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- I <br /> OA-1 <br /> Soil Vapor Extraction System Performance lata <br /> Time Oil-LoclWord Site <br /> 14000 E Highway 88 <br /> Lockeford,California <br /> TPH as QajolIM Senzene <br /> EIQ Influent Influent <br /> Hour Meter Ambient Blower Influent Conten- Removal Net Removed Conten- Removal Net Removed <br /> Sample Date Reading Dilution Vacuum Flow Rate Influent Effluent tration Rate Removed to Date tration Rate Removed to Date <br /> ID Sampled (hours) Valve (H20) (scfm) (ppmv) (ppmv) (ppmv) (lbslday) (pounds) (pounds) (ppmv) (lbs/day) (pounds) (pounds) <br /> INFL. 12!73199 7 863 1 a 6%0 3 154 10 000 20 6 900 00 00 Start-Up 1570 00 00 Start-Up <br /> INFL 01/25/00 8 821 0 5%0 20 156 1 900 10 3 990 2492 4 972 6 4 972 6 330 16 321 321 <br /> INFL 02/22/00 9 208 6 10%0 20 313 1,000 5 2 460 3082 4 501 1 9 473 7 338 33 397 718 <br /> INFL 03/13/00 9 378 6 15%0 10 204 1910 1 2,960 2417 1 9476 114215 27 0 17 178 896 <br /> INFL 04/13/00 9 394 4 1%0 161 1701 2 990 5 3 810 2594 1650 11 586 5 245 <br /> 13 1 0 906 <br /> INFL 05/03/00 9 823 2 4%0 121 101 7 1,490 5 2 820 1148 3 343 3 14 929 8 314 10 205 ill 1 <br /> INFL 06/14/00 10 831 6 3%0 98 1471 795 0 5 080 2991 8 696 5 23 626 3 375 17 572 1683 <br /> INFL 08109/00 10 854 1 2%0 20 2 131 >10 000' 2 2 330 1221 1975 23,8238 317 1 3 14 1697 <br /> INFL 09114/00 11 523 4 C 201 1879 690 0 1 120 842 2 877 8 26 701 6 7 2 0 4 240 1937 <br /> INFL 10/19/00 12 031 3 C 389 1897 345 0 1 260 957 1 903 9 28 605 5 633 0 4 844 2022 <br /> INFL 11107100 12 350 9 C 101 1837 298 0 895 65 8 1 0754 29 680 9 4 39 03 418 2063 <br /> INFL 12x20100 12 774 2 D -- -- — — — _ — — <br /> INFL 01117/01 12 922 0 C 30 1921 475 0 379 291 1 129 9 30 810 9 1 11 01 379 2101 <br /> INFL 02/21/01 13 762 0 C 40 1912 293 0 10 08 6155 31,4264 ND 0 0 1 17 211 3 <br /> INFL 03/14101 13,9284 C 25 184 8 475 4 430 31 8 1129 31 539 3 2 2 04 14 2126 <br /> INFL 04/18/01 14 764 5 C 30 1947 375 0 520 405 1,2600 32 799 3 68 00 68 2195 <br /> INFL 05/17/01 15 352 4 C 25 1924 275 5 110 85 6002 33 399 5 ND 05 59 2254 <br /> INFL 06/13/01 15 797 6 C 25 1914 400 20 440 337 3913 33 790 7 8 0 00 48 2302 <br /> INFL 07/11/01 163936 C 30 191 5 450 0 310 238 7136 34,504 3 06 00 04 2306 <br /> INFL 08/15/01 17 232 5 C 25 151 3 400 30 330 20 0 7648 35 269 1 ND 00 00 2306 <br /> INFL 09/05/01 17 682 5 C 25 191 3 400 30 490 37 5 5392 35 808 3 ND 00 00 2306 <br /> INFL 10/10/01 18 331 3 C 30 1385 300 0 360 20 0 7769 36 585 2 ND 0 0 0 0 2306 <br /> INFL 11/28/01 19 001 4 C 20 1887 375 40 110 83 3946 36 979 8 ND 01 12 231 8 <br /> INFL 12/12/01 19 339 2 C 25 161 2 325 0 280 181 1856 37 165 4 1 5 00 06 2325 <br /> INFL 01/02102 19 709 4 C 25 1513 210 10 190 00 1394 37 304 8 ND 00 00 2325 <br /> INFL 02x06!02 20,4745 C 90 537 2 700 50 270 00 00 37 304 8 ND 00 00 2325 <br /> INFL 03106102 21 1458 C 100 532 1 100 40 170 00 0 0 37 304 8 ND 00 0 0 2325 <br /> FfEPi, N - 1102 to 03130102 <br /> TOT Fft tt 118Ey�° 37.3 23Z,S <br /> `' W VEA: _"► X7 <br /> P 1091 a Q <br /> P i2e- 'b°a3 <br /> 1P � lis <br /> m t t rAIL- <br /> scfm =Standard cubic feet per minute NS=Not sampled <br /> lbs =Pounds a System startup initial air samples taken <br /> NA =Not available or not applicable = FID(flame-ionization detector)reading (Flame Out) <br /> ND =Non-detectable above detection limit Please note No samples were taken in July because the remediation system was down <br /> ppmv =Parts per million by volume converted from micrograms C=dilution air valve is dosed <br /> per liter,assuming TPH as gasoline and benzene vapor D=System is down due to repairlmaintenance <br /> density is 0 278 and 0 217 lbs per cubic foot respectively Density of benzene=7 34 pounds per gallon <br /> TPH =Total Petroleum Hydrocarbons Density of gasoline=6 1 pounds per gallon <br /> 077 41737 002/Q1-02 Lockeford O&MTableslTABLE A-1 <br />