§ 63.1343 What standards apply to my kilns, clinker coolers, raw material dryers, and open clinker storage piles?
(a) General. The provisions in this section apply to each kiln and any alkali bypass associated with that kiln, clinker cooler, raw material dryer, and open clinker storage pile. All D/F, HCl, and total hydrocarbon (THC) emissions limit are on a dry basis. The D/F, HCl, and THC limits for kilns are corrected to 7 percent oxygen. All THC emissions limits are measured as propane. Standards for mercury and THC are based on a rolling 30-day average. If using a CEMS to determine compliance with the HCl standard, this standard is based on a rolling 30-day average. You must ensure appropriate corrections for moisture are made when measuring flow rates used to calculate mercury emissions. The 30-day period means all operating hours within 30 consecutive kiln operating days excluding periods of startup and shutdown. All emissions limits for kilns, clinker coolers, and raw material dryers currently in effect that are superseded by the limits below continue to apply until the compliance date of the limits below, or until the source certifies compliance with the limits below, whichever is earlier.
(b) Kilns, clinker coolers, raw material dryers, raw mills, and finish mills. (1) The emissions limits for these sources are shown in Table 1.
Table 1—Emissions Limits for Kilns, Clinker Coolers, Raw Material Dryers, Raw and Finish Mills
If your source is a (an): | And the operating mode is: | And if is located at a: | Your emissions limits are: | And the units of the emissions limit are: | The oxygen correction factor is: |
---|---|---|---|---|---|
1. Existing kiln | Normal operation | Major or area source | PM 1 0.07 | lb/ton clinker | NA. |
D/F 2 0.2 | ng/dscm (TEQ) | 7 percent. | |||
Mercury 55 | lb/MM tons clinker | NA. | |||
THC 3 4 24 | ppmvd | 7 percent. | |||
2. Existing kiln | Normal operation | Major source | HCl 3 | ppmvd | 7 percent. |
3. Existing kiln | Startup and shutdown | Major or area source | Work practices (63.1346(g)) | NA | NA. |
4. New kiln | Normal operation | Major or area source | PM 1 0.02 | lb/ton clinker | NA. |
D/F 2 0.2 | ng/dscm (TEQ) | 7 percent. | |||
Mercury 21 | lb/MM tons clinker | NA. | |||
THC 3 4 24 | ppmvd | 7 percent. | |||
5. New kiln | Normal operation | Major source | HCl 3 | ppmvd | 7 percent. |
6. New kiln | Startup and shutdown | Major or area source | Work practices (63.1346(g)) | NA | NA. |
7. Existing clinker cooler | Normal operation | Major or area source | PM 0.07 | lb/ton clinker | NA. |
8. Existing clinker cooler | Startup and shutdown | Major or area source | Work practices (63.1348(b)(9)) | NA | NA. |
9. New clinker cooler | Normal operation | Major or area source | PM 0.02 | lb/ton clinker | NA. |
10. New clinker cooler | Startup and shutdown | Major or area source | Work practices (63.1348(b)(9)) | NA | NA. |
11. Existing or new raw material dryer | Normal operation | Major or area source | THC 3 4 24 | ppmvd | NA. |
12. Existing or new raw material dryer | Startup and shutdown | Major or area source | Work practices (63.1348(b)(9)) | NA | NA. |
13. Existing or new raw or finish mill | All operating modes | Major source | Opacity 10 | percent | NA. |