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SJVAPCD September 12,2003 <br /> Authority to Construct/Permit to Operate <br /> Page 3 <br /> Based on the highest influent concentration (160,000 mg/m3) observed during the <br /> feasibility test, and considering the destruction efficiency (98 percent) of the proposed <br /> equipment, the estimated mass emission rates for TPHG with a maximum flow rate of <br /> 200 scfm is approximately 9.25 pounds per day (lbs/day). Since the oxidizer units are <br /> generally identical with the same manufacturer's destruction efficiency of 95-98 percent, <br /> the emission rates for these units will also be identical. <br /> Stratus anticipates the influent soil vapor petroleum hydrocarbon concentrations to the <br /> proposed units to be similar or less than the concentrations observed during the feasibility <br /> test, and hence, lower mass emission rates. Table 1 presents the maximum stack <br /> emission parameters for catalytic mode of operation. These parameters are based on the <br /> maximum capacity of the blower and oxidizer. <br /> SVE SYSTEM START UP AND OPERATION <br /> Stratus proposes to conduct system start-up and source testing programs for the SVE <br /> remediation systems during the first seven days of system operation. The following <br /> parameters will be monitored and recorded on field data sheets during the system start up: <br /> • Vapor extraction rate, <br /> • Applied vacuum at each vapor extraction well, <br /> • Influent flow into the system, and <br /> • PID measurements for organic vapors from the extraction wells. <br /> During the source testing, two sets of influent and effluent air samples will be collected <br /> from each SVE unit and forwarded to a state-certified laboratory for analysis. The first set <br /> of air samples will be collected on the system start-up day, and the second set of air <br /> samples will be collected seven calendar days after the start-up date. The air samples will <br /> be analyzed on a 24-hour turnaround basis for TPHG by United States Environmental <br /> Protection Agency (USEPA) Method 8015, and for benzene, toluene, ethylbenzene, total <br /> xylenes (BTEX), and MTBE by USEPA Method 8260. Analytical results will be used to <br /> calculate the destruction efficiencies of the two SVE systems. Manufacturer's literature <br /> states that the destruction efficiency of both the oxidizer units for petroleum hydrocarbons <br /> is 95 to 98 percent. <br /> Table 1 presents the maximum stack emission parameters for catalytic mode of operation. <br /> These parameters are based on the maximum capacity of the blower and oxidizer. They do <br /> not necessarily represent typical operation flow rates of the system. <br /> Upon receipt of analytical results, a source test report will be prepared and submitted to <br /> San Joaquin Valley Air Pollution Control District(SJVAPCD) presenting the analytical <br /> results of vapor samples, tabulated field observations, and destruction efficiencies of the <br /> system. <br /> P:\Bp-Arco for URS\6100\Correspondence\Arco 6100 ATC appGcationAm <br />