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subsurface, and potentially cause temporary increases in the mobility of hydrocarbons Air <br /> quality issues during excavation would need to be addressed Additionally, areas of <br /> Isuspected residual hydrocarbons beneath Rosemarie Lane and the property north of the site <br /> would be left in place <br /> • Enhanced Bioremediation. Due to the predominance of low permeability zones under the <br /> site, substances used to enhance intrinsic biodegradation such as oxygen and nutrients will be <br /> Idifficult to deliver to the appropriate locations <br /> 0 Steam Stripping. Although this technology is aggressive for source remediation, it involves <br /> an extremely high cost, especially for source areas which are primarily trapped below the <br /> water table In addition, the need for removing residual LPH in low permeability soils greatly <br /> reduces the efficiency of this technology, and increases the energy demand To infect steam <br /> or hot water into a low permeability zone 35-45 feet bgs, multiple temporary injection wells <br /> would be required The addition of heat and/or liquids below the water level in areas that <br /> contain LPH and residual phase hydrocarbons can cause downgradient mobilization due to <br /> changes in pore pressure These changes in conditions alter the saturated zone Soil vapor <br /> extraction wells and water/vapor treatment would also be required Thus, both cost and the <br /> logistics of implementation make this technology less acceptable under the current <br /> conditions <br /> 0 Air Sparging and Soil Vapor Extraction (SVE). SVE is only applicable for the vadose <br /> zone Although it is a useful technology for vapor control, it cannot be used alone for <br /> removal of hydrocarbons below the water table Air sparging in conjunction with SVE was <br /> implemented at the site from 1994 to 1996 Two air spargmg wells and three SVE wells <br /> were installed at and near the downgradient edge of the former tank field area As described <br /> 1n Section 2 7 and shown in Figure 10, SVE influent concentrations and the cumulative <br /> estimated pounds of TPH-g removed became asymptotic over time The water table has <br /> increased by approximately 4 feet since 1996 Because the saturated zone is heterogeneous <br /> and largely silty, infected air is not uniformly distributed around the air Sparging well and <br /> instead flows in preferential channels in the saturated zone, making hydrocarbon removal <br /> from fine-grained materials and hydrocarbon vapor recovery difficult Based on current site <br /> conditions and former operational experience, further use of this alternative is not expected to <br /> be effective <br /> • Groundwater Extraction with In-well Air Stripping (UVB). Groundwater recovery well <br /> RW3 was converted to a UVB well in 1996 A UVB system was operated in this well from <br /> February 1997 to September 2000 Extracted groundwater was pumped from the lower <br /> screened interval of the well, which is screened from 35 5 and 39 5 feet bgs The upper <br /> screened interval where the lifted and VOC-stripped groundwater was discharged from is <br /> screened from 24 8 and 32 feet bgs UVB systems have the same inherent limitations of a <br /> groundwater pump-and-treat system, which are the lack of solubility of hydrocarbons in <br /> groundwater and partitioning of hydrocarbons between groundwater and soil <br /> Heterogeneities within hydrocarbon-impacted soils result in preferential groundwater <br /> • pathways through more permeable soils, which typically contain less hydrocarbon mass than <br /> finer-grained soil The concentrations of TPH-g and benzene over time in well UVB-MW 1 <br />' G1Projects1739421MA5TER\WP\%W3031WPtxdoc 15 <br />