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_ .Moe <br /> to create negative pressures for vapor removal. A process control system is used to monitor and adjust <br /> the air deliveryand removal equipment. Additional aboveground equipment may also include a knockout <br /> pot to separate liquids from the vapor stream and a vapor treatment system. Once the extracted mass <br /> ` removal rate has reached an asymptotic level,the AS/SVE system can be run intermittently to be more cost <br /> effective. <br /> r <br /> SVE is implemented by applying a vacuum to the vadose zone to remove vapor phase contaminants from <br /> the soil above the groundwater table. AS is used in conjunction with SVE to inject air into the <br /> �- contaminated groundwater and extract vapor in the unsaturated vadose zone above the aquifer using 2-inch <br /> diameter AS wells installed into the aquifer. This technology also promotes biodegradation in saturated and <br /> unsaturated soils by increasing subsurface oxygen concentrations. Air is bubbled into the aquifer and <br /> travels both horizontally and vertically,removing contaminants byvolatilization. Volatilized contaminants <br /> would then be removed by SVE. <br /> L <br /> 4.2.1.2 Evaluation <br /> In situ AS/SVE techniques have been shown to be effective for treating volatile contaminants in <br /> groundwater and have been implemented successfully at many sites. However,this technology is relatively <br /> difficult to implement as it would require afield pilot studyto obtain the information necessary to design and <br /> configure the system,along with the installation ofan estimated 10 AS wells and,assuming a 50-foot radius <br /> ofinfluence,three SVE wells. Approximately 600 feet ofAS piping and 350 feet of SVE piping would be <br /> ` required and 13 vaults would be used for well head completion. Installation ofwells would require closing <br /> local streets, and trenches for underground piping would need to be constructed and backfilled. In <br /> addition,there are several utilities in the area that would require working around or relocating. The <br /> treatment unit,including piping,connections,compressors,vacuum pumps,and air monitoring equipment, <br /> would need to be placed in the vicinity ofthe intersection of Sutter Street and Washington Street,a highly <br /> visible and busy downtown comer. This technologyrequires significant operation and maintenance(O&M) <br /> costs; however, since the groundwater is treated in place, there is no need for disposal of treated <br /> groundwater. The effectiveness ofthis technology is also questionable as the soil in the contaminated zone <br /> consists of silt and clay(Lithologic Zone 4)overlain by sand and gravel(Lithologic Zone 3). AS/SVE <br /> technologies depend on the air permeability ofthe soil. SVE applied in the upper,more permeable zone <br /> would have much greater effectiveness. Finally,this technology is most effective when soil and groundwater <br /> concentrations are high and is much less effective when contaminants reach an asymptotic state,as they <br /> currently have at the site. The return,or amount of contaminants recovered,per dollar spent is not as <br /> favorable as it would be at more contaminated sites. WESTON therefore recommends that the in situ <br /> AS/SVE technology not be considered further. <br /> 10 <br />