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i <br /> 1 <br /> ' TABLE 5 <br /> ESTIMATED VAPOR EXTRACTION SYSTEM HYDROCARBON MASS REMOVAL <br /> 102 S Wilson Way <br /> Stockton, Calafomia <br /> Page 4 of 4 <br /> ' Period Hours CumMours Avg Flow Avg Vapor Mass Cumulative <br /> (ctm) Conc. Removed Mass Removed <br /> (pg/1) fibs) (lbs) <br /> 100 7,100 350 210 28 11,465 <br /> ' 100 7,200 350 240 31 11,496 <br /> 100 7,300 350 270 35 11,531 <br /> ' 100 7,400 350 300 39 11,570 <br /> 100 7,500 350 290 38 11,608 <br /> ' 100 7,600 350 280 37 11,645 <br /> 100 7,700 350 275 36 11,681 <br /> ' 100 7,800 350 270 35 11,716 <br /> 100 7,900 350 265 35 11,751 <br /> 100 8,000 350 260 34 11,785 <br /> 100 8,100 350 250 33 11,818 <br /> t100 8,200 350 225 30 11,848 <br /> 100 8,300 350 210 28 11,876 <br /> ' 100 8,400 350 185 24 11,900 <br /> 100 8,500 350 170 22 11,922 <br /> ' 100 8,600 350 160 21 11,943 <br /> 100 8,700 350 170 22 11,965 <br /> ' 100 8,800 350 (160) (21) (11,986) <br /> 100 8,900 350 (150) (20) (12,006) <br /> ' 100 9,000 350 <br /> 11 Totals 8,900 -- -- 112,006) (12,006) <br /> ' Note Vapor concentrations graphically interpolated from laboratory analytical data Values in <br /> parentheses are extrapolated estimates <br /> ro&\gj n A1b15nws rrm <br /> I <br /> I <br />