Flare

BAAQMD Refinery Flare Emission Report
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Tesoro Martinez - Ammonia Plant
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February - 2017
Date Vent Gas Flow Methane NMHC Sulfur Dioxide
(mo/day/yr) (volume in scf) See note **** (lbs) (lbs) (lbs)
2/1/2017 52,135.00 0.00 0.00 0.18
2/2/2017 65,328.00 0.00 0.00 0.17
2/3/2017 41,369.00 0.00 0.00 0.15
2/4/2017 0.00 0.00 0.00 118.05
2/5/2017 0.00 0.00 0.00 73.21
2/6/2017 13,240.00 0.00 0.00 101.28
2/7/2017 59,214.00 0.00 0.00 100.37
2/8/2017 80,273.00 0.00 0.00 87.73
2/9/2017 31,071.00 0.00 0.00 50.52
2/10/2017 0.00 0.00 0.00 423.58
2/11/2017 0.00 0.00 0.00 0.12
2/12/2017 0.00 0.00 0.00 0.15
2/13/2017 0.00 0.00 0.00 1.12
2/14/2017 0.00 0.00 0.00 0.13
2/15/2017 8,313.00 0.00 0.00 0.14
2/16/2017 0.00 0.00 0.00 0.16
2/17/2017 12,167.00 0.00 0.00 0.16
2/18/2017 27,555.00 0.00 0.00 0.12
2/19/2017 30,180.00 0.00 0.00 0.14
2/20/2017 19,168.00 0.00 0.00 0.16
2/21/2017 21,847.00 0.00 0.00 0.20
2/22/2017 26,067.00 0.00 0.00 0.23
2/23/2017 35,031.00 0.00 0.00 0.19
2/24/2017 26,437.00 0.00 0.00 0.18
2/25/2017 58,150.00 0.00 0.00 0.18
2/26/2017 40,368.00 0.00 0.00 0.14
2/27/2017 51,574.00 0.00 0.00 0.20
2/28/2017 36,778.00 0.00 0.00 0.19
February Totals 736,265.00 0.00 0.00 959.15
  • * Natural gas is used for both pilot and purge gas for the refinery flare system, except for the Emergency Flare that uses nitrogen as purge gas.
    The flow is determined using an orifice calculation based on the orifice size in the lines and the line pressure upstream of the orifice.
    ** The purge gas and pilot gas flows at the Ammonia Plant flare are measured by rotameters in the natural
    gas and nitrogen lines.
    *** The purge gas and pilot gas flows at the 50 Unit flare are measured by flow meters
    **** Corrected for seal pot level and pressure data
    ***** 50 Unit change in flare purge gas to nitrogen
    In the case of an invalid sample, the monthly average was used for composition data
Tesoro Martinez Ammonia Plant Flare Report 2/1/2017 - 2/28/2017
 
 

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Last Updated: 4/13/2023