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Table A 1 <br /> Soil Vapor Extraction System Performance Data <br /> Time Oli Lockeford Site <br /> 14000 E Highway 88 <br /> Lockafard California <br /> TPH as G sollns <br /> EID Influent __.. Influent <br /> Hour Meter Ambient Blower Influent Conran Removal Net Removed Concen Removal Net Removed <br /> Sample Date Resding Dilution Vacuum Flow Rate Influent Effluent trallon Rate Removed to Date tration Rate Removed to Date <br /> ID Sampled (hours) Valve (H2O) (srfm) (ppmv) (ppmv) (ppmv) Ob day) ( nds) (pounds) (ppmv) (Ibslday) (pounds) (pounds) <br /> INFL 12/13199 7 8631 a 6%O 3 154 10 000 20 6 900 0 0 0 0 Start Up 157 0 1 6 00 Start Up <br /> 32 1 32 1 <br /> INFL 01/25/00 8 821 0 5%0 20 156 1 9D0 10 3 990 2492 4 972 6 4 972 6 330 1 8 <br /> INFL 02122/00 9 208 6 10%0 20 313 1 000 5 2 460 3082 4 501 1 9 473 7 338 3 3 39 7 71 <br /> INFL 03113/00 9 378 6 15%0 10 204 1910 1 2 960 241 7 1 947 8 11 421 5 270 1 7 17 8 896 <br /> INFL 04113/00 9 394 4 1%0 161 170 1 2 990 5 3 810 2594 1650 11 586 5 245 <br /> 1 3 1 0 906 <br /> 6 <br /> INFL 05103/00 9 823 2 4%0 121 101 7 1 490 5 2 820 1148 3 343 3 14 929 8 314 ID 205 111 1 <br /> INFL 06114100 10 831 6 3%0 98 147 1 795 0 5 080 2991 06965 23 626 3 375 17 572 1683 <br /> INFL 06!49100 10 854 1 2%0 202 131 X10 DOG" 2 2 330 1221 1075 23 823 8 31 7 13 14 1697 <br /> INFL 09114100 11 5234 C 20 1 1879 690 0 1 120 642 2 877 8 267010 72 04 240 1037 <br /> INFL 10/19100 12 031 3 C 389 1897 345 0 1 260 957 1 903 9 28 605 5 633 04 8 44 2022 <br /> INFL 11/07/00 12 350 9 C 181 163 7 298 0 895 658 1 075 4 29 680 9 439 03 418 2063 <br /> INFL 12!211100 12 774 2 D - - - <br /> INFL 01117/01 12 922 0 C 30 1921 475 0 379 291 1 1299 30 810 9 1 11 01 379 2101 <br /> INFL 02121/01 13 762 0 C 40 191 2 293 0 10 08 6155 31 426 4 ND 00 1117 2113 <br /> INFL 0314f01 13 928 4 C 25 1848 475 4 430 31 8 1129 31 5393 22 04 14 2126 <br /> INFL 04118/01 14 764 5 C 30 194 7 375 0 520 405 1 260 0 32 799 3 68 of) 68 2195 <br /> INFL 05117/01 15 352 4 C 25 1924 275 5 110 es 600 2 33 399 5 ND 05 59 2254 <br /> INFL 08!13101 15 797 6 C 25 1914 400 20 440 337 391 3 33 790 7 so 00 48 2302 <br /> INFL 07111M 16 393 5 C 30 1915 450 0 310 238 7136 34 504 3 06 00 04 2306 <br /> INFL 08115101 172326 C 25 1513 400 30 330 200 7648 35 269 1 ND 00 00 2306 <br /> INFL 09105101 17 682 5 C 25 1913 400 30 490 375 5392 35 806 3 ND 00 00 2306 <br /> INFL 10/10/01 18 331 3 C 30 138 5 300 0 360 200 7769 36 585 2 ND 00 00 2306 <br /> INFL 11/28/01 19 001 4 C 20 1687 375 40 110 63 3946 36 979 8 ND 01 12 231 8 <br /> INFL 12112!01 19 339 2 C 25 161 2 325 0 280 181 1856 37 165 4 15 00 DG 2325 <br /> INFL 01!02!02 19 709 4 C 25 151 3 210 10 190 11 5 2281 37 393 5 ND 00 Do 2326 <br /> INFL 02(06102 20 474 5 C 90 537 2 700 50 270 58 2759 37 669 5 NO 00 00 2325 <br /> INFL 03!08102 21 145 8 C 100 532 1 100 40 170 36 131 8 37 801 3 ND 00 00 2325 <br /> INFL 04IM02 21 8049 C 95 523 650 0 610 128 2261 38 026 4 ND CID 0 1 2326 <br /> INFL 05!01102 22 276 0 C 100 527 350 25 130 27 1523 38 178 7 052 00 01 2327 <br /> INFL 06125/02 23 043 6 D - - -- - <br /> 07!23102 231843 C 75 042 650 6 360 93 2270 38 405 6 ND CO 03 2329 <br /> 0 08706/02 23 520 1 C 75 61 7 600 20 170 42 941 38 499 7 07 00 01 2330 <br /> 09/03102 24 200 9 10%0 50 521 575 20 260 54 1365 38 636 2 ND 00 00 2330 <br /> INFL 10/01 02 24 949 8 10%0 60 51 7 575 7 76 16 1092 38 745 4 ND 00 00 2330 <br /> INFL 11/05/02 25 526 2 10%0 50 502 450 5 28 D6 257 38 771 0 ND 00 00 2330 <br /> INFL 12/03/02 26 051 8 10%0 50 51 2 475 6 38 08 147 38 785 7 ND 00 00 2330 <br /> INFL 01/07/03 26 862 1 5%0 55 473 350 5 39 07 256 38 811 3 ND 00 011 2331 <br /> INFL 02!04103 276359 C 55 487 325 5 35 07 199 38 831 3 021 00 00 2331 <br /> INFL 03/05/03 28 233 7 10%0 50 473 225 2 26 05 17 1 38 848 3 ND 00 00 2331 <br /> INFL 04101703 288300 1D%O 50 483 225 0 26 00 66 388650 02 00 00 2331 <br /> INFL 05/02103 29 622 5 10%0 50 443 275 0 28 00 00 36 855 0 ND 00 00 2331 <br /> INFL 08/05/03 29 622 6 C 50 437 100 0 54 00 00 38 855 0 ND 00 00 2331 <br /> r}� A11 O � 1ERe�C� o0103 <br /> 709RF$O . <br /> {T;7P+J' <br /> •`T 1 b V�Y�J �.1 f..f�, L'.. _ <br /> � <br /> r <br /> �,..,' <br /> �,€� <br /> Ofa'�a " <br /> 4, <br /> P k' <br /> acfm -Standard Tubb fee[par minute NS=Not sampled <br /> =Pounds a System startup Initial air samples taken <br /> lbs <br /> NA Not available or not applicable "= FID(8ame•lonlzatlon detactar)reading (Flame Out) <br /> ND =Non-detectable above detection limit <br /> ppmv =Parts per minion by volume converted from mkxogD e System <br /> C= y tslem Is down duo to repairfmaintenance <br /> valva Is efos <br /> Per utter assuming TPH as gasoline and benzene vapor s <br /> density is 0 278 and 0217 lbs per cubic foot respee6ve1y Density of benzene=7 34 pounds per gallon <br /> TPH o Total IDensity of gasoline=61 pounds per ganon <br /> 0 <br /> 7707 41737 00 000211]2.03 Lockafard O&MTablow TABLE Art <br />