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ISE Sulam ON M M ISE M M W M M WE ISE ISE ON Mir Table A 1 Dual Phase Extraction System Soil Vapor Extraction Performance Data ARCO 4932 16 East Harding Way Stockton California TPH as Gasoline Benzene MISE Well Field Well Field FID Influent Influent Influent Hour Meter Dilution Blower Manifold Manifold Well Field Well Field Concen Removal Net Removed Concen-Removal Net Removed Conten Removal Net Removed Sample Date Reading Valve Vacuum Vacuum Temperature Flow Rate Flaw Rate Influent Efflueril tration Rate Removed to Hate trabon Rate Removed to Date trabon Rate Removed to Date ID Sampled (hours) (%Open) ("Hg) ("H20) (F) (acfm) (scfm) (ppmv) (ppmv) (ppmv) (lbs/day) (pounds) (pounds) (ppmv) (lbstday)(pounds) (pounds) (ppmv) (lbs/day) (pounds) (pounds) — 05/14/03 a 10 100% — — — -- -- 50000+ — 0 0 0 0 0 0 0 0 0 0 0 D INF 0529103 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 07/08/03 d 26 0 2% 200 — — 1372 120 20 000 1 1 17 000 766 26 435 200 71 025 41 4200 169 44 52 INF 08107!03 3987 0% 10 60 821 2062 169 43 500 0 21 61 DO 385 6 936 9 371 24 12 65 69 210 12 1 403 1 455 — 09/05/03 e — — — — — -- — — — — — — — — — — — — — — — INF 09/09103 f 1 020 8 0% 15 136 601 1627 104 7 800 0 00 2 900 113 6 459 15 831 <32 01 17 86 28 1 0 166 1 621 — 10109!03 1 724 3 0% 165 — — — — 550 0 — -- 1 993 17 823 — — 2 88 — — 32 1 653 INF 1023!03 2 055 8 0% 13 138 98 1 500 0 620 23 939 18 762 <1 6 00 1 89 37 12 15 1 668 — 1029103 2 203 6 0% 14 — — 165 117 1 100 2 5 — — 260 19 022 — — 0 89 — — 45 1 673 — 11105!03 2 251 5 0% 14 — — 110 78 1 000 45 — — 84 19 107 — -- 0 89 -- 15 1 674 INF 11/13103 g 2 325 6 0% 15 80 771 1767 137 1 1900 00 1 2DO 62 130 19 237 <1 6 01 0 89 <5 6 0 3 23 1 676 INF 12/03103 2 804 9 0% 15 140 — 1900 121 3 800 0 00 630 28 901 20 138 <0 16 00 1 90 19 01 33 1 680 INF 01/12104 3 743 5 0% 15 150 — 1627 116 226 00 29 2 591 20 729 <0 032 00 0 90 4 8 03 66 1 686 INF 02!04104 4 274 4 0% 15 — — 982 111 260 0 00 530 19 235 20 964 <0 32 00 0 90 <1 1 00 33 1 689 INF 03/03104 4 788 2 0% 15 — -- 2100 237 6030 00 340 27 495 21 459 17 01 1 92 063 00 086 1 690 INF 04/05104 5 512 9 0% 13 — — 2380 269 2780 00 490 44 1 063 22 522 24 02 4 2 96 <2 8 0 2 40 1 694 INF 0525M 61047 0% 10 — — 1470 166 1027 00 67 4 584 23 106 <0 080 00 21 98 <0 28 00 29 1 697 INF D6/14104 64800 0% 15 — — 1030 116 32D 0 00 200 8 89 23 195 <0 80 00 0 98 180 62 49 1 746 INF 07/13/04 6 938 7 0% 15 899 102 1215 00 100 3 106 23 301 12 00 0 98 65 02 61 1 807 INF 08/01104 h 7 208 5 0% 152 — — 772 87 889 00 150 4 43 23 344 1 9 00 0 99 48 12 81 1 815 INF 09/09104 7 626 7 0% 15 — — 1105 125 200 00 210 9 113 23 457 1 4 00 078 99 32 1 2 21 1 836 INF 10/04104 r 80371 0% 15 — — 771 87 130 00 110 3 101 23559 059 00 051 1DO 23 06 15 1851 INF 11101/04 8 597 3 0% 15 — 799 90 100 00 120 4 79 23 638 055 00 031 100 11 0 3 10 1 861 INF 12/13/04 9 603 3 0% 15 — 905 102 800 00 140 5 175 23 812 17 00 123 102 <0 69 00 7 1 868 INF 01/05/05 10 076 6 0% 15 — — 840 95 407 00 140 4 90 23 903 17 00 087 102 <0 56 00 0 1 868 INF 02109/05 10 916 9 0% 15 — 699 79 331 00 99 3 122 24 025 081 00 104 103 33 01 2 1 870 INF 03/10/05 11 225 5 0% 18 — 697 79 641 00 97 3 33 24 058 082 00 022 1 D4 36 01 1 1 871 INF 04/14/05 11 780 0 0% 15 — — 701 79 271 00 61 2 48 24106 093 00 042 104 014 00 1 1 872 INF 05/09/05 11 899 8 0% 15 — — 702 79 125 00 26 1 6 24 111 <0 031 00 005 104 <014 00 0 1 872 INF 06/01105 11 899 8 0% 15 — — 872 99 987 56 160 5 0 24 111 2 8 01 0 00 104 <D 17 00 0 1 872 REPORTING PERIOD SECOND QUARTER 2005 TOTAL POUNDS REMOVED 24111 104 1 872 TOTAL GALLONS REMOVED 3 953 14 303 PERIOD POUNDS REMOVED 53 05 1 PERIOD GALLONS REMOVED 9 0 06 0 TOTAL AVG FLOW RATE 118 scfm TOTAL PERCENT OPERATIONAL 66% PERIOD PERCENT OPERATIONAL 10% Definitions Chemical Properties scfm=Standard cubic feet per minute Standard conditions 60'F 1 atin lbs=Pounds Vapor density of gasoline=0 26 pounds per cubic feet(assumes molecular weight of gasoline is 1130 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 MtBE=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=6 1 pounds per gallon � FID=Flame Ionization Detector Liquid density of MtBE=618 pounds per gallon Notesystem start-up and shake-down b Source test for San Joaquin Valley Unified Air Pollution Control District performed 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 Permananenl system start up e SVE system shut down due to a car running into the compound SVE system restarted g Autodialer installed h System down on amval due to dogged filter I System dawn on arrival due to power failure Data not available at time of re n I W-ARCOLt93210 G MOPE O&M TalilwMCO 4932 08M Tables 2=.ids Pape t of t