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  <FDSYS>
    <CFRTITLE>40</CFRTITLE>
    <CFRTITLETEXT>Protection of Environment</CFRTITLETEXT>
    <VOL>6</VOL>
    <DATE>2007-07-01</DATE>
    <ORIGINALDATE>2007-07-01</ORIGINALDATE>
    <COVERONLY>false</COVERONLY>
    <TITLE>Standard for total reduced sulfur (TRS).</TITLE>
    <GRANULENUM>60.283</GRANULENUM>
    <HEADING>Section 60.283</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 60" SEQ="1">STANDARDS OF PERFORMANCE FOR NEW STATIONARY SOURCES</PARENT>
      <PARENT HEADING="Subpart BB" SEQ="0">Standards of Performance for Kraft Pulp Mills</PARENT>
    </ANCESTORS>
  </FDSYS>
  <SECTION>
    <SECTNO>§ 60.283</SECTNO>
    <SUBJECT>Standard for total reduced sulfur (TRS).</SUBJECT>
    <P>(a) On and after the date on which the performance test required to be conducted by § 60.8 is completed, no owner or operator subject to the provisions of this subpart shall cause to be discharged into the atmosphere:</P>
    <P>(1) From any digester system, brown stock washer system, multiple-effect evaporator system, or condensate stripper system any gases which contain TRS in excess of 5 ppm by volume on a dry basis, corrected to 10 percent oxygen, unless the following conditions are met:</P>
    <P>(i) The gases are combusted in a lime kiln subject to the provisions of paragraph (a)(5) of this section; or</P>
    <P>(ii) The gases are combusted in a recovery furnace subject to the provisions of paragraphs (a)(2) or (a)(3) of this section; or</P>
    <P>(iii) The gases are combusted with other waste gases in an incinerator or other device, or combusted in a lime kiln or recovery furnace not subject to the provisions of this subpart, and are subjected to a minimum temperature of 650 °C (1200 °F) for at least 0.5 second; or</P>

    <P>(iv) It has been demonstrated to the Administrator's satisfaction by the owner or operator that incinerating the exhaust gases from a new, modified, or reconstructed brown stock washer system is technologically or <PRTPAGE P="365"/>economically unfeasible. Any exempt system will become subject to the provisions of this subpart if the facility is changed so that the gases can be incinerated.</P>
    <P>(v) The gases from the digester system, brown stock washer system, or condensate stripper system are controlled by a means other than combustion. In this case, this system shall not discharge any gases to the atmosphere which contain TRS in excess of 5 ppm by volume on a dry basis, uncorrected for oxygen content.</P>
    <P>(vi) The uncontrolled exhaust gases from a new, modified, or reconstructed digester system contain TRS less than 0.005 g/kg air dried pulp (ADP) (0.01 lb/ton ADP).</P>
    <P>(2) From any straight kraft recovery furnace any gases which contain TRS in excess of 5 ppm by volume on a dry basis, corrected to 8 percent oxygen.</P>
    <P>(3) From any cross recovery furnace any gases which contain TRS in excess of 25 ppm by volume on a dry basis, corrected to 8 percent oxygen.</P>

    <P>(4) From any smelt dissolving tank any gases which contain TRS in excess of 0.016 g/kg black liquor solids as H<E T="52">2</E>S (0.033 lb/ton black liquor solids as H<E T="52">2</E>S).</P>
    <P>(5) From any lime kiln any gases which contain TRS in excess of 8 ppm by volume on a dry basis, corrected to 10 percent oxygen.</P>
    <CITA>[43 FR 7572, Feb. 23, 1978, as amended at 50 FR 6317, Feb. 14, 1985; 51 FR 18544, May 20, 1986; 65 FR 61758, Oct. 17, 2000]</CITA>
  </SECTION>
</CFRGRANULE>

