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E <br /> `4 Mz <br /> tixT <br /> FINAL REMEDIATION PLAN <br /> Shell OR Company <br /> 620 West Charter Way,Stockton,California <br /> Delta Project No.404M-586 <br /> Page 20 <br /> 4.3 Emission ControlSystemsand Permlftin2 <br /> Specific r-ir discharge requirements mist be met when operating any soil or ground water remedial system <br /> that emits hydrocairbow to the air under the jurisdiction of the San Joaquin County Air Pollution Cont rot <br /> District(APCD). The APCD requires the use of best available control technology. The pump and vapi-I­ <br /> extraction indicate that in order to meet the discharge limits,an einission control devicc'wil,'be <br /> t tlto site",,T?Lrw emission control dvim-granular activated carbon filters,a catsil Hb'ft&4, <br /> -4md'i the ziM'oajdi=lutye been evaluated. Appendix F gives more details on the rationale of emission <br /> control device selection. <br /> 4.3.1 Granular Activated Carbon Unit (VaMr-Phase) <br /> Activated carbon captures nearly 100 percent of the influent hydrocarbon.. Activated carbon would be a <br /> cost-effective emissions control alternative only at hydrocarbon vapor c-incentrations less than 20U ppm and <br /> at a flow rate of approximately 100 cfin. Siticetthe data obtained from the soil venting and ground water <br /> pump test indicate hydrombonconcmtmtions-at,laround JZ000 ppm,--this-altern2&6 Is nofie666midhl <br /> -during this phasd bf the project. <br /> 4.3.2 Catalytic Oxidizer <br /> Tle catalytic oxidizer incorporates the use of platinum catalyst to oxidize hydrocarbon vapors. Catalytic <br /> oxidizers normally operate with a hydrocarbon destruction efficiency of between 90 to 99 percent. The <br /> catalytic oxidizer is most economical for hydrocarbon vapor concentrations between 150 and 3,000 ppm. <br /> Since!he vapor hydrocarbon concentrations from the soil venting and ground water pumping test were found <br /> to be approximately-12,000 ppm,the use of the catalytic o)ddizer,would not be.economical. <br /> 64 <br />