e. Determine the 2 run block average THC percentage reduction for the emission test. The average THC percentage reduction for each test run. Calculate the average of the average THC percentage reductions for each test run. 11. Each batch process unit that is equipped with a thermal oxidizer. a. Establish the operating limit for the minimum thermal oxidizer combustion chamber temperature. i. Continuous recording of the output of the combustion chamber temperature measurement device. ( 1) At least every 15 minutes, measure and record the thermal oxidizer combustion chamber temperature; and ( 2) Provide at least one temperature measurement during at least three 15 minute periods per hour of testing and ( 3) Calculate the hourly average combustion chamber temperature for each hour of the 3 hour peak emissions period, as defined in item 9. d. or 10. c. of this table, whichever applies and ( 4) Calculate the minimum allowable thermal oxidizer combustion chamber operating temperature as the average of the hourly combustion chamber temperatures for the 3 hour peak emissions period, minus 14 ° C ( 25 ° F). 12. Each batch process unit that is equipped with a catalytic oxidizer. a. Establish the operating limit for the minimum temperature at the inlet of the catalyst bed. i. Continuous recording of the output of the temperature measurement device ( 1) At least every 15 minutes, measure and record the temperature at the inlet of the catalyst bed; and ( 2) Provide at least one catalyst bed inlet temperature measurement during at least three 15 minute periods per hour of testing; and ( 3) Calculate the hourly average catalyst bed inlet temperature for each hour of the 3 hour peak emissions period, as defined in item 9. d. or 10. c. of this table, whichever applies and ( 4) Calculate the minimum allowable catalytic oxidizer catalyst bed inlet temperature as the average of the hourly catalyst bed inlet temperatures for the 3 hour peak emissions period, minus 14 ° C ( 25 ° F). 13. Each batch process unit that is equipped with a thermal or catalytic oxidizer. a. During each test run, maintain the applicable operating temperature of the oxidizer until emission levels allow the oxidizer to be shut off or the operating temperature of the oxidizer to be reduced. ( 1) The oxidizer can be shut off or the oxidizer operating temperature can be reduced if you do not use an emission profile to limit testing to the 3 hour peak emissions period, as specified in item 8. a. i. 4. of this table; and ( 2) At least 3 hours have passed since the affected process unit reached maximum temperature; and VerDate Jan< 31> 2003 14: 42 Apr 15, 2003 Jkt 200001 PO 00000 Frm 00040 Fmt 4701 Sfmt 4700 E:\ FR\ FM\ 16APR2. SGM 16APR2 18769 Federal Register / Vol. 68, No. 73 / Wednesday, April 16, 2003 / Rules and Regulations TABLE 4 TO SUBPART SSSSS TO PART 63.   REQUIREMENTS FOR PERFORMANCE TESTS   Continued For . . . You must . . . Using . . . According to the following requirements . . .

( 3) The applicable emission limit specified in item 6. a. or 6. b. of Table 1 to this subpart was met during each of the previous three 1 hour periods; and ( 4) The hourly average THC mass emissions rate did not increase during the 3 hour period since maximum process temperature was reached; and ( 5) The applicable emission limit specified in item 6. a. and 6. b. of Table 1 to this subpart was met during each of the four 15 minute periods immediately following the oxidizer temperature reduction; and ( 6) If the applicable emission limit specified in item 6. a. or 6. b. of Table 1 to this subpart was not met during any of the four 15 minute periods immediately following the oxidizer temperature reduction, you must return the oxidizer to its normal operating temperature as soon as possible and maintain that temperature for at least 1 hour; and ( 7) Continue the test run until the applicable emission limit specified in items 6. a. and 6. b. of Table 1 to this subpart is met for at least four consecutive 15 minute periods that immediately follow the temperature reduction and ( 8) Calculate the hourly average oxidizer operating temperature for each hour of the performance test since the affected process unit reached maximum temperature. 14. Each new continuous kiln that is used to process clay refractory products. a. Measure emissions of HF and HCl .. i. Method 26A of 40 CFR part 60, appendix A; or ii. Method 26 of 40 CFR part 60, appendix A; or iii. Method 320 of 40 CFR part 63, appendix A. ( 1) Conduct the test while the kiln is operating at the maximum production level; and ( 2) You may use Method 26 of 40 CFR part 60, appendix A, only if no acid PM ( e. g., HF or HCl dissolved in water droplets emitted by sources controlled by a wet scrubber) is present; and ( 3) If you use Method 320 of 40 CFR part 63, appendix A, you must follow the analyte spiking procedures of Section 13 of Method 320 unless you can demonstrate that the complete spiking procedure has been conducted at a similar source; and ( 4) Repeat the performance test if the affected source is controlled with a DLA and you change the source of the limestone used in the DLA. b. Perform a minimum of 3 test runs ... The appropriate test methods specified in items 1 and 14. a. of this table. Each test run must be at least 1 hour in duration.

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15. Each new continuous kiln that is subject to the production based HF and HCl emission limits specified in items 10. a. and 10. b. of Table 1 to this subpart. a. Record the uncalcined clay processing rate. i. Production data; and ......................... ii. Product formulation data that specify the mass fraction of uncalcined clay in the products that are processed during the performance test. ( 1) Record the production rate ( tons per hour of fired product); and ( 2) Calculate and record the average rate at which uncalcined clay is processed ( tons per hour) for each test run; and ( 3) Calculate and record the 3 run average uncalcined clay processing rate as the average of the average uncalcined clay processing rates for each test run. b. Determine the HF mass emissions rate at the outlet of the control device or in the stack. i. Method 26A of 40 CFR part 60, appendix A; or ii. Method 26 of 40 CFR part 60, appendix A; or iii. Method 320 of 40 CFR part 63, appendix A. Calculate the HF mass emissions rate for each test.

c. Determine the 3 hour block average production based HF emissions rate. i. The HF mass emissions rate for each test run; and ii. The average uncalcined clay processing rate. ( 1) Calculate the hourly productionbased HF emissions rate for each test run using Equation 3 of § 63.9800( g)( 3); and ( 2) Calculate the 3 hour block average production based HF emissions rate as the average of the hourly production based HF emissions rates for each test run. d. Determine the HCl mass emissions rate at the outlet of the control device or in the stack. i. Method 26A of 40 CFR part 60, appendix A; or ii. Method 26 of 40 CFR part 60, appendix A; or iii. Method 320 of 40 CFR part 63, appendix A. Calculate the HCl mass emissions rate for each test run.

e. Determine the 3 hour block average production based HCl emissions rate. i. The HCl mass emissions rate for each test run; and ii. The average uncalcined clay processing rate. ( 1) Calculate the hourly productionbased HCl emissions rate for each test run using Equation 3 of § 63.9800( g)( 3); and ( 2) Calculate the 3 hour block average production based HCl emissions rate as the average of the productionbased HCl emissions rates for each test run. 16. Each new continuous kiln that is subject to the HF and HCl percentage reduction limits specified in items 10. a. and 10. b. of Table 1 to this subpart. a. Measure the HF mass emissions rates at the inlet and outlet of the control device. i. Method 26A of 40 CFR part 60, appendix A; or ii. Method 26 of 40 CFR part 60, appendix A; or iii. Method 320 of 40 CFR part 63, appendix A. Calculate the HF mass emissions rates at the control device inlet and outlet for each test run.

b. Determine the 3 hour block average HF percentage reduction. i. The HF mass emissions rates at the inlet and outlet of the control device for each test run ( 1) Calculate the hourly HF percentage reduction using Equation 2 of § 63.9800( g)( 2); and ( 2) Calculate the 3 hour block average HF percentage reduction as the average of the HF percentage reductions for each test run. c. Measure the HCl mass emissions rates at the inlet and outlet of the control device. i. Method 26A of 40 CFR part 60, appendix A; or ii. Method 26 of 40 CFR part 60, appendix A; or iii. Method 320 of 40 CFR part 63, appendix A. Calculate the HCl mass emissions rates at the control device inlet and outlet for each test run.

d. Determine the 3 hour block average HCl percentage reduction. i. The HCl mass emissions rates at the inlet and outlet of the control device for each test run. ( 1) Calculate the hourly HCl percentage reduction using Equation 2 of § 63.9800( g)( 2); and ( 2) Calculate the 3 hour block average HCl percentage reduction as the average of HCl percentage reductions for each test run.

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17. Each new batch process kiln that is used to process clay refractory products. a. Measure emissions of HF and HCl at the inlet and outlet of the control device. i. Method 26A of 40 CFR part 60, appendix A; or ii. Method 26 of 40 CFR part 60, appendix A; or iii. Method 320 of 40 CFR part 63, appendix A. ( 1) Conduct the test while the kiln is operating at the maximum production level; and ( 2) You may use Method 26 of 40 CFR part 60, appendix A, only if no acid PM ( e. g., HF or HCl dissolved in water droplets emitted by sources controlled by a wet scrubber) is present; and ( 3) If you use Method 320 of 40 CFR part 63, you must follow the analyte spiking procedures of Section 13 of Method 320 unless you can demonstrate that the complete spiking procedure has been conducted at a similar source; and ( 4) Repeat the performance test if the affected source is controlled with a DLA and you change the source of the limestone used in the DLA. b. Perform a minimum of 2 test runs ... i. The appropriate test methods specified in items 1 and 17. a. of this table. ( 1) Each test run must be conducted over a separate batch cycle unless you satisfy the requirements of § 63.9800( f)( 3) and ( 4); and ( 2) Each test run must consist of a series of 1 hour runs at the inlet and outlet of the control device, beginning with the start of a batch cycle, except as specified in item 17. b. i. 4. of this table; and ( 3) Each test run must continue until the end of the batch cycle, except as specified in item 17. b. i. 4. of this table; and ( 4) If you develop an emissions profile, as described in § 63.9802( b), you can limit each test run to the 3 hour peak HF emissions period. c. Determine the hourly HF and HCl mass emissions rates at the inlet and outlet of the control device. i. The appropriate test methods specified in items 1 and 17. a. of this table. Determine the hourly mass HF and HCl emissions rates at the inlet and outlet of the control device for each hour of each test run. d. Determine the 3 hour peak HF emissions period. The hourly HF mass emissions rates at the inlet of the control device. Select the period of 3 consecutive hours over which the sum of the hourly HF mass emissions rates at the control device inlet is greater than the sum of the hourly HF mass emissions rates at the control device inlet for any other period of 3 consecutive hours during the test run. e. Determine the 2 run block average HF percentage reduction for the emissions test. i. The hourly average HF emissions rates at the inlet and outlet of the control device. ( 1) Calculate the HF percentage reduction for each hour of the 3 hour peak HF emissions period using Equation 2 of § 63.9800( g)( 2); and ( 2) Calculate the average HF percentage reduction for each test run as the average of the hourly HF percentage reductions for the 3 hour peak HF emissions period for that run; and ( 3) Calculate the 2 run block average HF percentage reduction for the emission test as the average of the average HF percentage reductions for the two test runs.

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f. Determine the 2 run block average HCl percentage reduction for the emission test. i. The hourly average HCl emissions rates at the inlet and outlet of the control device. ( 1) Calculate the HCl percentage reduction for each hour of the 3 hour peak HF emissions period using Equation 2 § 63.9800( g)( 2); and ( 2) Calculate the average HCl percentage reduction for each test run as the average of the hourly HCl percentage reductions for the 3 hour peak HF emissions period for that run; and ( 3) Calculate the 2 run block average HCl percentage reduction for the emission test as the average of the average HCl percentage reductions for the two test runs. 18. Each new kiln that is used to process clay refractory products and is equipped with a DLA. a. Establish the operating limit for the minimum pressure drop across the DLA. Data from the pressure drop measurement device during the performance test. ( 1) At least every 15 minutes, measure the pressure drop across the DLA; and ( 2) Provide at least one pressure drop measurement during at least three 15 minute periods per hour of testing and ( 3) Calculate the hourly average pressure drop across the DLA for each hour of the performance test; and ( 4) Calculate and record the minimum pressure drop as the average of the hourly average pressure drops across the DLA for the two or three test runs, whichever applies. b. Establish the operating limit for the limestone feeder setting. Data from the limestone feeder during the performance test. ( 1) Ensure that limestone in the feed hopper, silo, and DLA is free flowing at all times during the performance test; and ( 2) Establish the limestone feeder setting 1 week prior to the performance test; and ( 3) Record and maintain the feeder setting for the 1 week period that precedes the performance test and during the performance test. 19. Each new kiln that is used to process clay refractory products and is equipped with a DIFF or DLS/ FF. a. Document conformance with specifications and requirements of the bag leak detection system. Data from the installation and calibration of the bag leak detection system. Submit analyses and supporting documentation demonstrating conformance with EPA guidance and specifications for bag leak detection systems as part of the Notification of Compliance Status.

b. Establish the operating limit for the lime feeder setting. i. Data from the lime feeder during the performance test. ( 1) For continuous lime injection systems ensure that lime in the feed hopper or silo is free flowing at all times during the performance test; and ( 2) Record the feeder setting for the three test runs; and ( 3) If the feed rate setting varies during the three test runs, calculate and record the average feed rate for the two or three test runs, whichever applies 20. Each new kiln that is used to process clay refractory products and is equipped with a wet scrubber a. Establish the operating limit for the minimum scrubber pressure drop. i. Data from the pressure drop measurement device during the performance test. ( 1) At least every 15 minutes, measure the pressure drop across the scrubber and ( 2) Provide at least one pressure drop measurement during at least three 15 minute periods per hour of testing and VerDate Jan< 31> 2003 14: 42 Apr 15, 2003 Jkt 200001 PO 00000 Frm 00044 Fmt 4701 Sfmt 4700 E:\ FR\ FM\ 16APR2. SGM 16APR2 18773 Federal Register / Vol. 68, No. 73 / Wednesday, April 16, 2003 / Rules and Regulations TABLE 4 TO SUBPART SSSSS TO PART 63.   REQUIREMENTS FOR PERFORMANCE TESTS   Continued For . . . You must . . . Using . . . According to the following requirements . . .

( 3) Calculate the hourly average pressure drop across the scrubber for each hour of the performance test; and ( 4) Calculate and record the minimum pressure drop as the average of the hourly average pressure drops across the scrubber for the two or three test runs, whichever applies. b. Establish the operating limit for the minimum scrubber liquid pH. i. Data from the pH measurement device during the performance test. ( 1) At least every 15 minutes, measure scrubber liquid pH; and ( 2) Provide at least one pH measurement during at least three 15 minute periods per hour of testing; and ( 3) Calculate the hourly average pH values for each hour of the performance test; and ( 4) Calculate and record the minimum liquid pH as the average of the hourly average pH measurements for the two or three test runs, whichever applies c. Establish the operating limit for the minimum scrubber liquid flow rate. i. Data from the flow rate measurement device during the performance test. ( 1) At least every 15 minutes, measure the scrubber liquid flow rate; and ( 2) Provide at least one flow rate measurement during at least three 15 minute periods per hour of testing and ( 3) Calculate the hourly average liquid flow rate for each hour of the performance test; and ( 4) Calculate and record the minimum liquid flow rate as the average of the hourly average liquid flow rates for the two or three test runs, whichever applies. d. If chemicals are added to the scrubber liquid, establish the operating limit for the minimum scrubber chemical feed rate. i. Data from the chemical feed rate measurement device during the performance test. ( 1) At least every 15 minutes, measure the scrubber chemical feed rate; and ( 2) Provide at least one chemical feed rate measurement during at least three 15 minute periods per hour of testing; and ( 3) Calculate the hourly average chemical feed rate for each hour of the performance test; and ( 4) Calculate and record the minimum chemical feed rate as the average of the hourly average chemical feed rates for the two or three test runs, whichever applies.

As stated in § 63.9806, you must show initial compliance with the emission limits for affected sources according to the following table:

TABLE 5 TO SUBPART SSSSS OF PART 63.   INITIAL COMPLIANCE WITH EMISSION LIMITS For . . . For the following emission limit . . . You have demonstrated compliance if . . .

1. Each affected source listed in Table 1 to this subpart. a. Each applicable emission limit listed in Table 1 to this subpart. i. Emissions measured using the test methods specified in Table 4 to this subpart satisfy the applicable emission limits specified in Table 1 to this subpart; and ii. You establish and have a record of the operating limits listed in Table 2 to this subpart over the performance test period; and iii. You report the results of the performance test in the Notification of Compliance Status as specified by § 63.9812( e)( 1) and ( 2).

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2. Each new or existing curing oven, shape dryer, and kiln that is used to process refractory products that use organic HAP; each new or existing coking oven and defumer that is used to produce pitch impregnated refractory products; each new shape preheater that is used to produce pitch impregnated refractory products; AND each new or existing process unit that is exhausted to a thermal or catalytic oxidizer that also controls emissions from an affected shape preheater or pitch working tank. As specified in items 3 through 8 of this table You have satisfied the applicable requirements specified in items 3 through 8 of this table.

3. Each affected continuous process unit that is subject to the THC emission concentration limit listed in item 2. a., 3. a., 4, or 5 of Table 1 to this subpart. The average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygen The 3 hour block average THC emission concentration measured during the performance test using Methods 25A and 3A is equal to or less than 20 ppmvd, corrected to 18 percent oxygen. 4. Each affected continuous process unit that is subject to the THC percentage reduction limit listed in item 2. b. or 3. b. of Table 1 to this subpart. The average THC percentage reduction must equal or exceed 95 percent. The 3 hour block average THC percentage reduction measured during the performance test using Method 25A is equal to or greater than 95 percent. 5. Each affected batch process unit that is subject to the THC emission concentration limit listed in item 6. a., 7. a., 8, or 9 of Table 1 to this subpart. The average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygen The 2 run block average THC emission concentration for the 3 hour peak emissions period measured during the performance test using Methods 25A and 3A is equal to or less than 20 ppmvd, corrected to 18 percent oxygen. 6. Each affected batch process unit that is subject to the THC percentage reduction limit listed in item 6. b. or 7. b. of Table 1 to this subpart. The average THC percentage reduction must equal or exceed 95 percent. The 2 run block average THC percentage reduction for the 3 hour peak emissions period measured during the performance test using Method 25A is equal to or exceeds 95 percent. 7. Each affected continuous or batch process unit that is equipped with a control device other than a thermal or catalytic oxidizer and is subject to the emission limit listed in item 3 or 7 of Table 1 to this subpart. a. The average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygen; or i. You have installed a THC CEMS at the outlet of the control device or in the stack of the affected source; and b. The average THC percentage reduction must equal or exceed 95 percent. ii. You have satisfied the requirements of PS   8 of 40 CFR part 60, appendix B. 8. Each affected continuous or batch process unit that uses process changes to reduce organic HAP emissions and is subject to the emission limit listed in item 4 or 8 of Table 1 to this subpart. The average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygen i. You have installed a THC CEMS at the outlet of the control device or in the stack of the affected source; and ii. You have satisfied the requirements of PS   8 of 40 CFR part 60, appendix B. 9. Each new continuous kiln that is used to process clay refractory products. a. The average HF emissions must not exceed 0.019 kg/ Mg ( 0.038 lb/ ton) of uncalcined clay processed; OR the average uncontrolled HF emissions must be reduced by at least 90 percent. i. The 3 hour block average production based HF emissions rate measured during the performance test using one of the methods specified in item 14. a. i. of Table 4 to this subpart is equal to or less than 0.019 kg/ Mg ( 0.038 lb/ ton) of uncalcined clay processed or ii. The 3 hour block average HF emissions reduction measured during the performance test is equal to or greater than 90 percent. b. The average HCl emissions must not exceed 0.091 kg/ Mg ( 0.18 lb/ ton) of uncalcined clay processed; OR the average uncontrolled HCl emissions must be reduced by at least 30 percent. i. The 3 hour block average production based HCl emissions rate measured during the performance test using one of the methods specified in item 14. a. i. of Table 4 to this subpart is equal to or less than 0.091 kg/ Mg ( 0.18 lb/ ton) of uncalcined clay processed or ii. The 3 hour block average HCl emissions reduction measured during the performance test is equal to or greater than 30 percent. 10. Each new batch process kiln that is used to process clay refractory products. a. The average uncontrolled HF emissions must be reduced by at least 90 percent. The 2 run block average HF emission reduction measured during the performance test is equal to or greater than 90 percent. b. The average uncontrolled HCl emissions must be reduced by at least 30 percent. The 2 run block average HCl emissions reduction measured during the performance test is equal to or greater than 30 percent.

VerDate Jan< 31> 2003 14: 42 Apr 15, 2003 Jkt 200001 PO 00000 Frm 00046 Fmt 4701 Sfmt 4755 E:\ FR\ FM\ 16APR2. SGM 16APR2 18775 Federal Register / Vol. 68, No. 73 / Wednesday, April 16, 2003 / Rules and Regulations As stated in § 63.9806, you must show initial compliance with the work practice standards for affected sources according to the following table:

TABLE 6 TO SUBPART SSSSS OF PART 63.   INITIAL COMPLIANCE WITH WORK PRACTICE STANDARDS For each . . . For the following standard . . . You have demonstrated initial compliance if . . .

1. Each affected source listed in Table 3 to this subpart. a. Each applicable work practice standard listed in Table 3 to this subpart. i. You have selected a method for performing each of the applicable work practice standards listed in Table 3 to this subpart; and ii. You have included in your Initial Notification a description of the method selected for complying with each applicable work practice standard, as required by § 63.9( b); and iii. You submit a signed statement with the Notification of Compliance Status that you have implemented the applicable work practice standard listed in Table 3 to this subpart; and iv. You have described in your OM& M plan the method for complying with each applicable work practice standard specified in Table 3 to this subpart. 2. Each basket or container that is used for holding fired refractory shapes in an existing shape preheater and autoclave during the pitch impregnation process. a. Control POM emissions from any affected shape preheater. i. You have implemented at least one of the work practice standards listed in item 1 of Table 3 to this subpart; and ii. You have established a system for recording the date and cleaning method for each time you clean an affected basket or container 3. Each affected new or existing pitch working tank. Control POM emissions ................................... You have captured and vented emissions from the affected pitch working tank to the device that is used to control emissions from an affected defumer or coking oven, or to a thermal or catalytic oxidizer that is comparable to the control device used on an affected defumer or coking oven. 4. Each new or existing chromium refractory products kiln. Minimize fuel based HAP emissions ............... You use natural gas, or equivalent, as the kiln fuel. 5. Each existing clay refractory products kiln .... Minimize fuel based HAP emissions ............... You use natural gas, or equivalent, as the kiln fuel.

As stated in § 63.9810, you must show continuous compliance with the emission limits for affected sources according to the following table:

TABLE 7 TO SUBPART SSSSS TO PART 63.   CONTINUOUS COMPLIANCE WITH EMISSION LIMITS For . . . For the following emission limit . . . You must demonstrate continuous compliance by . . .

1. Each affected source listed in Table 1 to this subpart. a. Each applicable emission limit listed in Table 1 to this subpart. i. Collecting and recording the monitoring and process data listed in Table 2 ( operating limits) to this subpart; and ii. Reducing the monitoring and process data associated with the operating limits specified in Table 2 to this subpart; and iii. Recording the results of any control device inspections; and iv. Reporting, in accordance with § 63.9814( e), any deviation from the applicable operating limits specified in Table 2 to this subpart. 2. Each new or existing curing oven, shape dryer, and kiln that is used to process refractory products that use organic HAP; each new or existing coking oven and defumer that is used to produce pitch impregnated refractory products; each new shape preheater that is used to produce pitch impregnated refractory products; AND each new or existing process unit that is exhausted to a thermal or catalytic oxidizer that also controls emissions from an affected shape preheater or pitch working tank. As specified in items 3 though 7 of this table Satisfying the applicable requirements specified in items 3 through 7 of this table.

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3. Each affected process unit that is equipped with a thermal or catalytic oxidizer. a. The average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygen; OR the average THC percentage reduction must equal or exceed 95 percent. i. Collecting the applicable data measured by the control device temperature monitoring system, as specified in items 5, 6, 8, and 9 of Table 8 to this subpart; and ii. Reducing the applicable data measured by the control device temperature monitoring system, as specified in items 5, 6, 8, and 9 of Table 8 to this subpart; and iii. Maintaining the average control device operating temperature for the applicable averaging period specified in items 5, 6, 8, and 9 of Table 2 to this subpart at or above the minimum allowable operating temperature established during the most recent performance test. 4. Each affected process unit that is equipped with a control device other than a thermal or catalytic oxidizer. The average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygen OR the average THC performance reduction must equal or exceed 95 percent. Operating and maintaining a THC CEMS at the outlet of the control device or in the stack of the affected source, according to the requirements of Procedure 1 of 40 CFR part 60, appendix F. 5. Each affected process unit that uses process changes to meet the applicable emission limit. The average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygen Operating and maintaining a THC CEMS at the outlet of the control device or in the stack of the affected source, according to the requirements of Procedure 1 of 40 CFR part 60, appendix F. 6. Each affected continuous process unit .......... The average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygen OR the average THC percentage reduction must equal or exceed 95 percent. Recording the organic HAP processing rate ( pounds per hour) and the operating temperature of the affected source, as specified in items 3. b. and 3. c. of Table 4 to this subpart 7. Each affected batch process unit .................. The average THC concentration must not exceed 20 ppmvd, corrected to 18 percent oxygen OR the average THC percentage reduction must equal or exceed 95 percent. Recording the organic HAP processing rate ( pounds per batch); and process cycle time for each batch cycle; and hourly average operating temperature of the affected source, as specified in items 8. b. through 8. d. of Table 4 to this subpart. 8. Each kiln that is used to process clay refractory products. As specified in items 9 through 11 of this table. Satisfying the applicable requirements specified in items 9 through 11 of this table. 9. Each affected kiln that is equipped with a DLA. a. The average HF emissions must not exceed 0.019 kg/ Mg ( 0.038 lb/ ton) of uncalcined clay processed, OR the average uncontrolled HF emissions must be reduced by at least 90 percent; and b. The average HCl emissions must not exceed 0.091 kg/ Mg ( 0.18 lb/ ton) of uncalcined clay processed, or the average uncontrolled HCl emissions must be reduced by at least 30 percent. i. Maintaining the pressure drop across the DLA at or above the minimum levels established during the most recent performance test; and ii. Verifying that the limestone hopper contains an adequate amount of free flowing limestone by performing a daily visual check of the limestone in the feed hopper; and iii. Recording the limestone feeder setting daily to verify that the feeder setting is at or above the level established during the most recent performance test; and iv. Using the same grade of limestone as was used during the most recent performance test and maintaining records of the source and grade of limestone. 10. Each affected kiln that is equipped with a DIFF or DLS/ FF. a. The average HF emissions must not exceed 0.019 kg/ Mg ( 0.038 lb/ ton) of uncalcined clay processed; OR the average uncontrolled HF emissions must be reduced by at least 90 percent; and i. Verifying at least once each 8 hour shift that lime is free flowing by means of a visual check, checking the output of a load cell, carrier gas/ lime flow indicator, or carrier gas pressure drop measurement system; and b. The average HCl emissions must not exceed 0.091 kg/ Mg ( 0.18 lb/ ton) of uncalcined clay processed; OR the average uncontrolled HCl emissions must be reduced by at least 30 percent. ii. Recording feeder setting daily to verify that the feeder setting is at or above the level established during the most recent performance test; and VerDate Jan< 31> 2003 14: 42 Apr 15, 2003 Jkt 200001 PO 00000 Frm 00048 Fmt 4701 Sfmt 4700 E:\ FR\ FM\ 16APR2. SGM 16APR2 18777 Federal Register / Vol. 68, No. 73 / Wednesday, April 16, 2003 / Rules and Regulations TABLE 7 TO SUBPART SSSSS TO PART 63.   CONTINUOUS COMPLIANCE WITH EMISSION LIMITS   Continued For . . . For the following emission limit . . . You must demonstrate continuous compliance by . . .

iii. Initiating corrective action within 1 hour of a bag leak detection system alarm AND completing corrective actions in accordance with the OM& M plan, AND operating and maintaining the fabric filter such that the alarm does not engage for more than 5 percent of the total operating time in a 6 month block reporting period. 11. Each affected kiln that is equipped with a wet scrubber. a. The average HF emissions must not exceed 0.019 kg/ Mg ( 0.038 lb/ ton) of uncalcined clay processed; OR the average uncontrolled HF emissions must be reduced by at least 90 percent; and i. Maintaining the pressure drop across the scrubber, liquid pH, and liquid flow rate at or above the minimum levels established during the most recent performance test; and b. The average HCl emissions must not exceed 0.091 kg/ Mg ( 0.18 lb/ ton) of uncalcined clay processed; OR the average uncontrolled HCl emissions must be reduced by at least 30 percent. ii. If chemicals are added to the scrubber liquid maintaining the average chemical feed rate at or above the minimum chemical feed rate established during the most recent performance test.

As stated in § 63.9810, you must show continuous compliance with the operating limits for affected sources according to the following table:

TABLE 8 TO SUBPART SSSSS OF PART 63.   CONTINUOUS COMPLIANCE WITH OPERATING LIMITS For . . . For the following operating limit . . . You must demonstrate continuous compliance by . . .

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 ii. Conducting annually an inspection of all duct work, vents, and capture devices to verify that no leaks exist and that the capture device is operating such that all emissions are properly vented to the control device in accordance with the OM& M plan. 2. Each affected continuous kiln that is equipped with a 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. 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; and iii. Minimizing the duration of all periods of scheduled maintenance of the kiln control device when the kiln is operating and the control device is out of service. 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 iii. Maintaining the 3 hour block average organic HAP processing rate at or below the maximum organic HAP processing rate established during the most recent performance test. 5. Continuous process units that are equipped with a thermal 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 iii. Maintaining the 3 hour block average thermal oxidizer combustion chamber temperature at or above the minimum allowable operating temperature established during the most recent performance test; and iv. Reporting, in accordance with § 63.9814( e), any 3 hour block average operating temperature measurements below the minimum allowable thermal oxidizer combustion chamber operating temperature established during the most recent performance test. 6. Continuous process units that are equipped with a catalytic 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 iii. Maintaining the 3 hour block average temperature at the inlet of the catalyst bed at or above the minimum allowable catalyst bed inlet temperature established during the most recent performance test; and iv. Reporting, in accordance with § 63.9814( e), any 3 hour block average catalyst bed inlet temperature measurements below the minimum allowable catalyst bed inlet temperature established during the most recent performance; and v. Checking the activity level of the catalyst at least every 12 months and taking any necessary corrective action, such as replacing the catalyst, to ensure that the catalyst is performing as designed. 7. Each affected batch process 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 iii. Recording the process cycle time for each batch cycle; and iv. Maintaining the organic HAP processing rate at or below the maximum organic HAP processing rate established during the most recent performance test.

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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 iii. From the start of each batch cycle until 3 hours have passed since the process unit reached maximum temperature, maintaining the hourly average operating temperature in the thermal oxidizer combustion chamber at or above the minimum allowable operating temperature established for the corresponding period during the most recent performance test, as determined according to item 11 of Table 4 to this subpart; and iv. For each subsequent hour of the batch cycle, maintaining the hourly average operating temperature in the thermal oxidizer combustion chamber at or above the minimum allowable operating temperature established for the corresponding hour during the most recent performance test, as specified in item 13 of Table 4 to this subpart; and v. Reporting, in accordance with § 63.9814( e), any temperature measurements below the minimum allowable thermal oxidizer combustion chamber temperature measured during the most recent performance test. 9. Batch process units that are equipped with a catalytic 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 iii. From the start of each batch cycle until 3 hours have passed since the process unit reached maximum temperature, maintaining the hourly average operating temperature at the inlet of the catalyst bed at or above the minimum allowable bed inlet temperature established for the corresponding period during the most recent performance test, as determined according to item 12 of Table 4 to this subpart; and iv. For each subsequent hour of the batch cycle, maintaining the hourly average operating temperature at the inlet of the catalyst bed at or above the minimum allowable bed inlet temperature established for the corresponding hour during the most recent performance test, as specified in item 13 of Table 4 to this subpart; and v. Reporting, in accordance with § 63.9814( e), any catalyst bed inlet temperature measurements below the minimum allowable bed inlet temperature measured during the most recent performance test; and vi. Checking the activity level of the catalyst at least every 12 months and taking any necessary corrective action, such as replacing the catalyst, to ensure that the catalyst is performing as designed. 10. Each new kiln that is used to process clay refractory products. As specified in items 11 through 13 of this table. Satisfying the applicable requirements specified in items 11 through 13 of this table. 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 VerDate Jan< 31> 2003 14: 42 Apr 15, 2003 Jkt 200001 PO 00000 Frm 00051 Fmt 4701 Sfmt 4700 E:\ FR\ FM\ 16APR2. SGM 16APR2 18780 Federal Register / Vol. 68, No. 73 / Wednesday, April 16, 2003 / Rules and Regulations TABLE 8 TO SUBPART SSSSS OF PART 63.   CONTINUOUS COMPLIANCE WITH OPERATING LIMITS   Continued For . . . For the following operating limit . . . You must demonstrate continuous compliance by . . .

iii. Maintaining the 3 hour block average pressure drop across the DLA at or above the minimum pressure drop established during the most recent performance test. b. Maintain free flowing limestone in the feed hopper, silo, and DLA. Verifying that the limestone hopper has an adequate amount of free flowing limestone by performing a daily visual check of the limestone hopper. c. Maintain the limestone feeder setting at or above the level established during the most recent performance 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. 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. 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. 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. 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 iii. Maintaining the 3 hour block average scrubber pressure drop at or above the minimum pressure drop established during the most recent performance test. b. Maintain the average scrubber liquid pH for each 3 hour block period at or above the minimum scrubber liquid pH established during the most recent performance 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 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 iii. Maintaining the 3 hour block average scrubber liquid flow rate at or above the minimum scrubber liquid flow rate established during the most recent performance test. d. If chemicals are added to the scrubber liquid maintain the average scrubber chemical feed rate for each 3 hour block period at or above the minimum scrubber chemical feed rate established during the most recent performance 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 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.

As stated in § 63.9810, you must show continuous compliance with the work practice standards for affected sources according to the following table:

TABLE 9 TO SUBPART SSSSS OF PART 63.   CONTINUOUS COMPLIANCE WITH WORK PRACTICE STANDARDS For . . . For the following work practice standard . . . You must demonstrate continuous compliance by . . .

1. Each affected source listed in Table 3 to this subpart. Each applicable work practice requirement listed in Table 3 to this subpart. i. Performing each applicable work practice standard listed in Table 3 to this subpart; and ii. Maintaining records that document the method and frequency for complying with each applicable work practice standard listed in Table 3 to this subpart, as required by § § 63.10( b) and 63.9816( c)( 2). 2. Each basket or container that is used for holding fired refractory shapes in an existing shape preheater and autoclave during the pitch impregnation process. Control POM emissions from any affected shape preheater. i. Controlling emissions from the volatilization of residual pitch by implementing one of the work practice standards listed in item 1 of Table 3 to this subpart; and ii. Recording the date and cleaning method each time you clean an affected basket or container. 3. Each new or existing pitch working tank ....... Control POM emissions ................................... Capturing and venting emissions from the affected pitch working tank to the control device that is used to control emissions from an affected defumer or coking oven, or to a thermal or catalytic oxidizer that is comparable to the control device used on an affected defumer or coking oven. 4. Each new or existing chromium refractory products kiln. Minimize fuel based HAP emissions ............... i. Using natural gas, or equivalent, as the kiln fuel at all times except during periods of natural gas curtailment or supply interruption and ii. If you intend to use an alternative fuel, submitting a notification of alternative fuel use within 48 hours of the declaration of a period of natural gas curtailment or supply interruption, as defined in § 63.9824; and iii. Submitting a report of alternative fuel use within 10 working days after terminating the use of the alternative fuel, as specified in § 63.9814( g). 5. Each existing clay refractory products kiln .... Minimize fuel based HAP emissions ............... i. Using natural gas, or equivalent, as the kiln fuel at all times except during periods of natural gas curtailment or supply interruption and VerDate Jan< 31> 2003 14: 42 Apr 15, 2003 Jkt 200001 PO 00000 Frm 00053 Fmt 4701 Sfmt 4700 E:\ FR\ FM\ 16APR2. SGM 16APR2 18782 Federal Register / Vol. 68, No. 73 / Wednesday, April 16, 2003 / Rules and Regulations TABLE 9 TO SUBPART SSSSS OF PART 63.   CONTINUOUS COMPLIANCE WITH WORK PRACTICE STANDARDS   Continued For . . . For the following work practice standard . . . You must demonstrate continuous compliance by . . .

ii. If you intend to use an alternative fuel, submitting a notification of alternative fuel use within 48 hours of the declaration of a period of natural gas curtailment or supply interruption, as defined in § 63.9824; and iii. Submitting a report of alternative fuel use within 10 working days after terminating the use of the alternative fuel, as specified in § 63.9814( g).

As stated in § 63.9814, you must comply with the requirements for reports in the following table:

TABLE 10 TO SUBPART SSSSS OF PART 63.   REQUIREMENTS FOR REPORTS You must submit a( n) . . . The report must contain . . . You must submit the report . . .

1. Compliance report .......................................... The information in § 63.9814( c) through ( f) ..... Semiannually according to the requirements in § 63.9814( a) through ( f). 2. Immediate startup, shutdown, and malfunction report if you had a startup, shutdown, or malfunction during the reporting period that is not consistent with your SSMP. a. Actions taken for the event .......................... By fax or telephone within 2 working days after starting actions inconsistent with the plan.

b. The information in § 63.10( d)( 5)( ii) .............. By letter within 7 working days after the end of the event unless you have made alternative arrangements with the permitting authority 3. Report of alternative fuel use ......................... The information in § 63.9814( g) and items 4 and 5 of Table 9 to this subpart. If you are subject to the work practice standard specified in item 3 or 4 of Table 3 to this subpart, and you use an alternative fuel in the affected kiln, by letter within 10 working days after terminating the use of the alternative fuel.

As stated in § 63.9820, you must comply with the applicable General Provisions requirements according to the following table:

TABLE 11 TO SUBPART SSSSS OF PART 63.   APPLICABILITY OF GENERAL PROVISIONS TO SUBPART SSSSS Citation Subject Brief description Applies to subpart SSSSS § 63.1 .................... Applicability ........................................................ ............................................................................ Yes. § 63.2 .................... Definitions .......................................................... ............................................................................ Yes. § 63.3 .................... Units and Abbreviations ..................................... ............................................................................ 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 ......................................................... ............................................................................ Yes. § 63.6( b)( 6) ............ [ Reserved] § 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 days of effective date unless compliance extension. Yes.

§ 63.6( c)( 3)   ( 4) ..... [ Reserved] § 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.

VerDate Jan< 31> 2003 14: 42 Apr 15, 2003 Jkt 200001 PO 00000 Frm 00054 Fmt 4701 Sfmt 4700 E:\ FR\ FM\ 16APR2. SGM 16APR2 18783 Federal Register / Vol. 68, No. 73 / Wednesday, April 16, 2003 / Rules and Regulations TABLE 11 TO SUBPART SSSSS OF PART 63.   APPLICABILITY OF GENERAL PROVISIONS TO SUBPART SSSSS   Continued Citation Subject Brief description Applies to subpart SSSSS § 63.6( d) ................ [ Reserved] § 63.6( e)( 1)   ( 2) ..... Operation & Maintenance .................................. Operate to minimize emissions at all times; correct malfunctions as soon as practicable; requirements independently enforceable; information Administrator will use to determine if operation and maintenance requirements were met. Yes.

§ 63.6( e)( 3) ............ Startup, Shutdown, and Malfunction Plan ( SSMP). ............................................................................ Yes.

§ 63.6( f)( 1) ............. Compliance Except During SSM ....................... You must comply with emission standards at all times except during SSM. Yes.

§ 63.6( f)( 2)   ( 3) ...... Methods for Determining Compliance ............... Compliance based on performance test, operation and maintenance plans, records, inspection Yes.

§ 63.6( g)( 1)   ( 3) ..... Alternative Standard .......................................... Procedures for getting an alternative standard. Yes. § 63.6( h)( 1)   ( 9) ..... Opacity/ Visible Emission ( VE) Standards ......... ............................................................................ Not applicable. § 63.6( i)( 1)   ( 14) .... 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; must conduct 180 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( b)( 1) ............ Notification of Performance Test ....................... Must notify Administrator 60 days before the test. Yes.

§ 63.7( b)( 2) ............ Notification of Rescheduling .............................. Must notify Administrator 5 days before scheduled date and provide rescheduled date. Yes.

§ 63.7( c) ................ Quality Assurance/ Test Plan ............................. Requirements; test plan approval procedures; performance audit requirements; internal and external QA procedures for testing. Yes.

§ 63.7( d) ................ Testing Facilities ................................................ ............................................................................ Yes. § 63.7( e)( 1) ............ Conditions for Conducting Performance Tests Performance tests must be conducted under representative conditions; cannot conduct performance tests during SSM; not a violation to exceed standard during SSM. No, § 63.9800 specifies requirements; Yes; Yes.

§ 63.7( e)( 2) ............ Conditions for Conducting Performance Tests Must conduct according to subpart and EPA test methods unless Administrator approves alternative. Yes.

§ 63.7( e)( 3) ............ Test Run Duration ............................................. Must have three test runs of at least 1 hour each; compliance is based on arithmetic mean of three runs; conditions when data from an additional test run can be used. Yes; Yes, except where specified in § 63.9800 for batch process sources; Yes. § 63.7( f) ................. Alternative Test Method ..................................... ............................................................................ Yes. § 63.7( g) ................ Performance Test Data Analysis ....................... ............................................................................ Yes. § 63.7( h) ................ Waiver of Test ................................................... ............................................................................ Yes. § 63.8( a)( 1) ............ Applicability of Monitoring Requirements .......... ............................................................................ Yes. § 63.8( a)( 2) ............ Performance Specifications ............................... Performance Specifications in appendix B of 40 CFR part 60 apply. Yes.

§ 63.8( a)( 3) ............ [ Reserved] § 63.8( a)( 4) ............ Monitoring with Flares ....................................... ............................................................................ 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. Yes.

§ 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 is complying with operation and maintenance requirements Yes.

§ 63.8( c)( 2)   ( 3) ..... Monitoring System Installation ........................... Must install to get representative emission and parameter measurements. Yes.

§ 63.8( c)( 4) ............ CMS Requirements ........................................... ............................................................................ No, § 63.9808 specifies requirements. § 63.8( c)( 5) ............ COMS Minimum Procedures ............................. ............................................................................ Not applicable.

VerDate Jan< 31> 2003 14: 42 Apr 15, 2003 Jkt 200001 PO 00000 Frm 00055 Fmt 4701 Sfmt 4700 E:\ FR\ FM\ 16APR2. SGM 16APR2 18784 Federal Register / Vol. 68, No. 73 / Wednesday, April 16, 2003 / Rules and Regulations TABLE 11 TO SUBPART SSSSS OF PART 63.   APPLICABILITY OF GENERAL PROVISIONS TO SUBPART SSSSS   Continued Citation Subject Brief description Applies to subpart SSSSS § 63.8( c)( 6) ............ CMS Requirements ........................................... ............................................................................ Applies only to sources required to install and operate a THC CEMS. § 63.8( c)( 7)( i)( A) .... CMS Requirements ........................................... ............................................................................ Applies only to sources required to install and operate a THC CEMS. § 63.8( c)( 7)( i)( B) .... CMS Requirements ........................................... ............................................................................ Applies only to sources required to install and operate a THC CEMS. § 63.8( c)( 7)( i)( C) .... CMS Requirements ........................................... ............................................................................ Not applicable. § 63.8( c)( 7)( ii) ........ CMS Requirements ........................................... Corrective action required when CMS is out of control. Yes.

§ 63.8( c)( 8) ............ CMS Requirements ........................................... ............................................................................ Yes. § 63.8( d) ................ CMS Quality Control .......................................... ............................................................................ Applies only to sources required to install and operate a THC CEMS. § 63.8( e) ................ CMS Performance Evaluation ........................... ............................................................................ Applies only to sources required to install and operate a THC CEMS. § 63.8( f)( 1)   ( 5) ...... Alternative Monitoring Method ........................... ............................................................................ Yes. § 63.8( f)( 6) ............. Alternative to Relative Accuracy Test ............... ............................................................................ Yes. § 63.8( g) ................ Data Reduction .................................................. ............................................................................ Applies only to sources required to install and operate a THC CEMS. § 63.9( a) ................ Notification Requirements .................................. ............................................................................ Yes. § 63.9( b)( 1)   ( 5) ..... Initial Notifications .............................................. ............................................................................ Yes. § 63.9( c) ................ Request for Compliance Extension ................... ............................................................................ Yes. § 63.9( d) ................ Notification of Special Compliance Requirements for New Source. ............................................................................ Yes.

§ 63.9( e) ................ Notification of Performance Test ....................... Notify Administrator 60 days prior ..................... Yes. § 63.9( f) ................. Notification of VE/ Opacity Test .......................... ............................................................................ Not applicable. § 63.9( g) ................ Additional Notifications When Using CMS ........ ............................................................................ Applies only to sources required to install and operate a THC CEMS. § 63.9( h) ................ Notification of Compliance Status ..................... ............................................................................ Yes. § 63.9( i) ................. Adjustment of Submittal Deadlines ................... ............................................................................ Yes. § 63.9( j) ................. Change in Previous Information ........................ ............................................................................ Yes. § 63.10( a) .............. Recordkeeping/ Reporting .................................. ............................................................................ Yes. § 63.10( b)( 1) .......... Recordkeeping/ Reporting .................................. ............................................................................ Yes. § 63.10( b)( 2)( i)   ( v) Records Related to Startup, Shutdown, and Malfunction. ............................................................................ Yes.

§ 63.10( b)( 2)( vi) and ( x   xi). CMS Records .................................................... ............................................................................ Yes.

§ 63.10( b)( 2)( vii)   ( ix). Records .............................................................. Measurements to demonstrate compliance with emission limitations; performance test, performance evaluation, and visible emission observation results; measurements to determine conditions of performance tests and performance evaluations. Yes.

§ 63.10( b)( 2)( xii) .... Records .............................................................. Records when under waiver .............................. Yes. § 63.10( b)( 2)( xiii) ... Records .............................................................. Records when using alternative to relative accuracy test. Not applicable.

§ 63.10( b)( 2)( xiv) ... Records .............................................................. All documentation supporting Initial Notification and Notification of Compliance Status. Yes.

§ 63.10( b)( 3) .......... Records .............................................................. Applicability Determinations ............................... Yes. § 63.10( c)( 1)   ( 6), ( 9)   ( 15). Records .............................................................. Additional Records for CMS .............................. Not applicable.

§ 63.10( c)( 7)   ( 8) ... Records .............................................................. Records of excess emissions and parameter monitoring exceedances for CMS. No, § 63.9816 specifies requirements. § 63.10( d)( 1) .......... General Reporting Requirements ...................... Requirements for reporting ................................ Yes. § 63.10( d)( 2) .......... Report of Performance Test Results ................. When to submit to Federal or State authority ... Yes. § 63.10( d)( 3) .......... Reporting Opacity or VE Observations ............. ............................................................................ Not applicable.

VerDate Jan< 31> 2003 14: 42 Apr 15, 2003 Jkt 200001 PO 00000 Frm 00056 Fmt 4701 Sfmt 4700 E:\ FR\ FM\ 16APR2. SGM 16APR2 18785 Federal Register / Vol. 68, No. 73 / Wednesday, April 16, 2003 / Rules and Regulations TABLE 11 TO SUBPART SSSSS OF PART 63.   APPLICABILITY OF GENERAL PROVISIONS TO SUBPART SSSSS   Continued Citation Subject Brief description Applies to subpart SSSSS § 63.10( d)( 4) .......... Progress Reports ............................................... Must submit progress reports on schedule if under compliance extension. Yes.

§ 63.10( d)( 5) .......... Startup, Shutdown, and Malfunction Reports .... Contents and submission .................................. Yes. § 63.10( e)( 1)   ( 2) ... Additional CMS Reports .................................... ............................................................................ Applies only to sources required to install and operate a THC CEMS. § 63.10( e)( 3) .......... Reports .............................................................. ............................................................................ No, § 63.9814 specifies requirements. § 63.10( e)( 4) .......... Reporting COMS data ....................................... ............................................................................ Not applicable. § 63.10( f) ............... Waiver for Recordkeeping/ Reporting ................ ............................................................................ Yes. § 63.11 .................. Flares ................................................................. ............................................................................ Not applicable. § 63.12 .................. Delegation .......................................................... ............................................................................ Yes. § 63.13 .................. Addresses .......................................................... ............................................................................ Yes. § 63.14 .................. Incorporation by Reference ............................... ............................................................................ Yes. § 63.15 .................. Availability of Information ................................... ............................................................................ Yes.

[ FR Doc. 03   5622 Filed 4   15   03; 8: 45 am]

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