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i <br /> Table A 1 <br /> Dual Phase Extraction System Soil Vapor Extraction Performance Data <br /> ARCO 4932 <br /> 16 East Harding Way Stockton California <br /> TRH as Gasoline Benzene MOE <br /> Well Field Well Field { FID Influent hhnuent Influent <br /> 5 Hour .Meter.Dilution_'Blowers Man�fald Mamfald Well Feld Well Fiel Conten Removal Net R Cortes► Removal Net Remo Conten Remove! Net Removed <br /> Sample`=Date w Reading Vahre- Vacuums Vacuum;Temperature Flow Rete Flow Irtfluerd Effl tmtion Rate Removed to Date Mon Rate Removed to Date tration Rate Removed to Date <br /> ID} w Sampled;;% - (htiuis)—(%'Open) ("H9)=' ("l-W) CF? -, (adm) (sdm) (ppm-) (ppmv} (ppmv) (It>slday) (Pounds) (pounQs) (ppmv) (lbs/day)(Pounds) (Pounds) (ppmv) Qbslday) (Pounds) (pounds) <br /> - 05/14/03 a 10 100% - -- - -- - 50000+ - 0 0 0 0 0 0 0 0 0 0 0 0 <br /> INF 05129ro3 be 252 0% 13 402 - 1502 135 48 000 1 1 16 000 811 409 409 190 76 38 38 2 100 95 48 48 <br /> INF 07/08103 d 260 2% 200 - - 1372 120 20 000 1 1 17 000 766 26 435 200 71 025 41 4200 169 44 52 <br /> INF 08/07/03 3987 0% 10 60 821 206 2 169 43 500 0 21 6 100 385 8 936 9 371 24 12 65 69 210 12 140 1 455 <br /> - 09/05103 - <br /> INF 09/09/03 f 1 020 8 0% 15 136 801 1627 104 7 800 0 00 2 900 113 6 459 15 831 <3 2 01 17 86 28 10 166 1 621 <br /> - 10/09103 1 724 3 0% 155 - - - - 550 0 - - 1993 17 823 - - 2 88 - -- 32 1 653 <br /> INF 10/23103 20558 0% 13 - - 138 98 1500 0 620 23 939 18762 <16 00 1 89 37 12 15 1668 <br /> - 10129M3 2 203 6 0% 14 - - 165 117 1 100 25 - - 260 19 022 - -- 0 89 - -- 4 5 1 673 <br /> -- 11105!03 2 251 5 0% 14 - - 110 78 1 000 45 - - 84 19 107 - - 0 89 - - Is 1 674 <br /> INF 1111=3 g 2 325 6 0% 15 80 771 1767 137 1 1800 00 1200 62 130 19 237 <1 6 01 0 89 <5 6 03 23 1 676 <br /> INF 12103103 2 804 9 0% 15 740 - 1900 121 3 800 0 00 630 28 901 20 138 <0 16 00 1 90 19 01 33 1 680 <br /> INF 01112104 3 743 5 0% 15 150 - 1627 116 226 00 29 2 591 20 729 <0 032 00 0 90 48 03 66 1 686 <br /> INF 02104104 4 274 4 0% 15 - - 982 111 2600 00 530 19 235 20 964 <0 32 00 0 90 <1 1 00 33 1 689 <br /> INF 03/03104 4 788 2 0% 15 - - 2100 237 6030 00 340 27 495 21 459 1 7 01 1 92 063 00 086 1 690 <br /> INF 04105!04 5 512 9 0% 13 - - 2380 269 2780 00 490 44 1 063 22 522 24 02 42 96 <2 a 02 40 1 694 <br /> INF 05/25104 61047 0% 10 - - 1470 166 1027 00 67 4 584 23106 <0 080 00 21 98 <0 28 00 29 1 697 <br /> INF 06/14104 6 480 8 0% 15 - - 1030 116 3200 00 200 8 89 23 195 <0 60 00 0 98 180 62 49 1 746 <br /> INF 07/13/04 6 938 7 0% 15 - - 899 102 1215 00 100 3 106 23 301 1 2 00 0 98 65 02 61 1 807 <br /> INF 08W1104 h 7 208 5 0% 152 - - 77 2 87 889 00 150 4 43 23 344 19 00 0 99 48 12 al I 1 815 <br /> INF 09109104 7 626 7 0% 15 - - 1105 125 20 0 00 210 9 113 23 457 14 00 078 99 32 12 21 1 836 <br /> REPORTING PERIOD THIRD QUARTER 2004 - <br /> TOTAL'-POUNDS REMOVEDi 1 cup 6 23,457 99 1,836 <br /> 3,846 14 297 <br /> TOTAL GALLDN5,REMOVED',. <br /> PERIOD POUNDS REMOVED 262 15 90 <br /> PERIOD GALLONNS REMOVEDa 1t4 e'a s= __Y y, �w's r ;� 43 021 1S <br /> OTAL"AVG FLOW RATE131 ecim = <br /> TOTAL PERCENT <br /> PERIOD P RCE tOPERAATIONAL 74 * <br /> 49% <br /> Definitions Chemical Properiles <br /> sctrrh-Standard cubic feet per minute Standard conditions 60'F t atm <br /> lbs=Pounds Vapor density of gasoline=0 26 pounds per cubic feet(assumes molecular weight of gasoline is 100 pounds per pound mole) <br /> -=Data not available Vapor density of benzene-0 206 pounds per cubic feet <br /> ppmv=Parts per million by volume Vapor density of MtBE-0 232 Pounds per cubic feet <br /> TPH=Total petroleum hydrocarbons Liquid density of benzene=7 34 pounds per gallon <br /> "Hg =Inches of mercury Liquid density of gasoline a 6 1 pounds per gallon <br /> FID =Flame Ionization Detector Liquid density of MtBE=6 18 pounds per gallon <br /> Notes <br /> a System start-up and shake-down <br /> b Source test for San Joaquin Valley Unified Air Pollution Control District performed <br /> c Analyte values given were analyzed beyond the EPA recommended holding time The analysis was performed because the onginal analysis detected an analyte in the assoc4ated blank as well as in the sample <br /> Id Permananent system start up <br /> e SVE system shut down due to a car running into the compound <br /> I SVE system restarted <br /> g Autodialer installed <br /> h System down on amval due to clogged fitter <br /> i System down on amval due to power failure <br /> Data not available at tome of reporting <br /> 144RCO1493W R M%RCO 4832 O&M Tables 3004AS Page 1 of 1 <br />