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ry <br /> v OF PETROLEUM HYDROCARBON CONSTITUENTS IN THERMAL OXIDIZER EFFLUENT VAPOR AND <br /> STOCKTON,CALIFORNIA <br /> CONCENTRATIONS(ppm Daily <br /> TABLE 2 TRPmv)OF EFFICIENCY DATA,FOEtiv4ER CHEVRON 55 9-1918,45 EAST OXIDIZE WAYS Average Percent TVH <br /> CALCULATED DES Unidentified went Destruction <br /> Peaks After Volatile Elfcienc <br /> ThOx Ethyl" Benxenc H droearbons Conc. <br /> TEMP. peaks Prior Toluene benzene X !encs <br /> to Benzene Benzene 35 6,533 98.39 <br /> Effluent Date NA ND 6,533 99.13 <br /> � ND ND ND 19 99.49 <br /> 11/16190 1,450 35 ND ND ND ND 11 6,533 <br /> 99.77 <br /> 2 11/16190 1,425 19 iD ND ND ND ND 5 6,533 6,533 98.76 I <br /> 1ND,440 ND ND ND 27 <br /> 5 ND ND <br /> 99.82 <br /> 4 11116 1,475 11/16/90 1,485 27 D ND 4 6,5 99.95 <br /> 5 ND ND N ND 1 6,500100.00 a <br /> 6 11119/90 1,4?5 i ND ND ND ND Q 6,500 61500 100.00 <br /> 7 11/19190 1,485ND ND ND 6,500 99.31 <br /> g 11/19/90 1,440 I D ND ND 15 99.26 <br /> 6,500 <br /> 9 11/19/90 1,435 ND ND ND ND ND D ND 5 6,500 99.72 <br /> 10 11/19190 1,470 16 ND ND ND ND ND 6 6.500 100.00 <br /> 11 11/19/90 1,47 0 6 ND ND ND ND ND <br /> 12 11119140 1435 ND ND ND 0 4,900 100.00 <br /> 100.00 <br /> 13 11/19190 ND ND 0 4,900 <br /> ND NND 00 <br /> 11/2119 100.00 <br /> ND ND D ND 0 4,9 <br /> 14 <br /> 0 1,450 ND ND ND ND 4,900 !W.00 <br /> 15 11/21190 1,440 ND ND ND ND 0 4,900 100.00 <br /> 16 ND <br /> 11!21190 1,450 ND ND ND ND ND ND 0 4,900 100.00 <br /> 1? 11/21190 1,460 ND ND NU ND ND ND ND 0 4,900 100.00 <br /> 18 11/21190 1,430 ND ND ND ND ND ND 0 4,90011t21/90 100.00 <br /> 1,470 ND ND ND ND19 4. <br /> 20 11/21140 1,4?0 ND ND <br /> ND ND ND 50 5,900 99 39 <br /> 21 11/2119 ND ND 12 ND 5'9� 99.34 <br /> 26 24 ND ND 13 5,900 <br /> 22 llf27190 1,500 4 28 ND ND ND ND <br /> 23 11/27190 1,440 8 5 ND <br /> 24 11127190 1'440 <br /> 1 <br /> 's <br /> in <br /> Notet�ppvmvm Concentrations areP per million on a volumetric basis. <br /> ed greater tan h 1 ppm• <br /> ND _ No concentration measur ' <br /> x <br />