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i <br /> 440 West Charter Way, Stockton, California September 16, 1992 <br /> Texaco Environmental Services Page 4 <br /> (wells 1 A and 3A were the only wells which did not have enough influence on adjacent wells to <br /> determine a radius of influence The greatest recorded induced vacuum of 17 inches of water <br /> was observed in VE-26, when vacuum was applied the VE-2A This extremely high induced <br /> vacuum is probably attributed to an inadequate bentonite seal between the two screened <br /> sections within VE-2 <br /> The radius of influence was graphically determined for each measured condition from a log- <br /> normal plot of drawdown versus distance (Appendix B) The radius of influence was defined as <br /> the distance at which measured vacuum would be 0 1 inch of water Because of the variety of <br /> extraction levels and monitoring levels, the radius of influence was determined for each <br /> extraction level by only using monitoring data acquired from the same stratigraphic level <br /> Interpretation of the results is greatly simplified into a single radius of influence for each <br /> individual well The results are summarized in Table 2 <br /> Based on the log normal plots of drawdown versus distance, the measured radii of influence for, <br /> the VE's ranged between 23 and 54 feet and were highly asymmetric, indicating anisotropic <br /> pneumatic conductivity of the subsurface materials The average radius of influence was <br /> approximately 40 feet Conservatively, a 20 cfm flow rate will produce approximately a 25 <br /> foot radius of influence, overlapping the influence field of the neighboring VE's A 25 foot i <br /> radius of influence and the placement of the vapor extraction wells is sufficient to influence the <br /> area containing adsorbed hydrocarbons in the subsurface Hence, by drawing vapors from all <br /> the extraction wells at a flow rate of 20 cfm, a 160 cfm total flow is required' However, this <br /> flow is subject to change based on the operating parameters for the off-gas control device to <br /> be used to destroy hydrocarbon emissions If necessary, vapors can be drawn from individual <br /> wells by manifoldmg the system together and providing independent valves for each extraction <br /> well <br /> Table 3 summarizes laboratory analyses yses of hydrocarbon concentrations in vapor collected on <br /> June 24, 1992 Copes of the complete laboratory reports and chain-of-custody manifests are <br /> presented in Appendix C Laboratory analyses reported concentrations of TPH-G ranging from <br /> 4,700 to 30,000 ug/I in the A level wells and from 3,300 to 21,000 Ng/I in the B level VE's <br /> Benzene concentrations ranged from 86 to 240 ug/l in the A level and 55 to 500 Ng/1 in the B <br /> . level VE's The average concentrations of vapors extracted from all the wells was <br /> approximately 1 1,500 Ng/I TPH-G and 200 Ng/l benzene rI <br /> GROUNDWATER <br /> I '' i�� TECHNOLOGY <br />