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  <FDSYS>
    <CFRTITLE>40</CFRTITLE>
    <CFRTITLETEXT>Protection of Environment</CFRTITLETEXT>
    <VOL>6</VOL>
    <DATE>2008-07-01</DATE>
    <ORIGINALDATE>2008-07-01</ORIGINALDATE>
    <COVERONLY>false</COVERONLY>
    <TITLE>Work practice standards.</TITLE>
    <GRANULENUM>60.103a</GRANULENUM>
    <HEADING>Section 60.103a</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 Ja" SEQ="0">Standards of Performance for Petroleum Refineries for Which Construction, Reconstruction, or Modification Commenced After May 14, 2007</PARENT>
    </ANCESTORS>
  </FDSYS>
  <SECTION>
    <SECTNO>§ 60.103a</SECTNO>
    <SUBJECT>Work practice standards.</SUBJECT>
    <P>(a) Each owner or operator that operates a flare that is subject to this subpart shall develop and implement a written flare management plan. The owner or operator of a newly constructed or reconstructed flare must develop and implement the flare management plan by no later than the date that flare becomes an affected flare subject to this subpart. The owner or operator of a modified flare must develop and implement the flare management plan by no later than 1 year after the flare becomes an affected flare subject to this subpart. The plan must include:</P>
    <P>(1) A diagram illustrating all connections to the flare;</P>
    <P>(2) Methods for monitoring flow rate to the flare, including a detailed description of the manufacturer's specifications, including but not limited to, make, model, type, range, precision, accuracy, calibration, maintenance, and quality assurance procedures for flare gas monitoring devices;</P>

    <P>(3) Procedures to minimize discharges to the flare gas system during the planned start-up and shutdown of <PRTPAGE P="308"/>the refinery process units that are connected to the affected flare;</P>
    <P>(4) Procedures to conduct a root cause analysis of any process upset or malfunction that causes a discharge to the flare in excess of 14,160 m<SU>3</SU>/day (500,000 scfd);</P>
    <P>(5) Procedures to reduce flaring in cases of fuel gas imbalance (i.e., excess fuel gas for the refinery's energy needs); and</P>
    <P>(6) Explanation of procedures to follow during times that the flare must exceed the limit in § 60.102a(g)(3) (e.g., keep records of natural gas purchases to support assertion that the refinery is producing more fuel gas than needed to operate the processes).</P>

    <P>(b) Each owner or operator that operates a fuel gas combustion device or sulfur recovery plant subject to this subpart shall conduct a root cause analysis of any emission limit exceedance or process start-up, shutdown, upset, or malfunction that causes a discharge to the atmosphere in excess of 227 kilograms per day (kg/day) (500 lb per day (lb/day)) of SO<E T="8052">2</E>. For any root cause analysis performed, the owner or operator shall record the identification of the affected facility, the date and duration of the discharge, the results of the root cause analysis, and the action taken as a result of the root cause analysis. The first root cause analysis for a modified flare must be conducted no later than the first discharge that occurs after the flare has been an affected flare subject to this subpart for 1 year.</P>
    <P>(c) Each owner or operator of a delayed coking unit shall depressure to 5 lb per square inch gauge (psig) during reactor vessel depressuring and vent the exhaust gases to the fuel gas system for combustion in a fuel gas combustion device.</P>
  </SECTION>
</CFRGRANULE>

