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i <br /> Table 1. Solt Vapor Extraction and Treatment Sys Influent Data,ARCO Station 434,Lodi,California <br /> i <br /> Start up date 613191 <br /> Sample Averdge flow Daye to Down days Percent Influent concentration ppmv a Removal rate,lbsiday Net removal,Ibs&gallons <br /> date Penod rate,cfm period to penod operational TPH-G B TPH G B TPH-G B <br /> 1219194 11/3194-12/27/94 62 54 2 96% Ito <0012 3 0 132 lbs 0 lbs <br /> 1/6/95 121271941118195 60 22 37 83% 76 0035 2 0 31 lbs 0 lbs <br /> 216!95 1118/95 2113195 53 26 161 38% 140 1 1 3 0 28 lbs 0 lbs <br /> 317/95 2113M VINO 55 31 32 90% 89 018 2 0 51 Ibs 0 lbs <br /> 415195 3/16195 415/95 60 29 0 100% 24 0 1 0 16 lbs 0 Ibs <br /> 5111195 (b) 415195 5/11195 20 36 22 39% 33 0 0 0 3 lbs 0 Ibs <br /> 5118195 5111195-5118195 20 7 0 t00% 66 0 0 0 3 lbs 0 Ibs <br /> 5126/95 5118/95 526195 20 8 0 100% 80 0 1 0 5 Ibs 0 lbs <br /> 6121195 512&95 6/21!95 22 26 0 10096 44 0 0 0 9 lbs 0 lbs, t <br /> 718195 6/21195 7/8195 22 17 0 10096 77 <0l6 t 0 11 lbs 0 Ibs <br /> 8122/95 718195 8122/95 22 45 0 100% 54 <016 0 0 20 lbs 0 lbs <br /> 9111195 8122195 9/11/95 22 20 0 t00% 68 <016 1 0 II Ibs 0 lbs <br /> 12/31/95 9/11195 12/31/95 22 111 97 13% SYSTEM TURNED OFF ON 9/25195 0 lbs 0 lbs <br /> 112&96 12/31/95 3/31196 26 91 55 4O% 87 I NA I I I NA 30 Ib% NA lbs <br /> SYSTEM OPERATED 1!9!96-2114196 <br /> Totals and averages L/1196 1131196 26 91 55 4D% 87 NA I NA 30 lbs NA lbs <br /> for reporting period 5 grly NA gals <br /> Totals and averages 6/3191-3131196 80 1772 265 85% l 113 5 41 0 50862 lbs 153 lbs <br /> cumalanve <br /> 8204 gals 2 t gals <br /> Sample calculations <br /> Removal rate calculation <br /> Ibslduy-(gmlmole)s(umoldmole)'(moles11013+6 umoles)*(IOE+3 mglgm)'(I 177 molelcubic feet)+(2 204640E 6 lblmg)'(60 mm/hr)+(cubic feet/mm)"(24 hrdday) <br /> where(gm/mole)is molecular weight,(umolestmole)is ppm influent concentration,molecular weights of TPH G and Benzene are 100 2 and 78 1 respectively <br /> For pounds cumulative removal we used the removal Iblddy result and multiplied it by the difference to the number of days between the current and previous sampling event <br /> Gallons removal calculation(for TPH) <br /> allom removed—lbs•galloWdensity to lbs(denAty for TPH G is 6 2,benzene is 7 32 <br /> (a)from start up through lune 1992 influent samples were not taken beCdase there was no sample tap on the inlet to the cutdlytic oxidizer <br /> Therefore,the influent concentrations(in pins per million by volume)are an estimate <br /> (b)The cadyttc oxidizer was taken off line and replaced with u brordter system on 5111195 <br />