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1 <br /> 70 PROPOSED CORRECTIVE ACTION PLAN <br /> Based on the nature of the soil impacts beneath the site, and based on the results of the VET as <br /> described herein, Geocon recommends soil vapor extraction as the most feasible and cost effective <br /> interim corrective action option Test data indicates that vapor extraction has the ability to remove <br /> 1 hydrocarbon mass from beneath the site without further excavation and can utilize the existing <br /> extraction well <br /> The soil remediation goal for the subject site is to reduce the concentrations of TPHg in soil to below <br /> 100 mg/kg, this soil remediation goal is supported by the following discussion Geocon's previous <br /> experience in the operation of VES's indicates that the degree of soil contaminant reduction varies in <br /> accordance with the length of extraction and the mass removal decay rate Typically, if a soil VES is <br /> operated until the mass removal rate has dropped to approximately less than 5 ppd, resultant post- <br /> remediation soil concentrations are usually less than 100 mg/kg The operation of vapor extraction <br /> systems at mass removal rates significantly less than 5 ppd is not considered cost-effective because <br /> ' the residual contaminant mass consists of the heavier end range of the petroleum hydrocarbon <br /> product, which are difficult to extract due to decreased volatility <br /> This section outlines the proposed Corrective Action Plan (CAP) by providing preliminary design <br /> criteria and scheduling information relative to the design, permitting and operation of the VES In <br /> addition, this section presents a site specific VES layout which includes proposed subsurface trench <br /> routes and the aboveground remediation equipment compound location <br /> 7,1 Preliminan Design Criteria <br /> A VET was performed to simulate future vapor extraction and obtain preliminary design criteria for <br /> ' a VES Data obtained from the VET indicated that a vapor extraction well flowrate of approximately <br /> 60 scfm can be achieved However, the final VES design will include maintaining a flowrate of 100 <br /> scfm in order to produce an ROI of sufficient size to achieve remedial coverage of the entire on-site <br /> impacted soil plume The VET data also indicated that a TPHg vapor concentration of approximately <br /> 33,000 mg/m3, as limited by the processing capacity of the therm-ox, with a corresponding mass <br /> ' extraction rate of approximately 300 ppd can be expected at the time of VES start-up The results of <br /> the VET indicated that vapor extraction technology is a feasible remedial alternative for the site The <br /> ' preliminary design criteria for the VES is summarized below and a VES Capture Zone and Layout <br /> Map for the subject site is depicted on Figure 7 <br /> ' o Number of vapor extraction wells= 1 <br /> C Recommended extraction flowrate of the extraction well = 100 scfm <br /> ' 0 VES Maximum Process Capacity Specification = 150 scfm <br /> a Estimated TPHg vapor process concentration at start-up= 33,000 mg/m3 <br /> O VES TPHg mass extraction rate at 100 scfm = 300 ppd <br /> Project No 58100-06-18A -16- December 9, 1996 <br />