Flare

BAAQMD Refinery Flare Emission Report
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Phillips 66 Rodeo - Main
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January - 2015
Date Vent Gas Flow Methane NMHC Sulfur Dioxide
(mo/day/yr) (volume in scf) (lbs/day) See note 2 (lbs/day) See note 2 (lbs)
1/1/2015 0.00 0.00 0.00 0.00
1/2/2015 0.00 0.00 0.00 0.00
1/3/2015 0.00 0.00 0.00 0.00
1/4/2015 0.00 0.00 0.00 0.00
1/5/2015 0.00 0.00 0.00 0.00
1/6/2015 0.00 0.00 0.00 0.00
1/7/2015 0.00 0.00 0.00 0.00
1/8/2015 14,906.26 2.33 9.06 8.91
1/9/2015 0.00 0.00 0.00 0.00
1/10/2015 0.00 0.00 0.00 0.00
1/11/2015 0.00 0.00 0.00 0.00
1/12/2015 0.00 0.00 0.00 0.00
1/13/2015 0.00 0.00 0.00 0.00
1/14/2015 0.00 0.00 0.00 0.00
1/15/2015 0.00 0.00 0.00 0.00
1/16/2015 0.00 0.00 0.00 0.00
1/17/2015 0.00 0.00 0.00 0.00
1/18/2015 0.00 0.00 0.00 0.00
1/19/2015 0.00 0.00 0.00 0.00
1/20/2015 0.00 0.00 0.00 0.00
1/21/2015 0.00 0.00 0.00 0.00
1/22/2015 0.00 0.00 0.00 0.00
1/23/2015 0.00 0.00 0.00 0.00
1/24/2015 0.00 0.00 0.00 0.00
1/25/2015 295,751.81 18.24 169.95 34.37
1/26/2015 0.00 0.00 0.00 0.00
1/27/2015 0.00 0.00 0.00 0.00
1/28/2015 0.00 0.00 0.00 0.00
1/29/2015 0.00 0.00 0.00 0.00
1/30/2015 0.00 0.00 0.00 0.00
1/31/2015 34,053.35 5.22 11.81 1.70
January Totals 344,711.42 25.79 190.82 44.98
  • (1) The concentration of the constituents that were not detected is assumed to be zero. Non-detect H2S is assumed to be 0.01% by volume.
    (2) Methane and non-methane emissions are calculated using 98% efficiency.
    (3) The concentration of Non-methane hydrocarbons is calculated by subtracting hydrogen, nitrogen, other inorganic substances and methane from 100%.
    (4) Fuel non-methane portion molecular weight calculation is provided in Table 3.
Phillips 66 Rodeo Main Flare Report 1/1/2015 - 1/31/2015
 
 

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Last Updated: 4/13/2023