. You may not conduct performance tests during periods of malfunction. 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. Upon request, you shall make available to the Administrator such records as may be necessary to determine the conditions of performance tests.
(e) 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.
(f) You must use the data gathered during the performance test and the equations in paragraphs (f)(1) and (2) of this section to determine compliance with the emission limitations.
(1) To determine compliance with the production-based particulate matter (PM) and mercury (Hg) emission limits in Table 1 to this subpart, you must calculate your mass emissions per unit of production for each test run using Equation 1:
Where:(2) To determine compliance with the health-based standard for acid gas HAP for BSCP manufacturing facilities in Table 1 to this subpart, you must:
(i) Calculate the HCl-equivalent emissions for HF, HCl, and Cl
(ii) If you have multiple tunnel kilns at your facility, sum the HCl-equivalent values for all tunnel kilns at the facility using Equation 3:
Where:(iii) Compare this value to the health-based standard in Table 1 to this subpart.
(g) You must establish each site-specific operating limit in Table 2 to this subpart that applies to you as specified in paragraph (g)(1) of this section and in Table 4 to this subpart.
(1)(i) If you do not have an APCD installed on your kiln, calculate the maximum potential HCl-equivalent emissions for HF, HCl, and Cl
(ii) If you have multiple tunnel kilns at your facility, sum the maximum potential HCl-equivalent values for all tunnel kilns at the facility using Equation 5:
Where:(iii) If you have a single tunnel kiln at your facility and the total facility maximum potential HCl-equivalent emissions (E
(iv) If you have multiple tunnel kilns at your facility and the total facility maximum potential HCl-equivalent emissions (E
(2) [Reserved]
(h) For each affected kiln that is subject to the emission limits specified in Table 1 to this subpart and is equipped with an 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 (h)(1) and (2) of this section.
(1) Submit a request for approval of alternative monitoring procedures to the Administrator no later than the notification of intent to conduct a performance test. The request must contain the information specified in paragraphs (h)(1)(i) through (iv) of this section.
(i) A description of the alternative APCD or process changes.
(ii) The type of monitoring device or procedure that will be used.
(iii) The operating parameters that will be monitored.
(iv) The frequency that the operating parameter values will be determined and recorded to establish continuous compliance with the operating limits.
(2) Establish site-specific operating limits during the performance test based on the information included in the approved alternative monitoring procedures request and, as applicable, as specified in Table 4 to this subpart.
§ 63.8450 - What are my monitoring installation, operation, and maintenance requirements?
(a) You must install, operate, and maintain each CMS according to your OM&M plan and the requirements in paragraphs (a)(1) through (5) of this section.
(1) Conduct a performance evaluation of each CMS according to your OM&M plan.
(2) The CMS must 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 if you collect more than four data values per hour) for that hour (not including startup, shutdown, malfunction, out-of-control periods, or periods of routine control device maintenance covered by the routine control device maintenance alternative standard as specified in § 63.8420(d)).
(3) Determine and record the 3-hour block averages of all recorded readings, calculated after every 3 hours of operation as the average of the previous 3 operating hours. To calculate the average for each 3-hour average period, you must have at least 75 percent of the recorded readings for that period (not including startup, shutdown, malfunction, out-of-control periods, or periods of routine control device maintenance covered by the routine control device maintenance alternative standard as specified in § 63.8420(d)).
(4) Record the results of each inspection, calibration, and validation check.
(5) At all times, maintain the monitoring equipment including, but not limited to, maintaining necessary parts for routine repairs of the monitoring equipment.
(b) For each liquid flow measurement device, you must meet the requirements in paragraphs (a)(1) through (5) and paragraphs (b)(1) through (3) of this section.
(1) Locate the flow sensor in a position that provides a representative flowrate.
(2) Use a flow sensor with a minimum measurement sensitivity of 2 percent of the liquid flowrate.
(3) At least semiannually, conduct a flow sensor calibration check.
(c) For each pressure measurement device, you must meet the requirements in paragraphs (a)(1) through (5) and paragraphs (c)(1) through (7) of this section.
(1) Locate the pressure sensor(s) in or as close to a position that provides a representative measurement of the pressure.
(2) Minimize or eliminate pulsating pressure, vibration, and internal and external corrosion.
(3) Use a gauge with a minimum measurement sensitivity of 0.5 inch of water or a transducer with a minimum measurement sensitivity of 1 percent of the pressure range.
(4) Check the pressure tap daily to ensure that it is not plugged.
(5) Using a manometer, check gauge calibration quarterly and transducer calibration monthly.
(6) Any time the sensor exceeds the manufacturer's specified maximum operating pressure range, conduct calibration checks or install a new pressure sensor.
(7) At least monthly, inspect all components for integrity, all electrical connections for continuity, and all mechanical connections for leakage.
(d) For each pH measurement device, you must meet the requirements in paragraphs (a)(1) through (5) and paragraphs (d)(1) through (4) of this section.
(1) Locate the pH sensor in a position that provides a representative measurement of pH.
(2) Ensure the sample is properly mixed and representative of the fluid to be measured.
(3) Check the pH meter's calibration at one point daily.
(4) At least monthly, inspect all components for integrity and all electrical connections for continuity.
(e) For each bag leak detection system, you must meet the requirements in paragraphs (e)(1) through (11) of this section.
(1) Each triboelectric bag leak detection system must be installed, calibrated, operated, and maintained according to EPA-454/R-98-015, “Fabric Filter Bag Leak Detection Guidance,” (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 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 audible alarm system that will sound automatically when an increase in relative PM emissions over a preset level is detected. The alarm must be located where it is easily heard 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 EPA-454/R-98-015, “Fabric Filter Bag Leak Detection Guidance,” (incorporated by reference, see § 63.14).
(10) Following initial adjustment of the system, the sensitivity or range, averaging period, alarm set points, or alarm delay time may not be adjusted except as detailed in your OM&M plan. In no case may the sensitivity be increased by more than 100 percent or decreased 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, as defined in section 5.2 of the “Fabric Filter Bag Leak Detection Guidance,” (incorporated by reference, see § 63.14). Record each adjustment.
(11) Record the results of each inspection, calibration, and validation check.
(f) For each lime, chemical, or carbon feed rate measurement device, you must meet the requirements in paragraphs (a)(1) through (5) and paragraphs (f)(1) and (2) of this section.
(1) Locate the measurement device in a position that provides a representative feed rate measurement.
(2) At least semiannually, conduct a calibration check.
(g) For each limestone feed system on a dry limestone adsorber (DLA), you must meet the requirements in paragraphs (a)(1), (4), and (5) of this section and must ensure on a monthly basis that the feed system replaces limestone at least as frequently as the schedule set during the performance test.
(h) For each temperature measurement device, you must meet the requirements in paragraphs (a)(1) through (5) and paragraphs (h)(1) through (3) of this section.
(1) Locate the measurement device in a position that provides a representative temperature.
(2) Use a measurement device with a minimum sensitivity of 1 percent of the temperature being measured.
(3) At least semiannually, conduct a calibration check.
(i) Requests for approval of alternate monitoring procedures must meet the requirements in §§ 63.8445(h) and 63.8(f).
§ 63.8455 - How do I demonstrate initial compliance with the emission limitations and work practice standards?
(a) You must demonstrate initial compliance with each emission limitation and work practice standard that applies to you according to 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 in § 63.8445 and Table 4 to this subpart.
(c) You must submit the Notification of Compliance Status containing the results of the initial compliance demonstration according to the requirements in § 63.8480(c).
Continuous Compliance Requirements
§ 63.8465 - How do I monitor and collect data to demonstrate continuous compliance?
(a) You must monitor and collect data according to this section.
(b) Except for periods of 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, malfunction, and routine control device maintenance as specified in § 63.8420(d) when the affected source is operating.
(c) You may not use data recorded during monitoring malfunctions, associated repairs, out-of-control periods, or required quality assurance or control activities for purposes of calculating data averages. You must use all the valid data collected during all other periods in assessing compliance. Any averaging period for which you do not have valid monitoring data and such data are required constitutes a deviation from the monitoring requirements.
§ 63.8470 - How do I demonstrate continuous compliance with the emission limitations and work practice standards?
(a) You must demonstrate continuous compliance with each emission limit, operating limit, and work practice standard in Tables 1, 2, and 3 to this subpart that applies to you according to the methods specified in Table 6 to this subpart.
(b) For each affected kiln that is subject to the emission limits specified in Table 1 to this subpart and is equipped with an 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 § 63.8445(h)(2) according to the methods specified in your approved alternative monitoring procedures request, as described in §§ 63.8445(h)(1) and 63.8(f).
(c) 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 § 63.8485(c)(9).
(d) [Reserved]
(e)(1) VE testing. You must demonstrate continuous compliance with the operating limits in Table 2 to this subpart for visible emissions (VE) from tunnel 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 by monitoring VE at each kiln stack according to the requirements in paragraphs (e)(1)(i) through (v) of this section.
(i) Perform daily VE observations of each kiln stack according to the procedures of Method 22 of 40 CFR part 60, appendix A-7. You must conduct the Method 22 test while the affected source is operating under normal conditions. The duration of each Method 22 test must be at least 15 minutes.
(ii) If VE are observed during any daily test conducted using Method 22 of 40 CFR part 60, appendix A-7, you must promptly conduct an opacity test, according to the procedures of 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 Method 22 testing from daily to weekly for a kiln stack if one of the conditions in paragraph (e)(1)(iii)(A) or (B) of this section is met.
(A) No VE are observed in 30 consecutive daily Method 22 tests for any kiln stack; or
(B) No opacity greater than 10 percent is observed during any of the 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 Method 9 test, you must promptly initiate and complete corrective actions according to your OM&M plan, resume testing of that kiln stack following Method 22 of 40 CFR part 60, appendix A-7, on a daily basis, as described in paragraph (e)(1)(i) of this section, and maintain that schedule until one of the conditions in paragraph (e)(1)(iii)(A) or (B) of this section is met, at which time you may again decrease the frequency of Method 22 testing to a weekly basis.
(v) If greater than 10 percent opacity is observed during any test conducted using Method 9 of 40 CFR part 60, appendix A-4, you must report these deviations by following the requirements in § 63.8485.
(2) Alternative to VE testing. In lieu of meeting the requirements under paragraph (e)(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 Method 5 of 40 CFR part 60, appendix A-3, and the provisions of § 63.8445(e) and (f)(1).
Notifications, Reports, and Records
§ 63.8480 - 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), (g)(1), and (h) that apply to you, by the dates specified.
(b) You must submit all of the notifications specified in Table 8 to this subpart that apply to you, by the dates specified.
(c) If you are required to conduct a performance test or other initial compliance demonstration as specified in Tables 4 and 5 to this subpart, your Notification of Compliance Status as specified in Table 8 to this subpart must include the information in paragraphs (c)(1) through (3) of this section.
(1) The requirements in § 63.9(h)(2)(i).
(2) The operating limit parameter values established for each affected source with supporting documentation and a description of the procedure used to establish the values.
(3) For each APCD that includes a fabric filter, if a bag leak detection system is used, analysis and supporting documentation demonstrating conformance with EPA guidance and specifications for bag leak detection systems in § 63.8450(e).
§ 63.8485 - What reports must I submit and when?
(a) You must submit each report in Table 9 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 9 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 § 63.8395 and ending on either June 30 or December 31. The first reporting period must be 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, 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 the dates in paragraphs (b)(1) through (4) of this section.
(c) The compliance report must contain the information in paragraphs (c)(1) through (8) 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) A description of control device maintenance performed while the control device was offline and the kiln controlled by the control device was operating, including the information specified in paragraphs (c)(4)(i) through (iii) 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 offline.
(iii) A statement of whether or not the control device maintenance was included in your approved routine control device maintenance request developed as specified in § 63.8420(d). If the control device maintenance was included in your approved routine control device maintenance request, then you must report the information in paragraphs (c)(4)(iii)(A) through (C) of this section.
(A) The total amount of time that the kiln controlled by the control device operated during the current semiannual compliance period and during the previous semiannual compliance period.
(B) The amount of time that each kiln controlled by the control device operated while the control device was offline for maintenance covered under the routine control device maintenance alternative standard during the current semiannual compliance period and during the previous semiannual compliance period.
(C) Based on the information recorded under paragraphs (c)(4)(iii)(A) and (B) of this section, compute the annual percent of kiln operating uptime during which the control device was offline for routine maintenance using Equation 7.
Where:(5) A report of the most recent burner tune-up conducted to comply with the dioxin/furan work practice standard in Table 3 to this subpart.
(6) If there are no deviations from any emission limitations (emission limits or operating limits) that apply to you, the compliance report must contain a statement that there were no deviations from the emission limitations during the reporting period.
(7) If there were no periods during which the CMS was out-of-control as specified in your OM&M plan, the compliance report must contain a statement that there were no periods during which the CMS was out-of-control during the reporting period.
(8) The first compliance report must contain the startup push rate for each kiln, the minimum APCD inlet temperature for each APCD, and the temperature profile for each kiln without an APCD.
(9) For each deviation that occurs at an affected source, report such events in the compliance report by including the information in paragraphs (c)(9)(i) through (iii) of this section.
(i) The date, time, and duration of the deviation.
(ii) A list of the affected sources or equipment for which the deviation occurred.
(iii) 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 deviation from an emission limitation (emission limit or operating limit) occurring at an affected source where you are using a CMS to comply with the emission limitations in this subpart, you must include the information in paragraphs (c)(1) through (4) and (c)(9), and paragraphs (d)(1) through (11) of this section. This includes periods of startup, shutdown, and routine control device maintenance.
(1) The total operating time of each affected source during the reporting period.
(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 pertinent information in your OM&M plan.
(4) Whether each deviation occurred during routine control device maintenance covered in your approved routine control device maintenance alternative standard or during another period, and the cause of each deviation (including unknown cause, if applicable).
(5) A description of any corrective action taken to return the affected unit to its normal or usual manner of operation.
(6) A breakdown of the total duration of the deviations during the reporting period into those that were 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 brief description of the CMS.
(10) The date of the latest CMS certification or audit.
(11) A description of any changes in CMS, processes, or control equipment since the last reporting period.
(e) If you have obtained a title V operating permit according 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 9 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 permitting authority.
(f) Within 60 calendar days after the date of completing each performance test (as defined in § 63.2) required by this subpart, you must submit the results of the performance test following the procedure specified in either paragraph (f)(1) or (f)(2) of this section.
(1) For data collected using test methods supported by the EPA's Electronic Reporting Tool (ERT) as listed on the EPA's ERT Web site (http://www.epa.gov/ttn/chief/ert/index.html) at the time of the test, you must 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) (http://cdx.epa.gov/).) Performance test data must be submitted in a file format generated through the use of the EPA's ERT or an alternate electronic file format consistent with the extensible markup language (XML) schema listed on the EPA's ERT Web site. If you claim that some of the performance test information being submitted is confidential business information (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 Web site, 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/OAPQS/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 paragraph.
(2) For data collected using test methods that are not supported by the EPA's ERT as listed on the EPA's ERT Web site at the time of the test, you must submit the results of the performance test to the Administrator at the appropriate address listed in § 63.13.
§ 63.8490 - 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) Records of performance tests as required in § 63.10(b)(2)(viii).
(3) Records relating to control device maintenance and documentation of your approved routine control device maintenance request, if you request to use the alternative standard under § 63.8420(d).
(b) You must keep the records required in Table 6 to this subpart to show continuous compliance with each emission limitation and work practice standard that applies to you.
(c) You must also maintain the records listed in paragraphs (c)(1) through (11) of this section.
(1) 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.
(2) For each deviation, record the information in paragraphs (c)(2)(i) through (iv) of this section.
(i) The date, time, and duration of the deviation.
(ii) A list of the affected sources or equipment.
(iii) 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.
(iv) Actions taken to minimize emissions in accordance with § 63.8420(b) and any corrective actions taken to return the affected unit to its normal or usual manner of operation.
(3) For each affected source, records of production rates on a fired-product basis.
(4) Records for any approved alternative monitoring or test procedures.
(5) Records of maintenance and inspections performed on the APCD.
(6) Current copies of your OM&M plan, including any revisions, with records documenting conformance.
(7) Logs of the information required in paragraphs (c)(7)(i) through (iii) of this section to document proper operation of your periodic kiln.
(i) Records of the firing time and temperature cycle for each product produced in each periodic kiln. If all periodic kilns use the same time and temperature cycles, one copy may be maintained for each kiln. Reference numbers must be assigned to use in log sheets.
(ii) For each periodic kiln, a log that details the type of product fired in each batch, the corresponding time and temperature protocol reference number, and an indication of whether the appropriate time and temperature cycle was fired.
(iii) For each periodic kiln, a log of the actual tonnage of product fired in the periodic kiln and an indication of whether the tonnage was below the maximum tonnage for that specific kiln.
(8) Logs of the maintenance procedures used to demonstrate compliance with the maintenance requirements of the periodic kiln work practice standards specified in Table 3 to this subpart.
(9) Records of burner tune-ups used to comply with the dioxin/furan work practice standard for tunnel kilns.
(10) For periods of startup and shutdown, records of the following information:
(i) The date, time, and duration of each startup and/or shutdown period, recording the periods when the affected source was subject to the standard applicable to startup and shutdown.
(ii) For periods of startup, the kiln push rate and kiln exhaust temperature prior to the time the kiln exhaust reaches the minimum APCD inlet temperature (for a kiln with an APCD) or the kiln temperature profile is attained (for a kiln with no APCD).
(iii) For periods of shutdown, the kiln push rate and kiln exhaust temperature after the time the kiln exhaust falls below the minimum APCD inlet temperature (for a kiln with an APCD) or the kiln temperature profile is no longer maintained (for a kiln with no APCD).
(11) All site-specific parameters, temperature profiles, and procedures required to be established or developed according to the applicable work practice standards in Table 3 to this subpart.
§ 63.8495 - In what form and for 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
§ 63.8505 - What parts of the General Provisions apply to me?
Table 10 to this subpart shows which parts of the General Provisions in §§ 63.1 through 63.16 apply to you.
§ 63.8510 - 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 subpart E of this part, 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 (6) of this section.
(1) Approval of alternatives to the applicability requirements in §§ 63.8385 and 63.8390, the compliance date requirements in § 63.8395, and the non-opacity emission limitations in § 63.8405.
(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.
(6) Approval of a routine control device maintenance request under § 63.8420(d).
§ 63.8515 - 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:
Air pollution control device (APCD) means any equipment that reduces the quantity of a pollutant that is emitted to the air.
Bag leak detection system means an instrument that is capable of monitoring PM 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.
Brick and structural clay products (BSCP) manufacturing facility means a plant site that manufactures brick (including, but not limited to, face brick, structural brick, and brick pavers); clay pipe; roof tile; extruded floor and wall tile; and/or other extruded, dimensional clay products. Brick and structural clay products manufacturing facilities typically process raw clay and shale, form the processed materials into bricks or shapes, and dry and fire the bricks or shapes. A plant site that manufactures refractory products, as defined in 40 CFR 63.9824, or clay ceramics, as defined in 40 CFR 63.8665, is not a BSCP manufacturing facility.
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) or work practice standard; or
(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.
Dry lime injection fabric filter (DIFF) means an APCD 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 APCD that includes continuous injection of humidified hydrated lime or other sorbent into a reaction chamber followed by a fabric filter. These systems typically include recirculation of some of the sorbent.
Dry limestone adsorber (DLA) means an APCD 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 emission limit or operating limit.
Fabric filter means an APCD used to capture PM by filtering a gas stream through filter media; also known as a baghouse.
Initial startup means:
(1) For a new or reconstructed tunnel kiln controlled with a DLA, the time at which the temperature in the kiln first reaches 260 °C (500 °F) and the kiln contains product; or
(2) for a new or reconstructed tunnel kiln controlled with a DIFF, DLS/FF, or wet scrubber (WS), the time at which the kiln first reaches a level of production that is equal to 75 percent of the kiln design capacity or 12 months after the affected source begins firing BSCP, whichever is earlier.
Fired product means brick or structural clay products that have gone through the firing process via kilns.
Kiln exhaust process stream means the portion of the exhaust from a tunnel kiln that exhausts directly to the atmosphere (or to an APCD), rather than to a sawdust dryer.
Large tunnel kiln means a tunnel kiln (existing, new, or reconstructed) with a design capacity equal to or greater than 9.07 Mg/hr (10 tph) of fired product.
Minimum APCD inlet temperature means the minimum temperature that kiln exhaust can be vented to the APCD that ensures the long-term integrity of the APCD.
Particulate matter (PM) means, for purposes of this subpart, emissions of PM that serve as a measure of total particulate emissions, as measured by Method 5 (40 CFR part 60, appendix A-3) or Method 29 (40 CFR part 60, appendix A-8), and as a surrogate for non-mercury metal HAP contained in the particulates including, but not limited to, antimony, arsenic, beryllium, cadmium, chromium, cobalt, lead, manganese, nickel, and selenium.
Periodic kiln means a batch firing kiln.
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.
Responsible official means responsible official as defined in 40 CFR 70.2.
Small tunnel kiln means a tunnel kiln (existing, new, or reconstructed) with a design capacity less than 9.07 Mg/hr (10 tph) of fired product.
Startup means the setting in operation of an affected source and starting the production process.
Startup push rate means the kiln push rate required to bring the kiln to the proper operating temperature during startup.
Tunnel kiln means any continuous kiln that is used to fire BSCP. Some tunnel kilns have two process streams, including a process stream that exhausts directly to the atmosphere or to an APCD, and a process stream in which the kiln exhaust is ducted to a sawdust dryer where it is used to dry sawdust before being emitted to the atmosphere.
Tunnel kiln design capacity means the maximum amount of brick, in Mg (tons), that a kiln is designed to produce in one year divided by the number of hours in a year (8,760 hours), taking into account the void space in the brick, the push rate for the kiln, and the stacking pattern, if applicable. If a kiln is modified to increase the capacity, the design capacity is considered to be the capacity following modifications.
Wet scrubber (WS) means an APCD that uses water, which may include caustic additives or other chemicals, as the sorbent. Wet scrubbers may use any of various design mechanisms to increase the contact between exhaust gases and the sorbent.
Work practice standard means any design, equipment, work practice, operational standard, or combination thereof, that is promulgated pursuant to section 112(h) of the Clean Air Act.
Tables to Subpart JJJJJ of Part 63
- Table 1 to Subpart JJJJJ of Part 63—Emission Limits
As stated in § 63.8405, you must meet each emission limit in the following table that applies to you:
For each . . . | You must meet the following emission limits . . . | Or you must comply with the following . . . | 1. Collection of all tunnel kilns at facility, including all process streams | HF, HCl, and Cl | Not applicable. | 2. Existing large tunnel kiln (design capacity ≥10 tons per hour (tph) of fired product), including all process streams | a. PM emissions must not exceed 0.018 kg/Mg (0.036 lb/ton) of fired product | i. PM emissions must not exceed 6.6 mg/dscm (0.0029 gr/dscf) at 17% O ii. Non-Hg HAP metals emissions must not exceed 0.0026 kg/hr (0.0057 lb/hr). | b. Hg emissions must not exceed 2.1 E-05 kilogram per megagram (kg/Mg) (4.1 E-05 pound per ton (lb/ton)) of fired product | i. Hg emissions must not exceed 7.7 micrograms per dry standard cubic meter (µg/dscm) at 17% O | ii. Hg emissions must not exceed 2.5 E-04 kg/hr (5.5 E-04 lb/hr). | 3. Existing small tunnel kiln (design capacity <10 tph of fired product), including all process streams | a. PM emissions must not exceed 0.19 kg/Mg (0.37 lb/ton) of fired product | i. PM emissions must not exceed 4.8 mg/dscm (0.0021 gr/dscf) at 17% O ii. Non-Hg HAP metals emissions must not exceed 0.047 kg/hr (0.11 lb/hr). | b. Hg emissions must not exceed 1.7 E-04 kg/Mg (3.3 E-04 lb/ton) of fired product | i. Hg emissions must not exceed 91 µg/dscm at 17% O | ii. Hg emissions must not exceed 8.5 E-04 kg/hr (0.0019 lb/hr). | 4. New or reconstructed large tunnel kiln (design capacity ≥10 tph of fired product), including all process streams | a. PM emissions must not exceed 0.0089 kg/Mg (0.018 lb/ton) of fired product. | i. PM emissions must not exceed 3.2 mg/dscm (0.0014 gr/dscf) at 17% O ii. Non-Hg HAP metals emissions must not exceed 0.0026 kg/hr (0.0057 lb/hr) of fired product. | b. Hg emissions must not exceed 1.4 E-05 kg/Mg (2.8 E-05 lb/ton) of fired product | i. Hg emissions must not exceed 6.2 µg/dscm at 17% O | ii. Hg emissions must not exceed 1.6 E-04 kg/hr (3.4 E-04 lb/hr). | 5. New or reconstructed small tunnel kiln (design capacity <10 tph of fired product), including all process streams | a. PM emissions must not exceed 0.015 kg/Mg (0.030 lb/ton) of fired product | i. PM emissions must not exceed 4.7 mg/dscm (0.0021 gr/dscf) at 17% O ii. Non-Hg HAP metals emissions must not exceed 0.047 kg/hr (0.11 lb/hr) of fired product. | b. Hg emissions must not exceed 1.7 E-04 kg/Mg (3.3 E-04 lb/ton) of fired product | i. Hg emissions must not exceed 91 µg/dscm at 17% O | ii. Hg emissions must not exceed 8.5 E-04 kg/hr (0.0019 lb/hr). |
---|
- Table 2 to Subpart JJJJJ of Part 63—Operating Limits
As stated in § 63.8405, you must meet each operating limit in the following table that applies to you:
For each . . . | You must . . . | 1. Tunnel kiln equipped with a DLA | a. Maintain the average pressure drop across the DLA for each 3-hour block period at or above the average pressure drop established during the HF/HCl/Cl | b. Maintain an adequate amount of limestone in the limestone hopper, storage bin (located at the top of the DLA), and DLA at all times; maintain the limestone feeder setting (on a per ton of fired product basis) at or above the level established during the HF/HCl/Cl | c. Use the same grade of limestone from the same source as was used during the HF/HCl/Cl | d. Maintain no VE from the DLA stack. | 2. Tunnel kiln equipped with a DIFF or DLS/FF | a. If you use a bag leak detection system, initiate corrective action within 1 hour of a bag leak detection system alarm and complete corrective actions in accordance with your OM&M plan; operate and maintain the fabric filter such that the alarm is not engaged for more than 5 percent of the total operating time in a 6-month block reporting period; or maintain no VE from the DIFF or DLS/FF stack; and | b. Maintain free-flowing lime in the feed hopper or silo and to the APCD at all times for continuous injection systems; maintain the feeder setting (on a per ton of fired product basis) at or above the level established during the HF/HCl/Cl | 3. Tunnel kiln equipped with a WS | a. Maintain the average scrubber liquid pH for each 3-hour block period at or above the average scrubber liquid pH established during the HF/HCl/Cl | b. Maintain the average scrubber liquid flow rate for each 3-hour block period at or above the highest average scrubber liquid flow rate established during the HF/HCl/Cl | 4. Tunnel kiln equipped with an ACI system | 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 demonstrated. | 5. Tunnel kiln with no add-on control | a. Maintain no VE from the stack.
b. Maintain the kiln process rate at or below the kiln process rate determined according to § 63.8445(g)(1). |
---|
- Table 3 to Subpart JJJJJ of Part 63—Work Practice Standards
As stated in § 63.8405, you must meet each work practice standard in the following table that applies to you:
For each . . . | You must . . . | According to the following requirements . . . | 1. Existing, new or reconstructed periodic kiln | a. Minimize HAP emissions | i. Develop and use a designed firing time and temperature cycle for each periodic kiln. You must either program the time and temperature cycle into your kiln or track each step on a log sheet; and | ii. Label each periodic kiln with the maximum load (in tons) of product that can be fired in the kiln during a single firing cycle; and | iii. For each firing load, document the total tonnage of product placed in the kiln to ensure that it is not greater than the maximum load identified in item 1b; and | iv. Develop and follow maintenance procedures for each kiln that, at a minimum, specify the frequency of inspection and maintenance of temperature monitoring devices, controls that regulate air-to-fuel ratios, and controls that regulate firing cycles; and | v. Develop and maintain records for each periodic kiln, as specified in § 63.8490. | 2. Existing, new or reconstructed tunnel kiln | a. Minimize dioxin/furan emissions | i. Maintain and inspect the burners and associated combustion controls (as applicable); and | ii. Tune the specific burner type to optimize combustion. | 3. Existing, new or reconstructed tunnel kiln during periods of startup | a. Minimize HAP emissions | i. Establish the startup push rate for each kiln, the minimum APCD inlet temperature for each APCD, and temperature profile for each kiln without an APCD and include them in your first compliance report, as specified in § 63.8485(c)(8); and | ii. After initial charging of the kiln with loaded kiln cars, remain at or below the startup push rate for the kiln until the kiln exhaust reaches the minimum APCD inlet temperature for a kiln with an APCD or until the kiln temperature profile is attained for a kiln with no APCD; and | iii. If your kiln has an APCD, begin venting the exhaust from the kiln through the APCD by the time the kiln exhaust temperature reaches the minimum APCD inlet temperature. | 4. Existing, new or reconstructed tunnel kiln during periods of shutdown | a. Minimize HAP emissions | i. Do not push loaded kiln cars into the kiln once the kiln exhaust temperature falls below the minimum APCD inlet temperature if the kiln is controlled by an APCD or when the kiln temperature profile is no longer maintained for an uncontrolled kiln; and | ii. If your kiln has an APCD, continue to vent the exhaust from the kiln through the APCD until the kiln exhaust temperature falls below the minimum inlet temperature for the APCD. | 5. Existing, new or reconstructed tunnel kiln during periods of routine control device maintenance | a. Minimize HAP emissions. | i. Develop and use a temperature profile for each kiln; and
ii. Develop and follow maintenance procedures for each kiln that, at a minimum, specify the frequency of inspection and maintenance of temperature monitoring devices and controls that regulate air-to-fuel ratios; and | iii. Develop and maintain records for each kiln, as specified in § 63.8490(a)(3). |
---|
As stated in § 63.8445, you must conduct each performance test in the following table that applies to you:
- Table 4 to Subpart JJJJJ of Part 63—Requirements for Performance Tests
As stated in § 63.8445, you must conduct each performance test in the following table that applies to you:
For each . . . | You must . . . | Using . . . | According to the following requirements . . . | 1. Tunnel kiln | a. Select locations of sampling ports and the number of traverse points | Method 1 or 1A of 40 CFR part 60, appendix A-1 | Sampling sites must be located at the outlet of the APCD and prior to any releases to the atmosphere for all affected sources. | b. Determine velocities and volumetric flow rate | Method 2 of 40 CFR part 60, appendix A-1 | You may use Method 2A, 2C, 2D, or 2F of 40 CFR part 60, appendix A-1, or Method 2G of 40 CFR part 60, appendix A-2, as appropriate, as an alternative to using Method 2 of 40 CFR part 60, appendix A-1. | c. Conduct gas molecular weight analysis | Method 3 of 40 CFR part 60, appendix A-2 | You may use Method 3A or 3B of 40 CFR part 60, appendix A-2, as appropriate, as an alternative to using Method 3 of 40 CFR part 60, appendix A-2. ANSI/ASME PTC 19.10-1981 (incorporated by reference, see § 63.14) may be used as an alternative to the manual procedures (but not the instrumental procedures) in Methods 3A and 3B. | d. Measure moisture content of the stack gas | Method 4 of 40 CFR part 60, appendix A-3 | e. Measure HF, HCl and Cl | i. Method 26A of 40 CFR part 60, appendix A-8; or | You may use Method 26 of 40 CFR part 60, appendix A-8, as an alternative to using Method 26A of 40 CFR part 60, appendix A-8, when no acid PM ( | ii. Method 320 of appendix A of this part | When using Method 320 of appendix A of this part, you must follow the analyte spiking procedures of section 13 of Method 320 of appendix A of this part, unless you can demonstrate that the complete spiking procedure has been conducted at a similar source. ASTM D6348-03 (Reapproved 2010) (incorporated by reference, see § 63.14) may be used as an alternative to 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. | f. Measure PM emissions or non-Hg HAP metals | i. For PM only: Method 5 of 40 CFR part 60, appendix A-3; or | ii. For PM or non-Hg HAP metals: Method 29 of 40 CFR part 60, appendix A-8 | g. Measure Hg emissions | Method 29 of 40 CFR part 60, appendix A-8 | ASTM D6784-02 (Reapproved 2008) (incorporated by reference, see § 63.14) may be used as an alternative to Method 29 (portion for Hg only). | 2. Tunnel kiln with no add-on control | Establish the operating limit(s) for kiln process rate if the total facility maximum potential HCl-equivalent emissions are greater than the HCl-equivalent limit in Table 1 to this subpart | HCl-equivalent limit in Table 1 to this subpart and emissions and production data from the HF/HCl/Cl | Using the procedures in § 63.8445(g)(1), you must determine the maximum process rate(s) for your kiln(s) that would ensure total facility maximum potential HCl-equivalent emissions remain at or below the HCl-equivalent limit in Table 1 to this subpart. The maximum process rate(s) would become your site-specific process rate operating limit(s). | 3. Tunnel kiln that is complying with PM and/or Hg production-based emission limits | Determine the production rate during each PM/Hg test run in order to determine compliance with PM and/or Hg production-based emission limits | Production data collected during the PM/Hg performance tests ( | You must measure and record the production rate, on a fired-product basis, of the affected source for each of the three test runs. | 4. Tunnel kiln equipped with a DLA | a. Establish the operating limit for the average pressure drop across the DLA | Data from the pressure drop measurement device during the HF/HCl/Cl | You must continuously measure the pressure drop across the DLA, determine and record the block average pressure drop values for the three test runs, and determine and record the 3-hour block average of the recorded pressure drop measurements for the three test runs. The average of the three test runs establishes your minimum site-specific pressure drop operating limit. | b. Establish the operating limit for the limestone feeder setting | Data from the limestone feeder during the HF/HCl/Cl | You must ensure that you maintain an adequate amount of limestone in the limestone hopper, storage bin (located at the top of the DLA), and DLA at all times during the performance test. You must establish your limestone feeder setting, on a per ton of fired product basis, one week prior to the performance test and maintain the feeder setting for the one-week period that precedes the performance test and during the performance test. | c. Document the source and grade of limestone used | Records of limestone purchase | 5. Tunnel kiln equipped with a DIFF or DLS/FF | Establish the operating limit for the lime feeder setting | Data from the lime feeder during the HF/HCl/Cl | For continuous lime injection systems, you must ensure that lime in the feed hopper or silo and to the APCD is free-flowing at all times during the performance test and record the feeder setting, on a per ton of fired product basis, for the three test runs. If the feed rate setting varies during the three test runs, determine and record the average feed rate from the three test runs. The average of the three test runs establishes your minimum site-specific feed rate operating limit. | 6. Tunnel kiln equipped with a WS | a. Establish the operating limit for the average scrubber liquid pH | Data from the pH measurement device during the performance HF/HCl/Cl | You must continuously measure the scrubber liquid pH, determine and record the block average pH values for the three test runs, and determine and record the 3-hour block average of the recorded pH measurements for the three test runs. The average of the three test runs establishes your minimum site-specific liquid pH operating limit. | b. Establish the operating limit for the average scrubber liquid flow rate | Data from the flow rate measurement device during the HF/HCl/Cl | You must continuously measure the scrubber liquid flow rate, determine and record the block average flow rate values for the three test runs, and determine and record the 3-hour block average of the recorded flow rate measurements for the three test runs. The average of the three test runs establishes your minimum site-specific liquid flow rate operating level. If different average wet scrubber liquid flow rate values are measured during the HF/HCl/Cl | 7. Tunnel kiln equipped with an ACI system | Establish the operating limit for the average carbon flow rate | Data from the carbon flow rate measurement conducted during the Hg performance test | You 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. |
---|
- Table 5 to Subpart JJJJJ of Part 63—Initial Compliance With Emission Limitations and Work Practice Standards
As stated in § 63.8455, you must demonstrate initial compliance with each emission limitation and work practice standard that applies to you according to the following table:
For each . . . | For the following . . . | You have demonstrated initial compliance
if . . . | 1. Collection of all tunnel kilns at the facility, including all process streams | a. HF, HCl, and Cl | i. You measure HF, HCl, and Cl | ii. You calculate the HCl-equivalent emissions for each kiln using Equation 2 to this subpart; and | iii. You sum the HCl-equivalent values for all kilns at the facility using Equation 3 to this subpart; and | iv. The facility total HCl-equivalent does not exceed 26 kg/hr (57 lb/hr). | 2. Existing large tunnel kiln (design capacity ≥10 tph of fired product), including all process streams | a. PM emissions must not exceed 0.018 kg/Mg (0.036 lb/ton) of fired product or 6.6 mg/dscm (0.0029 gr/dscf) at 17% O | i. The PM emissions measured using Method 5 of 40 CFR part 60, appendix A-3 or Method 29 of 40 CFR part 60, appendix A-8, over the period of the initial performance test, according to the calculations in § 63.8445(f)(1), do not exceed 0.018 kg/Mg (0.036 lb/ton) of fired product or 6.6 mg/dscm (0.0029 gr/dscf) at 17% O | ii. You establish and have a record of the applicable operating limits listed in Table 2 to this subpart over the 3-hour performance test during which PM emissions did not exceed 0.018 kg/Mg (0.036 lb/ton) of fired product or 6.6 mg/dscm (0.0029 gr/dscf) at 17% O | b. Non-Hg HAP metals emissions must not exceed 0.0026 kg/hr (0.0057 lb/hr) | i. The non-Hg HAP metals emissions measured using Method 29 of 40 CFR part 60, appendix A-8, over the period of the initial performance test, do not exceed 0.0026 kg/hr (0.0057 lb/hr); and | ii. You establish and have a record of the applicable operating limits listed in Table 2 to this subpart over the 3-hour performance test during which non-Hg HAP metals emissions did not exceed 0.0026 kg/hr (0.0057 lb/hr). | c. Hg emissions must not exceed 2.1 E-05 kg/Mg (4.1 E-05 lb/ton) of fired product or 7.7 µg/dscm at 17% O | i. The Hg emissions measured using Method 29 of 40 CFR part 60, appendix A-8 or its alternative, ASTM D6784-02 (Reapproved 2008) (incorporated by reference, see § 63.14), over the period of the initial performance test, do not exceed 2.1 E-05 kg/Mg (4.1 E-05 lb/ton) of fired product or 7.7 µg/dscm at 17% O | ii. You establish and have a record of the applicable operating limits listed in Table 2 to this subpart over the 3-hour performance test during which Hg emissions did not exceed 2.1 E-05 kg/Mg (4.1 E-05 lb/ton) of fired product or 7.7 µg/dscm at 17% O | 3. Existing small tunnel kiln (design capacity <10 tph of fired product), including all process streams | a. PM emissions must not exceed 0.19 kg/Mg (0.37 lb/ton) of fired product or 4.8 mg/dscm (0.0021 gr/dscf) at 17% O | i. The PM emissions measured using Method 5 of 40 CFR part 60, appendix A-3 or Method 29 of 40 CFR part 60, appendix A-8, over the period of the initial performance test, according to the calculations in § 63.8445(f)(1), do not exceed 0.19 kg/Mg (0.37 lb/ton) of fired product or 4.8 mg/dscm (0.0021 gr/dscf) at 17% O | ii. You establish and have a record of the applicable operating limits listed in Table 2 to this subpart over the 3-hour performance test during which PM emissions did not exceed 0.19 kg/Mg (0.37 lb/ton) of fired product or 4.8 mg/dscm (0.0021 gr/dscf) at 17% O | b. Non-Hg HAP metals emissions must not exceed 0.047 kg/hr (0.11 lb/hr) | i. The non-Hg HAP metals emissions measured using Method 29 of 40 CFR part 60, appendix A-8, over the period of the initial performance test, do not exceed 0.047 kg/hr (0.11 lb/hr); and | ii. You establish and have a record of the applicable operating limits listed in Table 2 to this subpart over the 3-hour performance test during which non-Hg HAP metals emissions did not exceed 0.047 kg/hr (0.11 lb/hr). | c. Hg emissions must not exceed 1.7 E-04 kg/Mg (3.3 E-04 lb/ton) of fired product or 91 µg/dscm at 17% O | i. The Hg emissions measured using Method 29 of 40 CFR part 60, appendix A-8 or its alternative, ASTM D6784-02 (Reapproved 2008) (incorporated by reference, see § 63.14), over the period of the initial performance test, do not exceed 1.7 E-04 kg/Mg (3.3 E-04 lb/ton) of fired product or 91 µg/dscm at 17% O | ii. You establish and have a record of the applicable operating limits listed in Table 2 to this subpart over the 3-hour performance test during which Hg emissions did not exceed 1.7 E-04 kg/Mg (3.3 E-04 lb/ton) of fired product or 91 µg/dscm at 17% O | 4. New or reconstructed large tunnel kiln (design capacity ≥10 tph of fired product), including all process streams | a. PM emissions must not exceed 0.0089 kg/Mg (0.018 lb/ton) of fired product or 3.2 mg/dscm (0.0014 gr/dscf) at 17% O | i. The PM emissions measured using Method 5 of 40 CFR part 60, appendix A-3, over the period of the initial performance test, according to the calculations in § 63.8445(f)(1), do not exceed 0.0089 kg/Mg (0.018 lb/ton) of fired product or 3.2 mg/dscm (0.0014 gr/dscf) at 17% O | ii. You establish and have a record of the applicable operating limits listed in Table 2 to this subpart over the 3-hour performance test during which PM emissions did not exceed 0.0089 kg/Mg (0.018 lb/ton) of fired product or 3.2 mg/dscm (0.0014 gr/dscf) at 17% O | b. Non-Hg HAP metals emissions must not exceed 0.0026 kg/hr (0.0057 lb/hr) | i. The non-Hg HAP metals emissions measured using Method 29 of 40 CFR part 60, appendix A-8, over the period of the initial performance test, do not exceed 0.0026 kg/hr (0.0057 lb/hr); and | ii. You establish and have a record of the applicable operating limits listed in Table 2 to this subpart over the 3-hour performance test during which non-Hg HAP metals emissions did not exceed 0.0026 kg/hr (0.0057 lb/hr). | c. Hg emissions must not exceed 1.4 E-05 kg/Mg (2.8 E-05 lb/ton) of fired product or 6.2 µg/dscm at 17% O | i. The Hg emissions measured using Method 29 of 40 CFR part 60, appendix A-8 or its alternative, ASTM D6784-02 (Reapproved 2008) (incorporated by reference, see § 63.14), over the period of the initial performance test, do not exceed 1.4 E-05 kg/Mg (2.8 E-05 lb/ton) of fired product or 6.2 µg/dscm at 17% O | ii. You establish and have a record of the applicable operating limits listed in Table 2 to this subpart over the 3-hour performance test during which Hg emissions did not exceed 1.4 E-05 kg/Mg (2.8 E-05 lb/ton) of fired product or 6.2 µg/dscm at 17% O | 5. New or reconstructed small tunnel kiln (design capacity <10 tph of fired product), including all process streams | a. PM emissions must not exceed 0.015 kg/Mg (0.030 lb/ton) of fired product or 4.7 mg/dscm (0.0021 gr/dscf) at 17% O | i. The PM emissions measured using Method 5 of 40 CFR part 60, appendix A-3, over the period of the initial performance test, according to the calculations in § 63.8445(f)(1), do not exceed 0.015 kg/Mg (0.030 lb/ton) of fired product or 4.7 mg/dscm (0.0021 gr/dscf) at 17% O | ii. You establish and have a record of the applicable operating limits listed in Table 2 to this subpart over the 3-hour performance test during which PM emissions did not exceed 0.015 kg/Mg (0.030 lb/ton) of fired product or 4.7 mg/dscm (0.0021 gr/dscf) at 17% O | b. Non-Hg HAP metals emissions must not exceed 0.047 kg/hr (0.11 lb/hr) | i. The non-Hg HAP metals emissions measured using Method 29 of 40 CFR part 60, appendix A-8, over the period of the initial performance test, do not exceed 0.047 kg/hr (0.11 lb/hr); and | ii. You establish and have a record of the applicable operating limits listed in Table 2 to this subpart over the 3-hour performance test during which non-Hg HAP metals emissions did not exceed 0.047 kg/hr (0.11 lb/hr). | c. Hg emissions must not exceed 1.7 E-04 kg/Mg (3.3 E-04 lb/ton) of fired product or 91 µg/dscm at 17% O | i. The Hg emissions measured using Method 29 of 40 CFR part 60, appendix A-8 or its alternative, ASTM D6784-02 (Reapproved 2008) (incorporated by reference, see § 63.14), over the period of the initial performance test, do not exceed 1.7 E-04 kg/Mg (3.3 E-04 lb/ton) of fired product or 91 µg/dscm at 17% O | ii. You establish and have a record of the applicable operating limits listed in Table 2 to this subpart over the 3-hour performance test during which Hg emissions did not exceed 1.7 E-04 kg/Mg (3.3 E-04 lb/ton) of fired product or 91 µg/dscm at 17% O | 6. Existing, new or reconstructed periodic kiln | a. Minimize HAP emissions | i. Develop a designed firing time and temperature cycle for each periodic kiln. You must either program the time and temperature cycle into your kiln or track each step on a log sheet; and | ii. Label each periodic kiln with the maximum load (in tons) of product that can be fired in the kiln during a single firing cycle; and | iii. Develop maintenance procedures for each kiln that, at a minimum, specify the frequency of inspection and maintenance of temperature monitoring devices, controls that regulate air-to-fuel ratios, and controls that regulate firing cycles. | 7. Existing, new or reconstructed tunnel kiln | a. Minimize dioxin/furan emissions | i. Conduct initial inspection of the burners and associated combustion controls (as applicable); and | ii. Tune the specific burner type to optimize combustion. |
---|
- Table 6 to Subpart JJJJJ of Part 63—Continuous Compliance With Emission Limitations and Work Practice Standards
As stated in § 63.8470, you must demonstrate continuous compliance with each emission limitation and work practice standard that applies to you according to the following table:
For each . . . | For the following . . . | You must demonstrate continuous compliance by . . . | 1. Tunnel kiln equipped with a DLA | a. Each emission limit in Table 1 to this subpart and each operating limit in Item 1 of Table 2 to this subpart for tunnel kilns equipped with a DLA | i. Collecting the DLA pressure drop data according to § 63.8450(a); reducing the DLA pressure drop data to 3-hour block averages according to § 63.8450(a); maintaining the average pressure drop across the DLA for each 3-hour block period at or above the average pressure drop established during the HF/HCl/Cl | ii. Verifying that the limestone hopper and storage bin (located at the top of the DLA) contain adequate limestone by performing a daily visual check, which could include one of the following: (1) Conducting a physical check of the hopper; (2) creating a visual access point, such as a window, on the side of the hopper; (3) installing a camera in the hopper that provides continuous feed to a video monitor in the control room; or (4) confirming that load level indicators in the hopper are not indicating the need for additional limestone; and | iii. Recording the limestone feeder setting daily (on a per ton of fired product basis) to verify that the feeder setting is being maintained at or above the level established during the HF/HCl/Cl | iv. Using the same grade of limestone from the same source as was used during the HF/HCl/Cl | v. Performing VE observations of the DLA stack at the frequency specified in § 63.8470(e) using Method 22 of 40 CFR part 60, appendix A-7; maintaining no VE from the DLA stack. | 2. Tunnel kiln equipped with a DIFF or DLS/FF | a. Each emission limit in Table 1 to this subpart and each operating limit in Item 2 of Table 2 to this subpart for tunnel kilns equipped with DIFF or DLS/FF | i. If you use a bag leak detection system, as prescribed in 63.8450(e), initiating corrective action within 1 hour of a bag leak detection system alarm and completing corrective actions in accordance with your OM&M plan; operating and maintaining the fabric filter such that the alarm is not engaged 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 is counted as a minimum of 1 hour; if you take longer than 1 hour to initiate corrective action, the alarm time is counted as the actual amount of time taken by you to initiate corrective action; or performing VE observations of the DIFF or DLS/FF stack at the frequency specified in § 63.8470(e) using Method 22 of 40 CFR part 60, appendix A-7; and maintaining no VE from the DIFF or DLS/FF stack; and | ii. Verifying 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 in accordance with your OM&M plan; recording the feeder setting once during each shift of operation to verify that the feeder setting is being maintained at or above the level established during the HF/HCl/Cl | 3. Tunnel kiln equipped with a WS | a. Each emission limit in Table 1 to this subpart and each operating limit in Item 3 of Table 2 to this subpart for tunnel kilns equipped with WS | i. Collecting the scrubber liquid pH data according to § 63.8450(a); reducing the scrubber liquid pH data to 3-hour block averages according to § 63.8450(a); maintaining the average scrubber liquid pH for each 3-hour block period at or above the average scrubber liquid pH established during the HF/HCl/Cl | ii. Collecting the scrubber liquid flow rate data according to § 63.8450(a); reducing the scrubber liquid flow rate data to 3-hour block averages according to § 63.8450(a); maintaining the average scrubber liquid flow rate for each 3-hour block period at or above the highest average scrubber liquid flow rate established during the HF/HCl/Cl | 4. Tunnel kiln equipped with an ACI system | Each emission limit in Table 1 to this subpart and each operating limit in Item 4 of Table 2 to this subpart for tunnel kilns equipped with ACI system | Collecting the carbon flow rate data according to § 63.8450(a); reducing the carbon flow rate data to 3-hour block averages according to § 63.8450(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. | 5. Tunnel kiln with no add-on control | a. Each emission limit in Table 1 to this subpart and each operating limit in Item 5 of Table 2 to this subpart for tunnel kilns with no add-on control | i. Performing VE observations of the stack at the frequency specified in § 63.8470(e) using Method 22 of 40 CFR part 60, appendix A-7; and maintaining no VE from the stack. | ii. If your last calculated total facility maximum potential HCl-equivalent was not at or below the health-based standard in Table 1 to this subpart, collecting the kiln process rate data according to § 63.8450(a); reducing the kiln process rate data to 3-hour block averages according to § 63.8450(a); maintaining the average kiln process rate for each 3-hour block period at or below the kiln process rate determined according to § 63.8445(g)(1). | 6. Periodic kiln | a. Minimize HAP emissions | i. Using a designed firing time and temperature cycle for each periodic kiln; and | ii. For each firing load, documenting the total tonnage of product placed in the kiln to ensure that it is not greater than the maximum load identified in Item 1.a.ii of Table 3 to this subpart; and | iii. Following maintenance procedures for each kiln that, at a minimum, specify the frequency of inspection and maintenance of temperature monitoring devices, controls that regulate air-to-fuel ratios, and controls that regulate firing cycles; and | iv. Developing and maintaining records for each periodic kiln, as specified in § 63.8490. | 7. Tunnel kiln | a. Minimize dioxin/furan emissions | i. Maintaining and inspecting the burners and associated combustion controls (as applicable) and tuning the specific burner type to optimize combustion no later than 36 calendar months after the previous tune-up; and | ii. Maintaining records of burner tune-ups used to demonstrate compliance with the dioxin/furan work practice standard; and | iii. Submitting a report of most recent tune-up conducted with compliance report. |
---|
- Table 7 to Subpart JJJJJ of Part 63—Compliance Dates
As stated in § 63.8395, you must meet each compliance date in the following table that applies to you:
If you have a(n) . . . | Then you must . . . | No later than . . . | 1. New or reconstructed affected source and the initial startup of your affected source is after December 18, 2014, but before December 28, 2015 | Comply with the applicable emission limitations and work practice standards in Tables 1, 2, and 3 to this subpart | December 28, 2015. | 2. New or reconstructed affected source and the initial startup of your affected source is after December 28, 2015 | Comply with the applicable emission limitations and work practice standards in Tables 1, 2, and 3 to this subpart | Initial startup of your affected source. | 3. Existing affected source | Comply with the applicable emission limitations and work practice standards in Tables 1, 2, and 3 to this subpart | December 26, 2018. | 4. Existing area source that increases its emissions or its potential to emit such that it becomes a major source of HAP by adding a new affected source or by reconstructing | Be in compliance with this subpart | Initial startup of your affected source as a major source. | 5. New area source ( | Be in compliance with this subpart | Initial startup of your affected source as a major source. |
---|
- Table 8 to Subpart JJJJJ of Part 63—Deadlines for Submitting Notifications
As stated in § 63.8480, you must submit each notification that applies to you according to the following table:
If you . . . | You must . . . | No later than . . . | As specified in . . . | 1. Start up your affected source before December 28, 2015 | Submit an Initial Notification | June 22, 2016, or no later than 120 days after the source becomes subject to this subpart, whichever is later | § 63.9(b)(2). | 2. Start up your new or reconstructed affected source on or after December 28, 2015 | Submit an Initial Notification | 120 calendar days after you become subject to this subpart | § 63.9(b)(2). | 3. Are required to conduct a performance test | Submit a notification of intent to conduct a performance test | 60 calendar days before the performance test is scheduled to begin | § 63.7(b)(1). | 4. Are required to conduct a compliance demonstration that includes a performance test according to the requirements in Table 4 to this subpart | Submit a Notification of Compliance Status, including the performance test results | 60 calendar days following the completion of the performance test, by the close of business | § 63.9(h) and § 63.10(d)(2). | 5. Are required to conduct a compliance demonstration required in Table 5 to this subpart that does not include a performance test ( | Submit a Notification of Compliance Status | 30 calendar days following the completion of the compliance demonstrations, by the close of business | § 63.9(h). | 6. Request to use the routine control device maintenance alternative standard according to § 63.8420(d) | Submit your request | 120 calendar days before the compliance date specified in § 63.8395 |
---|
- Table 9 to Subpart JJJJJ of Part 63—Requirements for Reports
As stated in § 63.8485, you must submit each report that applies to you according to the following table:
You must submit . . . | The report must contain . . . | You must submit the report . . . | 1. A compliance report. | a. If there are no deviations from any emission limitations (emission limits, operating limits) that apply to you, a statement that there were no deviations from the emission limitations during the reporting period. If there were no periods during which the CMS was out-of-control as specified in your OM&M plan, a statement that there were no periods during which the CMS was out-of-control during the reporting period | Semiannually according to the requirements in § 63.8485(b). | b. If you have a deviation from any emission limitation (emission limit, operating limit) during the reporting period, the report must contain the information in § 63.8485(c)(9). If there were periods during which the CMS was out-of-control, as specified in your OM&M plan, the report must contain the information in § 63.8485(d) | Semiannually according to the requirements in § 63.8485(b). |
---|
- Table 10 to Subpart JJJJJ of Part 63—Applicability of General Provisions to Subpart JJJJJ
As stated in § 63.8505, you must comply with the General Provisions in §§ 63.1 through 63.16 that apply to you according to the following table:
Citation | Subject | Brief description | Applies to subpart JJJJJ? | § 63.1 | Applicability | Initial applicability determination; applicability after standard established; permit requirements; extensions, notifications | Yes. | § 63.2 | Definitions | Definitions for part 63 standards | Yes. | § 63.3 | Units and Abbreviations | Units and abbreviations for part 63 standards | Yes. | § 63.4 | Prohibited Activities | Compliance date; circumvention; severability | Yes. | § 63.5 | Construction/Reconstruction | Applicability; applications; approvals | Yes. | § 63.6(a) | Applicability | General Provisions (GP) apply unless compliance extension; GP apply to area sources that become major | Yes. | § 63.6(b)(1)-(4) | Compliance Dates for New and Reconstructed sources | Standards 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) | Notification | Must notify if commenced construction or reconstruction after proposal | Yes. | § 63.6(b)(6) | [Reserved] | No. | § 63.6(b)(7) | Compliance Dates for New and Reconstructed Area Sources That Become Major | Area sources that become major must comply with major source standards immediately upon becoming major, regardless of whether required to comply when they were area sources | Yes. | § 63.6(c)(1)-(2) | Compliance Dates for Existing Sources | Comply according to date in subpart, which must be no later than 3 years after effective date; for section 112(f) standards, comply within 90 calendar days of effective date unless compliance extension | Yes. | § 63.6(c)(3)-(4) | [Reserved] | No. | § 63.6(c)(5) | Compliance Dates for Existing Area Sources That Become Major | Area 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] | No. | § 63.6(e)(1)(i) | Operation & Maintenance | General Duty to minimize emissions | No. See § 63.8420(b) for general duty requirement. | § 63.6(e)(1)(ii) | Operation & Maintenance | Requirement to correct malfunctions ASAP | No. | § 63.6(e)(1)(iii) | Operation & Maintenance | Operation and maintenance requirements enforceable independent of emissions limitations | Yes. | § 63.6(e)(2) | [Reserved] | No. | § 63.6(e)(3) | Startup, Shutdown, and Malfunction Plan (SSMP) | Requirement for startup, shutdown, and malfunction (SSM) and SSMP; content of SSMP | No. | § 63.6(f)(1) | Compliance Except During SSM | You must comply with emission standards at all times except during SSM | No. | § 63.6(f)(2)-(3) | Methods for Determining Compliance | Compliance based on performance test, operation and maintenance plans, records, inspection | Yes. | § 63.6(g) | Alternative Standard | Procedures for getting an alternative standard | Yes. | § 63.6(h) | Opacity/VE Standards | Requirements for opacity and VE standards | No, not applicable. | § 63.6(i) | Compliance Extension | Procedures and criteria for Administrator to grant compliance extension | Yes. | § 63.6(j) | Presidential Compliance Exemption | President may exempt source category | Yes. | § 63.7(a)(1)-(2) | Performance Test Dates | Dates for conducting initial performance testing and other compliance demonstrations for emission limits and work practice standards; must conduct 180 calendar days after first subject to rule | Yes. | § 63.7(a)(3) | Section 114 Authority | Administrator may require a performance test under CAA section 114 at any time | Yes. | § 63.7(a)(4) | Notification of Delay in Performance Testing Due To Force Majeure | Must notify Administrator of delay in performance testing due to force majeure | Yes. | § 63.7(b)(1) | Notification of Performance Test | Must notify Administrator 60 calendar days before the test | Yes. | § 63.7(b)(2) | Notification of Rescheduling | Must notify Administrator 5 calendar days before scheduled date of rescheduled date | Yes. | § 63.7(c) | Quality Assurance(QA)/Test Plan | Requirements; test plan approval procedures; performance audit requirements; internal and external QA procedures for testing | Yes. | § 63.7(d) | Testing Facilities | Requirements for testing facilities | Yes. | § 63.7(e)(1) | Conditions for Conducting Performance Tests | Cannot conduct performance tests during SSM; not a violation to exceed standard during SSM | No, § 63.8445 specifies requirements. | § 63.7(e)(2)-(3) | Conditions for Conducting Performance Tests | Must conduct according to subpart and EPA test methods unless Administrator approves alternative; must have at least 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 used | Yes. | § 63.7(e)(4) | Testing under Section 114 | Administrator's authority to require testing under section 114 of the Act | Yes. | § 63.7(f) | Alternative Test Method | Procedures by which Administrator can grant approval to use an alternative test method | Yes. | § 63.7(g) | Performance Test Data Analysis | Must include raw data in performance test report; must submit performance test data 60 calendar days after end of test with the notification of compliance status | Yes. | § 63.7(h) | Waiver of Tests | Procedures for Administrator to waive performance test | Yes. | § 63.8(a)(1) | Applicability of Monitoring Requirements | Subject to all monitoring requirements in subpart | Yes. | § 63.8(a)(2) | Performance Specifications | Performance Specifications in appendix B of 40 CFR part 60 apply | Yes. | § 63.8(a)(3) | [Reserved] | No. | § 63.8(a)(4) | Monitoring with Flares | Requirements for flares in § 63.11 apply | No, not applicable. | § 63.8(b)(1) | Monitoring | Must conduct monitoring according to standard unless Administrator approves alternative | Yes. | § 63.8(b)(2)-(3) | Multiple Effluents and Multiple Monitoring Systems | Specific requirements for installing and reporting on monitoring systems | Yes. | § 63.8(c)(1) | Monitoring System Operation and Maintenance | Maintenance consistent with good air pollution control practices | Yes. | § 63.8(c)(1)(i) | Routine and Predictable SSM | Reporting requirements for SSM when action is described in SSMP | No. | § 63.8(c)(1)(ii) | SSM not in SSMP | Reporting requirements for SSM when action is not described in SSMP | Yes. | § 63.8(c)(1)(iii) | Compliance with Operation and Maintenance Requirements | How Administrator determines if source complying with operation and maintenance requirements | No. | § 63.8(c)(2)-(3) | Monitoring System Installation | Must install to get representative emission and parameter measurements | Yes. | § 63.8(c)(4) | CMS Requirements | Requirements for CMS | No, § 63.8450 specifies requirements. | § 63.8(c)(5) | Continuous Opacity Monitoring System (COMS) Minimum Procedures | COMS minimum procedures | No, not applicable. | § 63.8(c)(6) | CMS Requirements | Zero and high level calibration check requirements | Yes. | § 63.8(c)(7)-(8) | CMS Requirements | Out-of-control periods | Yes. | § 63.8(d)(1) and (2) | CMS Quality Control | Requirements for CMS quality control | Yes. | § 63.8(d)(3) | CMS Quality Control | Written procedures for CMS | No, § 63.8425(b)(9) specifies requirements | § 63.8(e) | CMS Performance Evaluation | Requirements for CMS performance evaluation | Yes. | § 63.8(f)(1)-(5) | Alternative Monitoring Method | Procedures for Administrator to approve alternative monitoring | Yes. | § 63.8(f)(6) | Alternative to Relative Accuracy Test | Procedures for Administrator to approve alternative relative accuracy test for continuous emissions monitoring systems (CEMS) | No, not applicable. | § 63.8(g) | Data Reduction | COMS and CEMS data reduction requirements | No, not applicable. | § 63.9(a) | Notification Requirements | Applicability; State delegation | Yes. | § 63.9(b) | Initial Notifications | Requirements for initial notifications | § 63.9(c) | Request for Compliance Extension | Can request if cannot comply by date or if installed BACT/LAER | Yes. | § 63.9(d) | Notification of Special Compliance Requirements for New Source | For sources that commence construction between proposal and promulgation and want to comply 3 years after effective date | Yes. | § 63.9(e) | Notification of Performance Test | Notify Administrator 60 calendar days prior | Yes. | § 63.9(f) | Notification of VE/Opacity Test | Notify Administrator 30 calendar days prior | No, not applicable. | § 63.9(g)(1) | Additional Notifications When Using CMS | Notification of performance evaluation | Yes. | § 63.9(g)(2)-(3) | Additional Notifications When Using CMS | Notification of COMS data use; notification that relative accuracy alternative criterion were exceeded | No, not applicable. | § 63.9(h) | Notification of Compliance Status | Contents; submittal requirements | Yes. | § 63.9(i) | Adjustment of Submittal Deadlines | Procedures for Administrator to approve change in when notifications must be submitted | Yes. | § 63.9(j) | Change in Previous Information | Must submit within 15 calendar days after the change | Yes. | § 63.9(k) | Electronic reporting procedures | Electronic reporting procedures for notifications per § 63.9(j) | Yes. | § 63.10(a) | Recordkeeping/Reporting | Applicability; general information | Yes. | § 63.10(b)(1) | General Recordkeeping Requirements | General requirements | Yes. | § 63.10(b)(2)(i) | Records Related to SSM | Recordkeeping of occurrence and duration of startups and shutdowns | No. | § 63.10(b)(2)(ii) | Records Related to SSM | Recordkeeping of failures to meet a standard | No. See § 63.8490(c)(2) for recordkeeping of (1) date, time and duration; (2) listing of affected source or equipment, and an estimate of the volume of each regulated pollutant emitted over the standard; and (3) actions to minimize emissions and correct the failure. | § 63.10(b)(2)(iii) | Records Related to SSM | Maintenance records | § 63.10(b)(2)(iv)-(v) | Records Related to SSM | Actions taken to minimize emissions during SSM | No. | § 63.10(b)(2)(vi)-(xii) and (xiv) | CMS Records | Records when CMS is malfunctioning, inoperative or out-of-control | Yes. | § 63.10(b)(2)(xiii) | Records | Records when using alternative to relative accuracy test | § 63.10(b)(3) | Records | Applicability Determinations | Yes. | § 63.10(c)(1)-(15) | Records | Additional records for CMS | No, §§ 63.8425 and 63.8490 specify requirements | § 63.10(d)(1) and (2) | General Reporting Requirements | Requirements for reporting; performance test results reporting | Yes. | § 63.10(d)(3) | Reporting Opacity or VE Observations | Requirements for reporting opacity and VE | No, not applicable. | § 63.10(d)(4) | Progress Reports | Must submit progress reports on schedule if under compliance extension | Yes. | § 63.10(d)(5) | SSM Reports | Contents and submission. | No. See § 63.8485(c)(9) for malfunction reporting requirements. | § 63.10(e)(1)-(3) | Additional CMS Reports | Requirements for CMS reporting | No, §§ 63.8425 and 63.8485 specify requirements. | § 63.10(e)(4) | Reporting COMS data | Requirements for reporting COMS data with performance test data | No, not applicable. | § 63.10(f) | Waiver for Recordkeeping/Reporting | Procedures for Administrator to waive | Yes. | § 63.11 | Flares | Requirement for flares | No, not applicable. | § 63.12 | Delegation | State authority to enforce standards | § 63.13 | Addresses | Addresses for reports, notifications, requests | Yes. | § 63.14 | Incorporation by Reference | Materials incorporated by reference | Yes. | § 63.15 | Availability of Information | Information availability; confidential information | Yes. | § 63.16 | Performance Track Provisions | Requirements for Performance Track member facilities | Yes. |
---|