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F.. <br /> FiV <br /> 6.0 CONCLUSIONS/RECOMMENDATIONS <br /> The test data ::..eve demonstrated that vapor extraction is an <br /> effective approach to the remediation of gasoline hydrocarbon <br /> contaminated soils at the subject site. The current placement of <br /> vadose wells VP1, VP2 and VP3 are adequate to affect the area of <br /> impacted soils in the tank pit area, as identified by soil sam- <br /> pling. Because boring ASBI identified an area of elevated soil <br /> hydrocarbons beneath the island along the east side of the <br /> property, a single vadose well will be placed in that area. Each <br /> well will operate at vapor extraction rates of approximately 30 <br /> to 70 cfm <br /> Four alternatives for control of extraction system off-gas emis- <br /> sions were evaluated. These are thermal oxidation, catalytic <br /> oxidation, carbon adsorption and destruction by an internal <br /> — combustion (IC) engine. Based on the relatively low levels of <br /> hydrocarbons in the vapor samples and the relatively high perme- <br /> abilities a combination of vapor phase carbon and an IC engine <br /> are recommended. The IC engine will be utilized for the initial <br /> extraction period (anticipated 30 to 60 days) during which vapor <br /> concentrations drop rapidly. After the extraction stream drops <br /> below approximately 10 lbs/day of hydrocarbons, the IC engine <br /> will be removed and replaced with activated carbon canisters, <br /> - Each wellhead will be equipped with vacuum gauges, sample port <br /> and control valve so that the flow rate can be adjusted to maxi- <br /> mize recovery rate. The IC engine is capable of drawing up to <br /> - approximately 150 cfm depending upon soil conditions. It is <br /> estimated that the TPH as gasoline concentrations in vapor re- <br /> moved from the wells will be reduced below 558 ug/l (125 ppmv) <br /> within 60 days of operation. The system would then be converted <br /> i to use activated carbon and a vacuum blower to complete the <br /> remediation. It is estimated that the blower/carbon adsorption <br /> - unit will operate for approximately 150 to 220 days. <br /> { <br /> 7.0 REFERENCES <br /> ~ Bear, J., 1979, Groundwater Kdra.ulics, McGraw Hill, N.X. <br /> Johnson, P.C., Kemblowski, M.W., Colthart, J.D., 1990, Quantita- <br /> tive Analysis for the Cleanup of Hydrocarbon Contaminated <br /> Soils by In-Situ Soil Venting, Groundwater, V.28, 11o.3, <br /> r, pp.413-429. <br /> 4 <br />