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REG 603 UPDATE-7 3/24/92 <br />• <br /> the vacuum pump. After the vapor stream leaves the vacuum pump, <br /> it is pushed into the thermal oxidizer (RXL 400 ) which oxidizes <br /> the gasoline range hydrocarbon vapors at no less than 1400°F and <br /> no greater than 1550 F. Influent samples are obtained from the <br /> exit of the pump and effluent samples are obtained from the stack <br /> of the thermal oxidizer. The gasoline range hydrocarbons are <br /> oxidized into heat, CO2 and water vapor, see Figure 7 and UPDATE <br /> STATUS REPORT #5 . <br /> A portable ambient air PID-GC (Photovac 1OS50 packed column) is <br /> used at the site to sample the influent and effluent of the REMOX <br /> oxidizer, and the individual wells (MW1, MW2-3, MW10 and EX-41' ) , <br /> see Tables 2, 3 and 4 . On October 22, and 24, 1991, "Tedlar" bag <br /> samples were obtained of the influent and effluent of the REMOX <br /> incenerator and on January 20, 1992, a influent sample was <br /> obtained. These samples were analyzed for TFH and BTEX along with <br /> screening for Tetrachloroethylene (PCE) , Trichloroethylene (TCE) <br /> and 1, 2, -Dichloroethane (DCE)using a Shi.madzu GC-FID chromatograph <br /> mounted permanently in WEGE ' s portable laboratory. These <br /> compounds have the following retention times in the above <br /> chromatograph, DCE = 2. 079 minutes, TCE = 3 . 023 minutes and PCE = <br /> 3 . 75 minutes. Prior to sampling the wells or the system, a <br /> calibrant prepared from fresh gasoline is injected into the GC- <br /> PID. The resulting chromatogram has numerous responses. The <br /> microprocessor of the GC-PTD computes the area, per response, in <br /> volt seconds, and assigns a peak #, and retention time. The sum <br /> of all the responses are then used to obtain a mg/L per volt <br /> second calibrant factor, which is used to calculate mg/L as <br /> gasoline vapor from each analysis produced. Using these mg/L <br /> values produced from the anlaysis of the different vapor recovery <br /> wells and the influent to the oxidizer, and the pressure <br /> differential created at the orifice to determine flow rates for <br /> each well and the influent to the oxidizer; pounds per day can be <br /> computed. The pounds per day values for each well and the <br /> influent are then averaged to the preceeding site visits pound per <br /> day and then multiplied by the number of days the system operated <br /> between visits to estimate the total pounds each well and the <br /> system has removed for that time period. This poundage is then <br /> added to the accumulated poundage of the previous visit to update <br /> The <br /> effluent <br /> ..,rvl .-. is o ,-e%y1T111�Orl <br /> the total pounds removed mo aaue. the e� fluent saxAmple is �-...L,.... ._ <br /> in the same fashion, but also includes natural gas flow along with <br /> the influent orifice flow rate. <br /> C. 2 . SAMPLING VAPOR STREAMS <br /> The vapor samples are obtained by attaching a dedicated air tight <br /> 60 cc syringe to a sample port on the vapor recovery manifold, <br /> well side of the orifice plate, with air tight fitted polytubing. <br /> The sample port is then opened and the syringe is purged by <br /> PAGE 8 <br />