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Table Dual Phase Extraction System-Soil Vapor Extraction Performance Data ARCO 4932 16 East Harding Way Stockton California y _tic 41 - TPH as Gasoline Benzene MTBE "' � r `ac ` " roFt# WeBFleld WellFleldy�t� FID Influent Ir>rluenl MtBE Hour Meter piton, 8lowerr Mm ifold 'Manifold Well Fletd Well Flel Conoen Removal `iV¢t R Cormalr Removal Net R Cowan- Removal Net Removed SampleA Date, ' Readingx`Valve Var uum"Vacuum Temperature-Flaw Rate Ftow Rat influent Efllue trati6n Rate Removed to Date 1ra1lon Rate Removed to Date tration Rate Removed ib Date }3� ID Sa_mpted �°"(hours)^I(%Open) {"Hg), °("flip) {°F)='�" ( ) ( )` (PPS) {Ppmv) '(PPm+r) (lbs/day) (pounds) (pounds) (ppmv) (tbslday)(pig) (Ps) (PPS) (Ihsldall) (Pam) (pounds) 05!14! a 10 10096 - - - - - 50 000+ - 0 0 0 0 0 0 0 0 0 0 0 0 INF 05'29!03 b c 252 0% 13 402 - 1502 135 48 000 1 1 16 000 811 409 409 190 76 38 38 2 100 95 48 48 INF 07108!03 d 260 2% 200 - - 1372 120 20 000 1 1 17,000 766 26 435 200 71 025 41 4200 169 44 52 INF 08/07/03 398 7 0% 10 60 821 2062 169 43 500 0 21 6 100 385 8 936 9 371 24 12 65 69 210 12 1 403 1 455 - 09/05103 e - - - - - - - - - - - - - - - - - - -- -- INF 09109!03 f 1 020 8 0% 15 136 801 1627 104 7 800 0 00 2 900 113 6 459 15 831 <32 01 17 86 28 10 166 1 621 - 10'09103 1 724 3 0% 155 - - - - 550 0 - - 1993 17 823 - - 2 88 - - 32 1 653 INF 10123!03 2 055 8 0% 13 - - 138 98 1 500a 620 23 939 18 762 <1 6 00 1 69 37 12 15 1 668 - 10/29M 2 203 6 0% 14 -- - 165 117 1 100 25 - - 260 19 022 -- - 0 89 -- -- 5 1 673 - 11!05103 2 251 5 0% 14 - - 110 78 1 000 45 - - 84 19 107 - - 0 89 - - 1 1 674 INF 11 h 3103 g 2 325 6 0% 15 80 771 1767 137 1 1800 00 1200 62 130 19 237 <1 6 01 0 89 <56 0 3 2 1 676 INF 12103/03 2 804 9 0% 15 140 - 1900 121 3 800 0 00 630 28 901 20 138 <016 00 1 90 19 01 3 1 680 INF 011112004 3,7435 0% 15 150 - 1627 116 226 00 29 2 591 20 729 <0 032 00 0 90 4 8 0 3 7 1 686 INF 02104104 4 274 4 0% 15 - - 982 111 260 0 00 530 19 235 20 964 <0 32 00 0 90 <1 1 00 3 1689 INF 03!0 M 47882 0% 15 - - 2100 237 6030 0 0 340 27 495 21 459 1 7 01 1 92 0 63 00 1 I 1 690 INF 04105/04 5 512 9 0% 13 - - 2380 269 278 0 00 490 44 1 063 22 522 24 02 4 96 <2 8 02 4 ' 1 694 INF 051255/04 6,1047 0% 10 - - 1470 166 102 7 00 67 4 564 23106 <0 080 00 2 98 <0 28 00 3 1697 INF 06114/04 6 480 8 0% 15 - - 1030 116 3200 00 200 8 89 23 195 <0 80 00 0 98 180 62 49 1 746 SPORTING PERIOD SECOND QUARTER 2004`w TA0.3-POUNDS RENM3VED Vr-- 'w - _28,79$ 98 1,748 y7ALGAf_Loks REMt1VED 3,802 13 283 PER1O0PDUND3REMOVED-4-'7-f' " w' '} `i{ r 3' _ 1,736 63 556 PERiO�tiALLON3 REMOVED� �z ' yr c o x -285 086 899 TOTAL AVG FLOW RATE 440 acini PERIOD PERCENT OPERATIONALYW%-. *"cur Definitions Chemical Properties scfrn-Standard cubic feet per minute Standard cond3lons 60°F,1 atm lbs=Pounds Vapor density of gasoline=0 26 pounds per cubic feet(assumes molecular weight of gasoline is 100 pounds per pound mole) -=Data not available Vapor density of benzene-0 206 pounds per cubic feet ppmv=Parts per million by volume Vapor density of ME=0 232 pounds per cubic feet TPH=Total petroleum hydrocarbons Liquid density of benzene-7 34 pounds per gallon "Hg=Inches of mercury Liquid density of gasoline=61 pounds per gallon FID=Flame Ionization Detector Liquid density of MISE=6 18 pounds per gallon Notes a System start-up and shake-down b Source test for San Joaquin Valley Unified Air Pollution Control District perfonned c Analyte values given were analyzed beyond the EPA recommended holding time The analysis was performed because the original analysis detected an analyte in the associated blank as well as in the sample d Pemmananermt system start up e SVE system shut dowry due to a car running into the compound SVE system restarted Autodialer installed �h 4 I iARC01t9 M 6 MMCO 49-2 OEM Tables 20Mads Page 1 of i