| For . . .
| For the following operating limit . . .
| You must demonstrate continuous compliance by . . .
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| 1. Each affected source listed in Table 2 to this subpart | a. Each applicable operating limit listed in Table 2 to this subpart | i. Maintaining all applicable process and control device operating parameters within the limits established during the most recent performance test; and
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| | | ii. Conducting annually an inspection of all duct work, vents, and capture devices to verify that no leaks exist and that the capture device is operating such that all emissions are properly vented to the control device in accordance with the OM&M plan.
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| 2. Each affected continuous kiln used to manufacture refractory products that use organic HAP that is equipped with a THC control device | a. The operating limits specified in items 2.a. through 2.c. of Table 2 to this subpart | i. Operating the control device on the affected kiln during all times except during periods of approved scheduled maintenance, as specified in § 63.9792(e); and
ii. Before May 19, 2022, minimizing HAP emissions from the affected kiln during all periods of scheduled maintenance of the kiln control device when the kiln is operating and the control device is out of service; on and after May 19, 2022, minimizing HAP emissions during the period when the kiln is operating and the control device is out of service by complying with the applicable standard in Table 3 to this subpart; and
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| | | iii. Minimizing the duration of all periods of scheduled maintenance of the kiln control device when the kiln is operating and the control device is out of service; on and after May 19, 2022, the total time during which the kiln is operating and the control device is out of service for the each year on a 12-month rolling basis must not exceed 750 hours.
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| 3. Each new or existing curing oven, shape dryer, and kiln that is used to process refractory products that use organic HAP; each new or existing coking oven and defumer that is used to produce pitch-impregnated refractory products; each new shape preheater that is used to produce pitch-impregnated refractory products; AND each new or existing process unit that is exhausted to a thermal or catalytic oxidizer that also controls emissions from an affected shape preheater or pitch working tank | As specified in items 4 through 9 of this table | Satisfying the applicable requirements specified in items 4 through 9 of this table.
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| 4. Each affected continuous process unit | Maintain process operating parameters within the limits established during the most recent performance test | i. Recording the organic HAP processing rate (pounds per hour); and
ii. Recording the operating temperature of the affected source at least hourly; and
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| | | iii. Maintaining the 3-hour block average organic HAP processing rate at or below the maximum organic HAP processing rate established during the most recent performance test.
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| 5. Continuous process units that are equipped with a thermal oxidizer | Maintain the 3-hour block average operating temperature in the thermal oxidizer combustion chamber at or above the minimum allowable operating temperature established during the most recent performance test | i. Measuring and recording the thermal oxidizer combustion chamber temperature at least every 15 minutes; and
ii. Calculating the hourly average thermal oxidizer combustion chamber temperature; and
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| | | iii. Maintaining the 3-hour block average thermal oxidizer combustion chamber temperature at or above the minimum allowable operating temperature established during the most recent performance test; and
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| | | iv. Reporting, in accordance with § 63.9814(e), any 3-hour block average operating temperature measurements below the minimum allowable thermal oxidizer combustion chamber operating temperature established during the most recent performance test.
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| 6. Continuous process units that are equipped with a catalytic oxidizer | a. Maintain the 3-hour block average temperature at the inlet of the catalyst bed at or above the minimum allowable catalyst bed inlet temperature established during the most recent performance test | i. Measuring and recording the temperature at the inlet of the catalyst bed at least every 15 minutes; and
ii. Calculating the hourly average temperature at the inlet of the catalyst bed; and
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| | | iii. Maintaining the 3-hour block average temperature at the inlet of the catalyst bed at or above the minimum allowable catalyst bed inlet temperature established during the most recent performance test; and
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| | | iv. Reporting, in accordance with § 63.9814(e), any 3-hour block average catalyst bed inlet temperature measurements below the minimum allowable catalyst bed inlet temperature established during the most recent performance; and
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| | | v. Checking the activity level of the catalyst at least every 12 months and taking any necessary corrective action, such as replacing the catalyst, to ensure that the catalyst is performing as designed.
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| 7. Each affected batch process unit | Maintain process operating parameters within the limits established during the most recent performance test | i. Recording the organic HAP processing rate (pounds per batch); and
ii. Recording the hourly average operating temperature of the affected source; and
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| | | iii. Recording the process cycle time for each batch cycle; and
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| | | iv. Maintaining the organic HAP processing rate at or below the maximum organic HAP processing rate established during the most recent performance test.
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| 8. Batch process units that are equipped with a thermal oxidizer | Maintain the hourly average temperature in the thermal oxidizer combustion chamber at or above the hourly average temperature established for the corresponding 1-hour period of the cycle during the most recent performance test | i. Measuring and recording the thermal oxidizer combustion chamber temperature at least every 15 minutes; and
ii. Calculating the hourly average thermal oxidizer combustion chamber temperature; and
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| | | iii. From the start of each batch cycle until 3 hours have passed since the process unit reached maximum temperature, maintaining the hourly average operating temperature in the thermal oxidizer combustion chamber at or above the minimum allowable operating temperature established for the corresponding period during the most recent performance test, as determined according to item 11 of Table 4 to this subpart; and
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| | | iv. For each subsequent hour of the batch cycle, maintaining the hourly average operating temperature in the thermal oxidizer combustion chamber at or above the minimum allowable operating temperature established for the corresponding hour during the most recent performance test, as specified in item 13 of Table 4 to this subpart; and
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| | | v. Reporting, in accordance with § 63.9814(e), any temperature measurements below the minimum allowable thermal oxidizer combustion chamber temperature measured during the most recent performance test.
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| 9. Batch process units that are equipped with a catalytic oxidizer | Maintain the hourly average temperature at the inlet of the catalyst bed at or above the corresponding hourly average temperature established for the corresponding 1-hour period of the cycle during the most recent performance test | i. Measuring and recording temperatures at the inlet of the catalyst bed at least every 15 minutes; and
ii. Calculating the hourly average temperature at the inlet of the catalyst bed; and
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| | | iii. From the start of each batch cycle until 3 hours have passed since the process unit reached maximum temperature, maintaining the hourly average operating temperature at the inlet of the catalyst bed at or above the minimum allowable bed inlet temperature established for the corresponding period during the most recent performance test, as determined according to item 12 of Table 4 to this subpart; and
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| | | iv. For each subsequent hour of the batch cycle, maintaining the hourly average operating temperature at the inlet of the catalyst bed at or above the minimum allowable bed inlet temperature established for the corresponding hour during the most recent performance test, as specified in item 13 of Table 4 to this subpart; and
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| | | v. Reporting, in accordance with § 63.9814(e), any catalyst bed inlet temperature measurements below the minimum allowable bed inlet temperature measured during the most recent performance test; and
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| | | vi. Checking the activity level of the catalyst at least every 12 months and taking any necessary corrective action, such as replacing the catalyst, to ensure that the catalyst is performing as designed.
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| 10. Each new kiln that is used to process clay refractory products | As specified in items 11 through 13 of this table | Satisfying the applicable requirements specified in items 11 through 13 of this table.
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| 11. Each new kiln that is equipped a DLA | a. Maintain the average pressure drop across the DLA for each 3-hour block period at or above the minimum pressure drop established during the most recent performance test | i. Collecting the DLA pressure drop data, as specified in item 18.a. of Table 4 to this subpart; and
ii. Reducing the DLA pressure drop data to 1-hour and 3-hour block averages; and
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| | | iii. Maintaining the 3-hour block average pressure drop across the DLA at or above the minimum pressure drop established during the most recent performance test.
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| | b. Maintain free-flowing limestone in the feed hopper, silo, and DLA | Verifying that the limestone hopper has an adequate amount of free-flowing limestone by performing a daily visual check of the limestone hopper.
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| | c. Maintain the limestone feeder setting at or above the level established during the most recent performance test | Recording the limestone feeder setting at least daily to verify that the feeder setting is being maintained at or above the level established during the most recent performance test.
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| | d. Use the same grade of limestone from the same source as was used during the most recent performance test | Using the same grade of limestone as was used during the most recent performance test and maintaining records of the source and grade of limestone.
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| | e. Maintain no VE from the stack | i. Performing VE observations of the stack at the frequency specified in § 63.9810(f) using EPA Method 22 of 40 CFR part 60, appendix A-7; and
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| | | ii. Maintaining no VE from the stack.
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| 12. Each new kiln that is equipped with a DIFF or DLS/FF | a. Initiate corrective action within 1 hour of a bag leak detection system alarm and complete corrective actions in accordance with the OM&M plan; AND operate and maintain the fabric filter such that the alarm does not engage for more than 5 percent of the total operating time in a 6-month block reporting period | i. Initiating corrective action within 1 hour of a bag leak detection system alarm and completing corrective actions in accordance with the OM&M plan; and
ii. Operating and maintaining the fabric filter such that the alarm does not engage for more than 5 percent of the total operating time in a 6-month block reporting period; in calculating this operating time fraction, if inspection of the fabric filter demonstrates that no corrective action is required, no alarm time is counted; if corrective action is required, each alarm shall be counted as a minimum of 1 hour; if you take longer than 1 hour to initiate corrective action, the alarm time shall be counted as the actual amount of time taken by you to initiate corrective action.
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| | b. Maintain free-flowing lime in the feed hopper or silo at all times for continuous injection systems; AND maintain feeder setting at or above the level established during the most recent performance test for continuous injection systems | i. Verifying at least once each 8-hour shift that lime is free-flowing via a load cell, carrier gas/lime flow indicator, carrier gas pressure drop measurement system, or other system; recording all monitor or sensor output, and if lime is found not to be free flowing, promptly initiating and completing corrective actions; and
ii. Recording the feeder setting once each day of operation to verify that the feeder setting is being maintained at or above the level established during the most recent performance test.
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| 13. Each new kiln that is used to process clay refractory products and is equipped with a wet scrubber | a. Maintain the average pressure drop across the scrubber for each 3-hour block period at or above the minimum pressure drop established during the most recent performance test | i. Collecting the scrubber pressure drop data, as specified in item 20.a. of Table 4 to this subpart; and
ii. Reducing the scrubber pressure drop data to 1-hour and 3-hour block averages; and
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| | | iii. Maintaining the 3-hour block average scrubber pressure drop at or above the minimum pressure drop established during the most recent performance test.
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| | b. Maintain the average scrubber liquid pH for each 3-hour block period at or above the minimum scrubber liquid pH established during the most recent performance test | i. Collecting the scrubber liquid pH data, as specified in item 20.b. of Table 4 to this subpart; and
ii. Reducing the scrubber liquid pH data to 1-hour and 3-hour block averages; and
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| | | iii. Maintaining the 3-hour block average scrubber liquid pH at or above the minimum scrubber liquid pH established during the most recent performance test.
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| | c. Maintain the average scrubber liquid flow rate for each 3-hour block period at or above the minimum scrubber liquid flow rate established during the most recent performance test | i. Collecting the scrubber liquid flow rate data, as specified in item 20.c. of Table 4 to this subpart; and
ii. Reducing the scrubber liquid flow rate data to 1-hour and 3-hour block averages; and
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| | | iii. Maintaining the 3-hour block average scrubber liquid flow rate at or above the minimum scrubber liquid flow rate established during the most recent performance test.
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| | d. If chemicals are added to the scrubber liquid, maintain the average scrubber chemical feed rate for each 3-hour block period at or above the minimum scrubber chemical feed rate established during the most recent performance test | i. Collecting the scrubber chemical feed rate data, as specified in item 20.d. of Table 4 to this subpart; and
ii. Reducing the scrubber chemical feed rate data to 1-hour and 3-hour block averages; and
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| | | iii. Maintaining the 3-hour block average scrubber chemical feed rate at or above the minimum scrubber chemical feed rate established during the most recent performance test.
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| 14. Each new and existing affected kiln that is equipped with an activated carbon injection system | a. 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 | i. Collecting the carbon flow rate data, as specified in item 23 of Table 4 to this subpart; and
ii. Reducing the carbon flow rate data to 3-hour block averages; and
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| | | iii. Maintaining the average carbon flow rate for each 3-hour block period at or above the average carbon flow rate established during the Hg performance test in which compliance was demonstrated.
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| 15. Each existing affected kiln that is equipped with a DLA or no add-on control | a. Maintain no VE from the stack | i. Performing VE observations of the stack at the frequency specified in § 63.9810(f) using EPA Method 22 of 40 CFR part 60, appendix A-7; and
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| | | ii. Maintaining no VE from the stack.
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| 16. Each existing affected kiln that is equipped with a FF | a. Maintain no VE from the stack; OR | i. Performing VE observations of the stack at the frequency specified in § 63.9810(f) using EPA Method 22 of 40 CFR part 60, appendix A-7; and
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| | | ii. Maintaining no VE from the stack.
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| | b. Initiate corrective action within 1 hour of a bag leak detection system alarm and complete corrective actions in accordance with the OM&M plan; AND operate and maintain the fabric filter such that the alarm does not engage for more than 5 percent of the total operating time in a 6-month block reporting period | i. Initiating corrective action within 1 hour of a bag leak detection system alarm and completing corrective actions in accordance with the OM&M plan; and
ii. Operating and maintaining the fabric filter such that the alarm does not engage for more than 5 percent of the total operating time in a 6-month block reporting period; in calculating this operating time fraction, if inspection of the fabric filter demonstrates that no corrective action is required, no alarm time is counted; if corrective action is required, each alarm shall be counted as a minimum of 1 hour; if you take longer than 1 hour to initiate corrective action, the alarm time shall be counted as the actual amount of time taken by you to initiate corrective action.
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| 17. Each existing affected kiln that is equipped with a wet scrubber | a. Maintain the average pressure drop across the scrubber for each 3-hour block period at or above the minimum pressure drop established during the most recent performance test | i. Collecting the scrubber pressure drop data, as specified in item 25.a of Table 4 to this subpart; and
ii. Reducing the scrubber pressure drop data to 1-hour and 3-hour block averages; and
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| | | iii. Maintaining the 3-hour block average scrubber pressure drop at or above the minimum pressure drop established during the most recent performance test.
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| | b. Maintain the average scrubber liquid flow rate for each 3-hour block period at or above the minimum scrubber liquid flow rate established during the most recent performance test | i. Collecting the scrubber liquid flow rate data, as specified in item 25.b. of Table 4 to this subpart; and
ii. Reducing the scrubber liquid flow rate data to 1-hour and 3-hour block averages; and
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| | | iii. Maintaining the 3-hour block average scrubber liquid flow rate at or above the minimum scrubber liquid flow rate established during the most recent performance test. |