<?xml version="1.0"?>
<?xml-stylesheet type="text/xsl" href="cfr.xsl"?>
<CFRGRANULE xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:noNamespaceSchemaLocation="CFRMergedXML.xsd">
  <FDSYS>
    <CFRTITLE>40</CFRTITLE>
    <CFRTITLETEXT>Protection of Environment</CFRTITLETEXT>
    <VOL>14</VOL>
    <DATE>2015-07-01</DATE>
    <ORIGINALDATE>2014-07-01</ORIGINALDATE>
    <COVERONLY>true</COVERONLY>
    <TITLE>Emission Limits for Existing Boilers and Process Heaters</TITLE>
    <GRANULENUM>2</GRANULENUM>
    <HEADING>Table 2 to Subpart DDDDD of Part 63</HEADING>
    <ANCESTORS>
      <PARENT HEADING="Title 40" SEQ="4">Protection of Environment</PARENT>
      <PARENT HEADING="CHAPTER I" SEQ="3">ENVIRONMENTAL PROTECTION AGENCY (CONTINUED)</PARENT>
      <PARENT HEADING="SUBCHAPTER C" SEQ="2">AIR PROGRAMS (CONTINUED)</PARENT>
      <PARENT HEADING="PART 63" SEQ="1">NATIONAL EMISSION STANDARDS FOR HAZARDOUS AIR POLLUTANTS FOR SOURCE CATEGORIES (CONTINUED)</PARENT>
      <PARENT HEADING="Subpart DDDDD" SEQ="0">National Emission Standards for Hazardous Air Pollutants for Major Sources: Industrial, Commercial, and Institutional Boilers and Process Heaters</PARENT>
    </ANCESTORS>
  </FDSYS>
  <APPENDIX>
    <PRTPAGE P="196"/>
    <EAR>Pt. 63, Subpt. DDDDD, Table 2</EAR>
    <HD SOURCE="HED">Table 2 to Subpart DDDDD of Part 63—Emission Limits for Existing Boilers and Process Heaters</HD>
    <P>As stated in § 63.7500, you must comply with the following applicable emission limits:</P>
    <GPOTABLE CDEF="s50,r50,r50,r50,r50" COLS="5" OPTS="L2">
      <TDESC>[Units with heat input capacity of 10 million Btu per hour or greater]</TDESC>
      <BOXHD>
        <CHED H="1" O="L">If your boiler or process heater is in this subcategory . . .</CHED>
        <CHED H="1" O="L">For the following<LI>pollutants . . .</LI>
        </CHED>
        <CHED H="1" O="L">The emissions must not exceed the following emission limits, except during startup and shutdown . . .</CHED>
        <CHED H="1" O="L">The emissions must not exceed the following alternative output-based limits, except during startup and<LI>shutdown . . .</LI>
        </CHED>
        <CHED H="1" O="L">Using this specified sampling volume or test run<LI>duration . . .</LI>
        </CHED>
      </BOXHD>
      <ROW>
        <ENT I="01">1. Units in all subcategories designed to burn solid fuel</ENT>
        <ENT>a. HCl</ENT>
        <ENT>2.2E-02 lb per MMBtu of heat input</ENT>
        <ENT>2.5E-02 lb per MMBtu of steam output or 0.27 lb per MWh</ENT>
        <ENT>For M26A, Collect a minimum of 1 dscm per run; for M26, collect a minimum of 120 liters per run.</ENT>
      </ROW>
      <ROW>
        <ENT I="22"> </ENT>
        <ENT>b. Mercury</ENT>
        <ENT>5.7E-06 lb per MMBtu of heat input</ENT>
        <ENT>6.4E-06 lb per MMBtu of steam output or 7.3E-05 lb per MWh</ENT>
        <ENT>For M29, collect a minimum of 3 dscm per run; for M30A or M30B, collect a minimum sample as specified in the method; for ASTM D6784 <SU>b</SU> collect a minimum of 3 dscm.</ENT>
      </ROW>
      <ROW>
        <ENT I="01">2. Units design to burn coal/solid fossil fuel</ENT>
        <ENT>a. Filterable PM (or TSM)</ENT>
        <ENT>4.0E-02 lb per MMBtu of heat input; or (5.3E-05 lb per MMBtu of heat input)</ENT>
        <ENT>4.2E-02 lb per MMBtu of steam output or 4.9E-01 lb per MWh; or (5.6E-05 lb per MMBtu of steam output or 6.5E-04 lb per MWh)</ENT>
        <ENT>Collect a minimum of 2 dscm per run.</ENT>
      </ROW>
      <ROW>
        <ENT I="01">3. Pulverized coal boilers designed to burn coal/solid fossil fuel</ENT>
        <ENT>a. CO (or CEMS)</ENT>
        <ENT>130 ppm by volume on a dry basis corrected to 3 percent oxygen, 3-run average; or (320 ppm by volume on a dry basis corrected to 3 percent oxygen, 30-day rolling average)</ENT>
        <ENT>0.11 lb per MMBtu of steam output or 1.4 lb per MWh; 3-run average</ENT>
        <ENT>1 hr minimum sampling time.</ENT>
      </ROW>
      <ROW>
        <ENT I="01">4. Stokers designed to burn coal/solid fossil fuel</ENT>
        <ENT>a. CO (or CEMS)</ENT>
        <ENT>160 ppm by volume on a dry basis corrected to 3 percent oxygen, 3-run average; or (340 ppm by volume on a dry basis corrected to 3 percent oxygen, 30-day rolling average)</ENT>
        <ENT>0.14 lb per MMBtu of steam output or 1.7 lb per MWh; 3-run average</ENT>
        <ENT>1 hr minimum sampling time.</ENT>
      </ROW>
      <ROW>
        <ENT I="01">5. Fluidized bed units designed to burn coal/solid fossil fuel</ENT>
        <ENT>a. CO (or CEMS)</ENT>
        <ENT>130 ppm by volume on a dry basis corrected to 3 percent oxygen, 3-run average; or (230 ppm by volume on a dry basis corrected to 3 percent oxygen, 30-day rolling average)</ENT>
        <ENT>0.12 lb per MMBtu of steam output or 1.4 lb per MWh; 3-run average</ENT>
        <ENT>1 hr minimum sampling time.</ENT>
      </ROW>
      <ROW>
        <ENT I="01">6. Fluidized bed units with an integrated heat exchanger designed to burn coal/solid fossil fuel</ENT>
        <ENT>a. CO (or CEMS)</ENT>
        <ENT>140 ppm by volume on a dry basis corrected to 3 percent oxygen, 3-run average; or (150 ppm by volume on a dry basis corrected to 3 percent oxygen, 30-day rolling average)</ENT>
        <ENT>1.3E-01 lb per MMBtu of steam output or 1.5 lb per MWh; 3-run average</ENT>
        <ENT>1 hr minimum sampling time.</ENT>
      </ROW>
      <ROW>
        <PRTPAGE P="197"/>
        <ENT I="01">7. Stokers/sloped grate/others designed to burn wet biomass fuel</ENT>
        <ENT>a. CO (or CEMS)</ENT>
        <ENT>1,500 ppm by volume on a dry basis corrected to 3 percent oxygen, 3-run average; or (720 ppm by volume on a dry basis corrected to 3 percent oxygen, 30-day rolling average)</ENT>
        <ENT>1.4 lb per MMBtu of steam output or 17 lb per MWh; 3-run average</ENT>
        <ENT>1 hr minimum sampling time.</ENT>
      </ROW>
      <ROW>
        <ENT I="22"> </ENT>
        <ENT>b. Filterable PM (or TSM)</ENT>
        <ENT>3.7E-02 lb per MMBtu of heat input; or (2.4E-04 lb per MMBtu of heat input)</ENT>
        <ENT>4.3E-02 lb per MMBtu of steam output or 5.2E-01 lb per MWh; or (2.8E-04 lb per MMBtu of steam output or 3.4E-04 lb per MWh)</ENT>
        <ENT>Collect a minimum of 2 dscm per run.</ENT>
      </ROW>
      <ROW>
        <ENT I="01">8. Stokers/sloped grate/others designed to burn kiln-dried biomass fuel</ENT>
        <ENT>a. CO</ENT>
        <ENT>460 ppm by volume on a dry basis corrected to 3 percent oxygen</ENT>
        <ENT>4.2E-01 lb per MMBtu of steam output or 5.1 lb per MWh</ENT>
        <ENT>1 hr minimum sampling time.</ENT>
      </ROW>
      <ROW>
        <ENT I="22"> </ENT>
        <ENT>b. Filterable PM (or TSM)</ENT>
        <ENT>3.2E-01 lb per MMBtu of heat input; or (4.0E-03 lb per MMBtu of heat input)</ENT>
        <ENT>3.7E-01 lb per MMBtu of steam output or 4.5 lb per MWh; or (4.6E-03 lb per MMBtu of steam output or 5.6E-02 lb per MWh)</ENT>
        <ENT>Collect a minimum of 1 dscm per run.</ENT>
      </ROW>
      <ROW>
        <ENT I="01">9. Fluidized bed units designed to burn biomass/bio-based solid</ENT>
        <ENT>a. CO (or CEMS)</ENT>
        <ENT>470 ppm by volume on a dry basis corrected to 3 percent oxygen, 3-run average; or (310 ppm by volume on a dry basis corrected to 3 percent oxygen, 30-day rolling average)</ENT>
        <ENT>4.6E-01 lb per MMBtu of steam output or 5.2 lb per MWh; 3-run average</ENT>
        <ENT>1 hr minimum sampling time.</ENT>
      </ROW>
      <ROW>
        <ENT I="22"> </ENT>
        <ENT>b. Filterable PM (or TSM)</ENT>
        <ENT>1.1E-01 lb per MMBtu of heat input; or (1.2E-03 lb per MMBtu of heat input)</ENT>
        <ENT>1.4E-01 lb per MMBtu of steam output or 1.6 lb per MWh; or (1.5E-03 lb per MMBtu of steam output or 1.7E-02 lb per MWh)</ENT>
        <ENT>Collect a minimum of 1 dscm per run.</ENT>
      </ROW>
      <ROW>
        <ENT I="01">10. Suspension burners designed to burn biomass/bio-based solid</ENT>
        <ENT>a. CO (or CEMS)</ENT>
        <ENT>2,400 ppm by volume on a dry basis corrected to 3 percent oxygen, 3-run average; or (2,000 ppm by volume on a dry basis corrected to 3 percent oxygen, 10-day rolling average)</ENT>
        <ENT>1.9 lb per MMBtu of steam output or 27 lb per MWh; 3-run average</ENT>
        <ENT>1 hr minimum sampling time.</ENT>
      </ROW>
      <ROW>
        <ENT I="22"> </ENT>
        <ENT>b. Filterable PM (or TSM)</ENT>
        <ENT>5.1E-02 lb per MMBtu of heat input; or (6.5E-03 lb per MMBtu of heat input)</ENT>
        <ENT>5.2E-02 lb per MMBtu of steam output or 7.1E-01 lb per MWh; or (6.6E-03 lb per MMBtu of steam output or 9.1E-02 lb per MWh)</ENT>
        <ENT>Collect a minimum of 2 dscm per run.</ENT>
      </ROW>
      <ROW>
        <PRTPAGE P="198"/>
        <ENT I="01">11. Dutch Ovens/Pile burners designed to burn biomass/bio-based solid</ENT>
        <ENT>a. CO (or CEMS)</ENT>
        <ENT>770 ppm by volume on a dry basis corrected to 3 percent oxygen, 3-run average; or (520 ppm by volume on a dry basis corrected to 3 percent oxygen, 10-day rolling average)</ENT>
        <ENT>8.4E-01 lb per MMBtu of steam output or 8.4 lb per MWh; 3-run average</ENT>
        <ENT>1 hr minimum sampling time.</ENT>
      </ROW>
      <ROW>
        <ENT I="22"> </ENT>
        <ENT>b. Filterable PM (or TSM)</ENT>
        <ENT>2.8E-01 lb per MMBtu of heat input; or (2.0E-03 lb per MMBtu of heat input)</ENT>
        <ENT>3.9E-01 lb per MMBtu of steam output or 3.9 lb per MWh; or (2.8E-03 lb per MMBtu of steam output or 2.8E-02 lb per MWh)</ENT>
        <ENT>Collect a minimum of 1 dscm per run.</ENT>
      </ROW>
      <ROW>
        <ENT I="01">12. Fuel cell units designed to burn biomass/bio-based solid</ENT>
        <ENT>a. CO</ENT>
        <ENT>1,100 ppm by volume on a dry basis corrected to 3 percent oxygen</ENT>
        <ENT>2.4 lb per MMBtu of steam output or 12 lb per MWh</ENT>
        <ENT>1 hr minimum sampling time.</ENT>
      </ROW>
      <ROW>
        <ENT I="22"> </ENT>
        <ENT>b. Filterable PM (or TSM)</ENT>
        <ENT>2.0E-02 lb per MMBtu of heat input; or (5.8E-03 lb per MMBtu of heat input)</ENT>
        <ENT>5.5E-02 lb per MMBtu of steam output or 2.8E-01 lb per MWh; or (1.6E-02 lb per MMBtu of steam output or 8.1E-02 lb per MWh)</ENT>
        <ENT>Collect a minimum of 2 dscm per run.</ENT>
      </ROW>
      <ROW>
        <ENT I="01">13. Hybrid suspension grate units designed to burn biomass/bio-based solid</ENT>
        <ENT>a. CO (or CEMS)</ENT>
        <ENT>2,800 ppm by volume on a dry basis corrected to 3 percent oxygen, 3-run average; or (900 ppm by volume on a dry basis corrected to 3 percent oxygen, 30-day rolling average)</ENT>
        <ENT>2.8 lb per MMBtu of steam output or 31 lb per MWh; 3-run average</ENT>
        <ENT>1 hr minimum sampling time.</ENT>
      </ROW>
      <ROW>
        <ENT I="22"> </ENT>
        <ENT>b. Filterable PM (or TSM)</ENT>
        <ENT>4.4E-01 lb per MMBtu of heat input; or (4.5E-04 lb per MMBtu of heat input)</ENT>
        <ENT>5.5E-01 lb per MMBtu of steam output or 6.2 lb per MWh; or (5.7E-04 lb per MMBtu of steam output or 6.3E-03 lb per MWh)</ENT>
        <ENT>Collect a minimum of 1 dscm per run.</ENT>
      </ROW>
      <ROW>
        <ENT I="01">14. Units designed to burn liquid fuel</ENT>
        <ENT>a. HCl</ENT>
        <ENT>1.1E-03 lb per MMBtu of heat input</ENT>
        <ENT>1.4E-03 lb per MMBtu of steam output or 1.6E-02 lb per MWh</ENT>
        <ENT>For M26A, collect a minimum of 2 dscm per run; for M26, collect a minimum of 240 liters per run.</ENT>
      </ROW>
      <ROW>
        <ENT I="22"> </ENT>
        <ENT>b. Mercury</ENT>
        <ENT>2.0E-06 lb per MMBtu of heat input</ENT>
        <ENT>2.5E-06 lb per MMBtu of steam output or 2.8E-05 lb per MWh</ENT>
        <ENT>For M29, collect a minimum of 3 dscm per run; for M30A or M30B collect a minimum sample as specified in the method, for ASTM D6784 <SU>b</SU> collect a minimum of 2 dscm.</ENT>
      </ROW>
      <ROW>
        <ENT I="01">15. Units designed to burn heavy liquid fuel</ENT>
        <ENT>a. CO</ENT>
        <ENT>130 ppm by volume on a dry basis corrected to 3 percent oxygen, 3-run average</ENT>
        <ENT>0.13 lb per MMBtu of steam output or 1.4 lb per MWh; 3-run average</ENT>
        <ENT>1 hr minimum sampling time.</ENT>
      </ROW>
      <ROW>
        <PRTPAGE P="199"/>
        <ENT I="22"> </ENT>
        <ENT>b. Filterable PM (or TSM)</ENT>
        <ENT>6.2E-02 lb per MMBtu of heat input; or (2.0E-04 lb per MMBtu of heat input)</ENT>
        <ENT>7.5E-02 lb per MMBtu of steam output or 8.6E-01 lb per MWh; or (2.5E-04 lb per MMBtu of steam output or 2.8E-03 lb per MWh)</ENT>
        <ENT>Collect a minimum of 1 dscm per run.</ENT>
      </ROW>
      <ROW>
        <ENT I="01">16. Units designed to burn light liquid fuel</ENT>
        <ENT>a. CO</ENT>
        <ENT>130 ppm by volume on a dry basis corrected to 3 percent oxygen</ENT>
        <ENT>0.13 lb per MMBtu of steam output or 1.4 lb per MWh</ENT>
        <ENT>1 hr minimum sampling time.</ENT>
      </ROW>
      <ROW>
        <ENT I="22"> </ENT>
        <ENT>b. Filterable PM (or TSM)</ENT>
        <ENT>7.9E-03 lb per MMBtu of heat input; or (6.2E-05 lb per MMBtu of heat input)</ENT>
        <ENT>9.6E-03 lb per MMBtu of steam output or 1.1E-01 lb per MWh; or (7.5E-05 lb per MMBtu of steam output or 8.6E-04 lb per MWh)</ENT>
        <ENT>Collect a minimum of 3 dscm per run.</ENT>
      </ROW>
      <ROW>
        <ENT I="01">17. Units designed to burn liquid fuel that are non-continental units</ENT>
        <ENT>a. CO</ENT>
        <ENT>130 ppm by volume on a dry basis corrected to 3 percent oxygen, 3-run average based on stack test</ENT>
        <ENT>0.13 lb per MMBtu of steam output or 1.4 lb per MWh; 3-run average</ENT>
        <ENT>1 hr minimum sampling time.</ENT>
      </ROW>
      <ROW>
        <ENT I="22"> </ENT>
        <ENT>b. Filterable PM (or TSM)</ENT>
        <ENT>2.7E-01 lb per MMBtu of heat input; or (8.6E-04 lb per MMBtu of heat input)</ENT>
        <ENT>3.3E-01 lb per MMBtu of steam output or 3.8 lb per MWh; or (1.1E-03 lb per MMBtu of steam output or 1.2E-02 lb per MWh)</ENT>
        <ENT>Collect a minimum of 2 dscm per run.</ENT>
      </ROW>
      <ROW>
        <ENT I="01">18. Units designed to burn gas 2 (other) gases</ENT>
        <ENT>a. CO</ENT>
        <ENT>130 ppm by volume on a dry basis corrected to 3 percent oxygen</ENT>
        <ENT>0.16 lb per MMBtu of steam output or 1.0 lb per MWh</ENT>
        <ENT>1 hr minimum sampling time.</ENT>
      </ROW>
      <ROW>
        <ENT I="22"> </ENT>
        <ENT>b. HCl</ENT>
        <ENT>1.7E-03 lb per MMBtu of heat input</ENT>
        <ENT>2.9E-03 lb per MMBtu of steam output or 1.8E-02 lb per MWh</ENT>
        <ENT>For M26A, collect a minimum of 2 dscm per run; for M26, collect a minimum of 240 liters per run.</ENT>
      </ROW>
      <ROW>
        <ENT I="22"> </ENT>
        <ENT>c. Mercury</ENT>
        <ENT>7.9E-06 lb per MMBtu of heat input</ENT>
        <ENT>1.4E-05 lb per MMBtu of steam output or 8.3E-05 lb per MWh</ENT>
        <ENT>For M29, collect a minimum of 3 dscm per run; for M30A or M30B, collect a minimum sample as specified in the method; for ASTM D6784 <SU>b</SU> collect a minimum of 2 dscm.</ENT>
      </ROW>
      <ROW>
        <ENT I="22"> </ENT>
        <ENT>d. Filterable PM (or TSM)</ENT>
        <ENT>6.7E-03 lb per MMBtu of heat input or (2.1E-04 lb per MMBtu of heat input)</ENT>
        <ENT>1.2E-02 lb per MMBtu of steam output or 7.0E-02 lb per MWh; or (3.5E-04 lb per MMBtu of steam output or 2.2E-03 lb per MWh)</ENT>
        <ENT>Collect a minimum of 3 dscm per run.</ENT>
      </ROW>
      <TNOTE>
        <SU>a</SU> If you are conducting stack tests to demonstrate compliance and your performance tests for this pollutant for at least 2 consecutive years show that your emissions are at or below this limit, you can skip testing according to § 63.7515 if all of the other provisions of § 63.7515 are met. For all other pollutants that do not contain a footnote a, your performance tests for this pollutant for at least 2 consecutive years must show that your emissions are at or below 75 percent of this limit in order to qualify for skip testing.</TNOTE>
      <TNOTE>
        <SU>b</SU> Incorporated by reference, see § 63.14.</TNOTE>
    </GPOTABLE>
    <CITA>[78 FR 7195, Jan. 31, 2013]</CITA>
  </APPENDIX>
</CFRGRANULE>
