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' Former Manna Pro Site Page 11 <br /> Project No 207 3 <br />' Remedial Feasibility Study <br />' 7.0 CONCLUSIONS & RECOMMENDATIONS <br /> 7.1 Conclusions <br /> 1 The total contaminant load as gasoline range hydrocarbons was estimated to be about <br /> 22,000 pounds with the dissolved phase being about 460 pounds These figures seem <br /> to be in reasonable agreement with the GTI estimate of 1994 <br /> 2 Given the recent high stand of groundwater, in conjunction with the thick clay / silt <br /> unit, it does not appear likely that either vapor extraction, or vapor extraction with <br /> groundwater pumping offers a viable remedial alternative The most intensely <br />' contaminated interval (35 to 45 feet) roughly corresponds to a clay- and silt-rich layer <br /> These fines-laden soils adsorb petroleum hydrocarbons, greatly reducing their <br /> mobility, as exemplified by the failure of the contaminant mass to rise with the rising <br />' surface of groundwater table The adsorbed state of the bulk of the contaminant mass <br /> in conjunction with the depth of the mass below the groundwater surface would <br /> appear to render vapor extraction as a stand-alone process or in conjunction with <br /> t groundwater pumping, less than feasible We conclude that the groundwater surface <br /> would need to fall about 8 to 10 feet (to about 35 feet bgs) in order for these methods <br /> to become feasible If such a change in the water table were to occur, the sands, <br />' which are present roughly between 20 and 30 feet, could be readily treated by vapor <br /> extraction In addition, the vapor extraction would tend to desiccate the clay and silt <br /> which would increase permeability and further enhance the effectiveness of the vapor <br />' extraction method Unfortunately there is no way of knowing when such a change in <br /> natural ambient groundwater conditions might occur <br />' 3 Both vapor extraction and vapor extraction with groundwater pumping would be <br /> likely to affect only the contaminated soils in the vadose zone and in the upper few <br /> feet of the saturated zone Insofar as most of the contaminant mass lies at 8 to 20 feet <br /> below the groundwater surface, neither of these methods is likely to remove a <br /> substantial portion of the gasoline contaminant mass By including air sparging in the <br />' remedial system, the rising air in the saturated zone will help to mobilize and vaporize <br /> some of the absorbed gasoline contaminant mass, bringing it to the groundwater <br /> surface where vapor extraction method should readily remove the material from the <br />' subsurface for destruction <br /> 4 Given the current aquifer conditions, it seems apparent that unless water levels drop <br />' considerably over the next few years, the only reasonable active remedial option is <br /> that of vapor extraction with air sparging Natural attenuation would also work, but <br /> we estimate the time needed to adequately mitigate the release by natural attenuation <br /> to lie between 25 to 100 years <br /> i <br /> r2937 Veneman Ave , #13240 Geo-Phase Environmental Inc Phone(209)569-0293 <br /> Modesto,CA 95356 Fax(209) 569-0295 <br /> I <br />