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M EN- = M M wM M ! =4r M TABLH 2B VAPOR EXTRACTION TEST MONITORING DATA Fire Engine Company No 2 116 West Sonora Sired, Sfackton, California January 16, 1994 (Page I of 1) Air Stream Conditions for Vapor Extraction Wall VW 1 Observation Wall Vacuum (In 1410) Vapor Sample Collection and Analyal■ (mplm31 Time Air Air 0 Vacuum Tamp VW 4 MW 1 VW 26 VW VW 6D Vapor Benzene Toluene Ethyl Total TPHp Velocity Flowrate Conc 55 Sample No Benzene Xylenes (fpml (acfm► (ppm) (In 1120) (F) 9 30 1000 87 0 2 4 63 0 000 029 >0 26 046 035 1000 000 09 B 6800 2 4 680 001 032 039 046 0 34 1030 800 99 a 7000 2 4 60 4 001 031 037 043 033 A 0118 INF1 106 06 100 240 7,200 11 00 900 78 3 8300 2 7 fib 8 000 035 044 061 0 38 11 30 900 78 3 5800 2 6 70 2 000 032 042 060 1 O 36 A 0118 1NF2 130 210 1 140 320 10000 1200 600 62 2 5800 1 7 89 0 0 015 020 027 031 022 12 30 600 62 2 1 7 704 002 0 19 026 030 021 A-0118 INF3 100 170 88 190 1 18180 Distance from Vapor Extraction Wall VW 1 ((eat) 16 5 10 8 Ali Stream Conditlone for Vapor Extractlon Wall VW 50 Observation Well Vacuum Un H10) Vapor Sample Collection and Analysis ling/ml] Tlme Air Alf OVA Vacuum Tamp PT 1 VW 1 VW 2D MW 1 Vapor Benzene Toluena Ethyl Total TPHp Velocity Fiawrate Conc sample No Benzene Xylanoa tfpm) tacfm) (ppm) (In H2O) (F► 1300 2200 191 4 22 9 684 000 000 0 OB 009 13 30 2500 217 5 >10K 35 I fib d 009 000 022 O 13 14 00 2600 217 6 >10K 36 7 68 d 009 002 028 022 A O1 18 iNF4 61 30 36 34 17 000 14 30 2500 2 1 7 6 >10K 36 5 09 8 0 02 003 0 30 0 23 1600 2600 217 6 >10K 35 8 do 0 000 003 O 31 0 23 A 0118 INFb 46 30 2B 24 .17000 16 30 2600 226 2 >10K 30 1 67 0 001 002 030 O 22 19 00 2800 2213 2 >16K 36 1 65 8 001 002 0 30 0 22 A-0118 INFO 14 21 26 20 16,000 A 0118 EFF 0 17 0 26 0 57 2 4 29 Distance from Vapor Extraction Well VW 6D {foot) 4 4 170 156 22 1 I 38009138009-08WRP TBIS WPS