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CLEAkWA'TE-R <br /> I c a oy P <br /> Environmental Services <br /> I <br /> the source of the majority of the dissolved-phase plume appears to be this area Based on <br /> assessment results, an estimated 4,030 cubic yards (in-place) of soil with TPHg concentrations <br /> greater than 1 mg/kg reside in this area However, due to practical constraints of equipment <br />' limitations, excavation sloping, and soil decompaction, it is estimated that excavation in this area <br /> would generate approximately 15,200 cubic yards of soil <br />' Based on assessment data, shallow soils (i e less than 19 feet bgs) in the area of the sorbed-phase <br /> footprint are free of gasoline contaminants Assuming this clean soil were segregated during <br /> excavation, approximately 5,250 cubic yards of contaminated soil would be generated for <br /> treatment The space available at the site is large enough to stockpile and aerate soil, so off-site <br /> treatment of contaminated soil is not the only option If off-site treatment were necessary, NDS <br /> in Richmond, CA is the closest facility This option would also require the destruction of wells <br /> MW-1, MW-3 and MW-5B (see Site Plan Figure 2) New wells should be reinstalled following <br /> excavation to continue monitoring of maximum dissolved-phase contaminant concentrations <br /> Another consideration is that not all contaminated soil could recovered through excavation as a <br /> portion of the sorbed-phase plume hes beneath a building, and the furthest eastern edge is under <br /> South Fresno Street, where the city of Stockton has already denied encroachment permits for <br /> monitoring well installations <br /> I6 2 2 Soil Vapor Extraction and Treatment <br /> Soil vapor extraction (SVE) involves the removal of hydrocarbon vapor from soil pore space in <br /> the vadose zone by applying a vacuum to wells to induce airflow through the contaminated zone <br /> Volatile hydrocarbon constituents are released from the soil into the air stream and treated at the <br /> surface as required SVE most effectively removes hydrocarbons from the vadose zone in <br /> situations where soil permeability is moderate to high, and where the contaminants consist <br /> primarily of the more volatile hydrocarbon compounds (i a gasoline constituents) <br /> The relatively fine-grained sediments observed beneath the site are not very conducive to any <br /> technology relying on the transmission of air or water through the subsurface Therefore, the <br /> soils beneath the site are not well suited for SVE alone Also, shallow water tables can make <br /> SVE problematic (i a upwelling and occlusion of well screen), the relatively low permeability of <br /> . soils at the site would require relatively high vacuums to produce sufficient air flow rates <br /> compounding the problem Additionally, SVE alone in areas of high water table would be <br /> IZB 171C CAP 13 November 20,2002 <br />