Laserfiche WebLink
CALCULATION SHEET H-2 <br /> SITE CALCULATIONS — AIR SPARGING EMISSIONS <br /> Former Canteen Facility <br /> 1500 Shaw Road <br /> Stockton, California <br /> Air Sparging <br /> Parameter Units Definitton Benzene TPHNOCs <br /> Input Parameters <br /> Q scfm Total Air Sparging Flow Rate 21 0 21 0 <br /> C, mg1L Initial Dissolved-Phase Concentration 240 180 <br /> Cf mg/L Final DLSSOlved-Phase Concentration --- — <br /> Eff – Air Sparging Efficiency 100 1 00 <br /> Pto1 atm Pressure within Water-Bearing Zone 1 00 1 00 <br /> Constants <br /> H, atm Henry's Constant for Component Y 02 32 0 232 <br /> Csp, mglL Solubility of 'r'from Gasoline in Water 5870 1187 <br /> M glmole Molecular Weight 7811 9505 <br /> Intermediate Calculation Results <br /> X, molelmolew, Mole Fraction of Component i' in Water 5 531 E-06 3 409E-05 <br /> Y, molefmole„ Mole Fraction of Component Y in Vapor 1 283E-08 7 908E-06 <br /> C„ap ppmv Vapor Phase Concentration of Component 1 1 283 7 908 <br /> C„ap Mg/M3 Vapor Phase Concentration of Component 4 230 2607 <br /> Output Parameters <br /> Eh. lbs/hr Hydrocarbon Remediation Rates 00003 00021 <br /> Eh. lbs/day Maximum Dally Remediation Rates 00080 00492 <br /> Note <br /> The monitoring wells exhibiting the highest dissolved-phase hydrocarbon <br /> concentrations {MW-3 and MW-13} were utilized In determining the estimated <br /> vapor-phase concentrations of the hydrocarbons volatilized by the air sparging <br /> system <br /> Job No 340092 August 22, 1996 <br />