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Cvapor =H*Cliquid: <br /> where, <br /> a = bulk density (kg/1), <br /> b = volumetric water content within the soil volume (dimensionless), <br /> c = volumetric air content within the soil volume (dimensionless), <br /> Kd = distribution coefficient (1/kg), and <br /> H = Henry's Law constant (dimensionless). <br /> Soil physical parameters used in the model include density, soil moisture <br /> content, and void ratio (porosity). The soil parameter values used in the model <br /> are presented on Table A-2 and are representative values for the soil type present <br /> at Tracy Yard. <br /> Thus soil vapor concentration can be estimated by Jury Model using average soil <br /> VOC concentration and soil physical parameters. For Tracy Yard, average soil <br /> concentrations were calculated using site characterization information available <br /> on VOC source area. Soil concentrations from borings SB6, MW-14B, TW-2B, <br /> TYB 29, TYB30 and TYB 31 were utilized for estimating average VOC <br /> concentrations within the target area of dual phase remediation system. Using <br /> the Jury Model and soil analytical results from the above borings, concentrations <br /> of VOC in vapor were estimated and are provided in Table A-2. <br /> Vapor Phase VOC Contribution from Ground Water <br /> Contribution of VOC concentration resulting from chemical transfer from <br /> ground water to the vapor phase was estimated based on average ground water <br /> concentration from recent ground water monitoring data. A flow rate of 75 cubic <br /> feet per minute (design capacity of the dual phase system) was used to estimate <br /> resulting concentration from volatilization of 90 percent of relevant chemicals to <br /> the vapor phase. Table A-3 summarizes calculation for this estimate. <br /> Net Vapor Phase VOC Concentration from Soil and Ground Water <br /> Net vapor phase VOC concentration resulting from contribution from soil and <br /> ground water in Tracy Yard is presented in Table A-2. <br /> A-2 <br />