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i <br /> <---Section B <br /> former <br /> fuel island <br /> MW- 1 B-S B- ! B-6 <br /> DEPTH r .d: remedial DEPTH <br /> (feel) tank 13-1-15 B-I-20 ¢et) <br /> excavation j B-411 11 - 554 <br /> B-5.15 limits ' T - 484, T - 203,000 <br /> MWI•IS B - ND 1 E = 395,000 E - 154,000 B•6-I5 <br /> 10 B - ND T - 384,000 X - 2,000,000 X - 729,000 /�I <br /> ll=ND 10 <br /> T = 18.2 E - 30,000 .,,�� G - 22,400 G 11,250 <br /> E - 5.5 X = 1,300,000 - \ D - ND D - ND -_6-20 <br /> X - 22.7 MW-1-20 9�,� G = 26 \ B-5-25 1. B-1-25 \ ' \ AU-ND <br /> G = 1,45 B = ND �� \ \ \ B - 92,000 \B = 298 B-I-30 <br /> 20 T = 16.4 /, \ `.. \ B-5.20 T 37,000 \ T = 10,900 \ B - 489 B-6-25 20 <br /> E = 5.4 //\ B - ND E = 223,000,.\ E = 7,580 T - 191\ B - ND <br /> X = 54 MW-1-25 \ T = 114,000 \' X 1,250,000 X = 20,500 - E = 35.1 T = ND <br /> G = 1.56 ` B�' E = ND \ G 70.7 \ G 1,850 X - 144 E = ND <br /> \ T 2L2 X = 143,000 \ \ \\ D = ND G - 1.10 X = IT7 <br /> 30 \ E = 6"2 G = 25.1 \ \ B-S-30 \ \ D - ND \ \ G ND 30 <br /> P \ X = 26.2 ` \ \ B - 99,000 \ B-1-35 <br /> g-6-30 <br /> G = 164 MW-1-30 �\ T - 736,000 B - 578 8-I•10 \ T <br /> MW-1-35 \" B - ND E - 226,000 \\ - 591 \ B - 86.9 B-6-35 T - ND <br /> B - ND - ` ` T = 16.9 \ X = 1,250,000 E = 227 T - 23.5 AU-ND E = 112.05 <br /> 40 T = 10.8 MW-1-40 E - ND G - 40.0 \X = 498 E - 101 \ X - 122.1 40 <br /> E = ND B = ND \ X = 15,8 \\ ` \ �`\\ G - 5.60 X - 476 \ \ G - 9.2 <br /> X - 8.9 T = 12.6 MWA45 - G = 1.25 \ -5.35 D - ND \\ G - 31.2 t <br /> G - 2.0 E = ND B = 58.5 B - 186,000 \ B-1-45 D - ND \\ \ B-6-40 <br /> \ X = 10.8• T = 14.9 B-5-40 T - 1,260,000 B - 2,450 <br /> B-6-45 B - 38.65 <br /> 50 --_WT - \- G _ 1.82\ E __ND--- B - 145,000 �{�'/' _ E_= 424,000 T = 7,250 S•1-50 _ B__ 67.64 T - ND 50 <br /> ------- ---------- <br /> X = 12.3" T - 132,000 / X - 2,320,000 E = 4,200 8 - 2,850 / T - ND E - 32.69 <br /> G = 1.55 E 323,000 / p - 371 / X - 15,900 / T - 253 / /E - ND X = ND <br /> X = 1.9 000 / G = 235 C - 301 X - ND G - ND <br /> /MWL50 G = 420 / / j D - 'ND / X - 2,000 / / G - ND % <br /> 60 B = ND / / 8-5-50 / / G - 148 / 60 <br /> T = ND - B-5-45 50,000 X/B•1.56 D - ND .-/ B 6-50 <br /> AU-ND <br /> E = ND T = 222,000 T = 181,000 B - 415 / r / AU-ND <br /> X - 121 T = 743,000 j E = 06,000 � T - 415 " <br /> G - 1.39 E = 220,000 X = 351,000 E - 91.8 <br /> 70 / X = 1,210,000 G. = 442 /• X = 573 i <-Section B 70 r <br /> G = 9.86 G = 18.9 <br /> � D - ND , <br /> MW-I-WATER (45'fi5) / / L.eQettd: <br /> B = 3.450 ug L 9 B-Bervsrx,ug kg <br /> 80 T = 20,600u8/L p T=Tohune,ugJkg 80 <br /> E = 2,530 uWl. E-Ethyl Benzene,ug/kg <br /> X = 12,406%iWL X-TuW Xylaxs,ug/Igl <br /> 0 40 G = 269 mg/L G-Gasobne,mg/kg <br /> D-Dtesc�mg/k8 <br /> 90 I 90 <br /> Horiz.Scale(feet) <br /> Canepa's Car Wash Figure 9 <br /> 248 E. Park Street, Stockton, California Contamination <br /> Cross Section A -A' <br /> HF,Inc.P.O.Box 570729,Modesto,CA 95357-6729 (looking North) <br /> SEC A-A'.XLS <br />