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EXECUTIVE SUMMARY <br /> This PAR and CAP was prepared for regulatory review and approval The preparation of the <br /> PAR included the installation of 2 additional groundwater monitoring wells (MW-6 and MW-7) at <br /> the site so that the downgradient extent of impacted groundwater could be defined and so that a <br /> groundwater table monitoring capability could be re-established <br /> On May 1, 1998, groundwater was monitored and sampled from the 2 newly-installed wells and <br /> the 2 deep vapor extraction wells (VW-1 D and VW-21D), and the elevations of all on-site <br /> wellheads were surveyed to an established benchmark Depth-to-groundwater beneath the site <br /> ranged between 38 and 40 feet bgs and the groundwater table has risen an average of 6 18 feet <br /> since the wells were last monitored in February 1998 The groundwater flow direction remains <br /> northeast at a gradient of 0 0014 foot/foot <br /> Results of the groundwater sampling and analysis indicate that significant concentrations of <br /> gasoline hydrocarbons continue to exist in proximity to the former USTs The downgradeint <br /> extent of impacted groundwater is defined by MW-6 and MW-7 <br /> According to the existing soil analytical data, the majority of hydrocarbon mass is contained in <br /> vadose zone soil between 10 and 30 feet bgs Based on the vapor extraction testing conducted <br /> in May 1995, extraction flow rates in this interval ranged from 7 to 17 actual cubic feet per minute <br /> (acfm) at vacuums ranging from 40 to 82 inches of H2O These relatively high wellhead <br /> vacuums at low test flow rates are reflective of the relatively low permeability associated with the <br /> silt- and clay-based sediments of the vadose zone Vacuum responses of 0 2 inches of H2O <br /> occurred within an average distance of 28 feet from the extraction well Using a conservatively <br /> selected radius of influence (ROI) of 20 feet, the 4 existing vapor extraction wells (VW-1, VW-2, <br /> { VW-3 and VW-4) are constructed and positioned to effectively remediate the impacted sod <br /> A thermal oxidizer would provide the most economical initial processing and atmospheric <br /> discharge of treated extracted soil gas At a flow rate of 10 scfm per well, the anticipated TPH- <br /> 1 as-Gasoline mass extraction rate would be 216 ppd fob the full system <br /> Based on the findings of this PAR and CAP, Ramage Environmental recommends the following <br /> course of environmental corrective action <br /> 1 Upon regulatory approval of this PAR/CAP document, prepare a set of engineering plans <br /> for the design of the soil vapor extraction system, obtain the required air quality permits <br /> and submit the appropriate utility service applications The cost for these tasks has <br /> already been pre-approved by the UST Cleanup Fund <br /> 2 Solicit 3 bids to construct and operate the system The bids should be submitted to the <br /> UST Cleanup Fund for review and cost pre-approval <br /> 3 Upon UST Cleanup Fund pre-approval, construct, start-up, operate and maintain the <br /> system as specified in the design plans and bid specifications, and in accordance with <br /> the permits to construct and operate the system <br /> i 4 Continue quarterly groundwater monitoring and sampling The cost of 3 additional <br /> quarters has already been pre-approved by the UST Cleanup Fund <br /> 2 <br />