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Table A 1 Solf Vapor Extmcdon System Performance Data Time Oil Lockeford Site 14000E Highway Lockeford Californiaia TPH oil$#aggl(pg Ben7Ane BD Influent influent Hour Meter Ambient Blower Influent Concen Removal Net Removed Concen Removal Net Removed Sample Date Reading Dilution Vacuum Flow Rate Influent Effluent tration Rate Removed to Date tration Rate Removed to Date ID Sampled (hours) Valve (H2O) (scfm) (ppmv) (ppmv) (ppmv) (lbs/day) (pounds) (pounds) (ppmv) jibs/day) (pounds) (pounds} INFL 12/13/99 7 863 1 a B%O 3 154 10 000 20 6 900 00 00 Start Up 1570 0 0 00 Start Up INFL 01/25/00 B a21 0 51/.0 20 156 1 900 10 3 990 2492 4 972 6 4 972 6 330 1 6 321 321 INFL 02/22/00 9 208 6 10%0 20 313 1 000 5 2 460 3062 4 501 1 9 473 7 338 3 3 397 71 8 INFL 03!13100 9 378 6 115%0 10 204 1910 1 2 960 2417 1 947 8 11 421 5 270 1 7 178 896 INFL 04113/00 9 394 4 1%0 161 1701 2 990 5 3 810 2594 1650 11 5136 5 245 1 3 1 0 90 6 INFL 05/03/00 9 823 2 4%0 121 101 7 1 490 5 2 620 1148 3 343 3 149290 31 4 1 0 206 111 1 INFL 06/14100 10 631 6 3%0 98 1471 795 0 5 080 2991 8 696 5 23 626 3 375 1 7 572 1683 INFL 08/09/00 10 1354 1 2%0 202 131 >10 000 2 2 330 1221 1975 230238 31 7 1 3 14 1697 INFL 09/14/00 11 523 4 C 201 1879 690 0 1 120 842 2 877 8 26 701 6 72 0 4 240 1937 INFL 10/19/00 12 031 3 C 38 9 1897 345 0 1 260 957 1 9039 28 605 5 6 33 0 4 044 202 2 INFL 11/07/00 123,509 C 181 1837 298 0 895 658 1 0754 29 680 9 4 30 0 3 418 2063 INFL 12/20/00 12 774 2 D — — — — -- — — — INFL 01/17/01 12 922 0 C 30 1921 475 0 379 291 1 1299 30 810 9 1 11 01 379 2101 INFL 02/21101 13 762 0 C 40 1912 293 0 10 08 6155 31 426 4 NO 0 0 117 211 3 INFL 03/14/01 13 928 4 C 25 1840 475 4 430 31 8 1129 31 5393 22 0 4 1 4 2126 INFL 04118/01 14 764 5 C 30 1947 375 0 $20 405 1 260 0 32 799 3 6 8 0 0 68 2195 INFL 05/17/01 15 352 4 C 25 1924 275 5 110 8 5 6002 33 399 5 NO 0 5 59 2254 INFL 06/13/01 15 797 6 C 25 19114 400 20 440 337 3913 33 790 7 80 0 0 48 2302 INFL 07/11/01 16 393 5 C 30 1915 450 0 310 238 7136 34 504 3 0 6 00 04 2306 INFL 08/15/01 17 232 5 C 25 1513 400 30 330 200 764 6 35 269 1 ND 0 0 00 2306 INFL 0910501 17 682 5 C 25 1913 400 30 490 375 6392 359083 NO 0 0 00 2306 INFL 10/16/01 183313 C 30 113135 300 0 360 200 7709 36 585 2 NO 0 0 00 2306 INFL 11/28/01 19 001 4 C 20 115137 375 40 110 83 3946 36 979 0 ND 0 1 1 2 2318 INFL 12/12/01 19 339 2 C 25 1612 325 0 280 181 1856 37 165 4 1 5 0 0 06 2325 INFL 01/02/02 19 709 4 C 25 1513 210 10 190 11 5 228 1 37 393 5 NO 0 0 00 2325 INFL 02/06402 20 474 6 C 90 537 2 700 50 270 58 2759 37 669 5 NO 0 0 00 2325 INFL 03IM02 21 1468 C 100 532 1 100 40 170 36 1318 37 801 3 NO 0 0 00 2325 . INFL 04/09/02 21 804 9 C 95 523 650 0 610 » 12 8 2251 38 026 4 NO — 0 D 011 2326 INFL 05/01/02 22 278 0 C 100 527 350 25 130 27 1523 38 178 7 052 0 0 01 2327 INFL 06/25/02 23 043 6 b INFL 07/23/02 23 184 3 C 75 64 2 650 6 360 93 2270 38 405 6 NO 0 0 03 2329 INFL 08108/02 23 520 1 C 75 617 600 20 170 4 2 941 38 499 7 0 7 00 01 2330 INFL 09/03/02 24 200 9 101/.0 50 .521 575 20 260 54 1365 38 636 2 NO 0 0 0 0 2330 INFL 10/08/02 24 949 8 10%O 60 517 575 7 76 1 6 1092 357454 NO 00 0 D 2330 INFL 11/05/02 25 526 2 101/.0 50 .502 450 5 28 0 6 257 38 771 0 ND 0 0 0 0 2330 INFL 12/03/02 26 051 B 10%O 50 512 475 6 38 0 8 147 38 785 7 ND 00 Do 2330 INFL 01/07/03 26 862 1 5%0 55 473 350 5 39 0 7 256 38 811 3 ND 00 o f 2331 INFL 02/04/03 27 535 9 C 55 487 325 5 35 0 7 199 38 831 3 021 0 0 00 2331 INFL 03/05/03 28 233 7 10%O 50 473 225 2 26 0 5 171 38 848 3 NO 0 0 00 2331 REPORTING PERIOD 01 M110310 00131103 YOTAL POUNDS REMOVED 38,849.9 2331 TOTAL GALLONS RF-MOV90 BAMS 31 8 PERIOD POUNDS REMOVED 620 01 PERIOD GALLONS REMOVED 103 00 PERIOD AVO FLOW RATE. 48 PERIOD PERCENT frPIERATIONAL. 99% scfm =Standard cubic feet per minute NS=Not sampled Ibis =Pounds a System startup mthai air samples taken NA =Not available or not applicable = FID(6ame Ionization detector)reading(Flame Out) ND =Non-detectable above detection limit Please note No samples were taken in July because the remediatton system was down ppmv =Parts per million by volume converted from micrograms C-dilution air valve is closed per liter assuming TPH as gasoline and benzene vapor D=System is down due to repair/maintenanoe density Is 0 278 and 0 217 lbs per cubic foot respectively Density of benzene=7 34 pounds per gallon TPH -Total Petroleum Hydrocarbons Density of gasoline=6 1 pounds per gallon 770T 41737 00 0002!01-03 Lockeford O&MTables/rABLE A 1