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AoC°. ". :.F. ar a "a••a •�u, a n ..v-, <br /> ��a- <br /> s. ll <br /> �.a <br /> MAL REMEDIATION PIAN_ <br /> Shell Oil Company <br /> 620 West Chatter Way,Stockton,California <br /> Delta Project No.4 .88-586 <br /> Page 21 <br /> 'The thermal oxidizer reduces hydtoc-arbon emisriord to tho`atm*hefe with a destruction efciefiq beta. , <br /> t a X95 and 0993 pesaa k and is most cost-effective athydrocarbon ydrocarbon concentrations above.3Au"+7,"m.--Since . <br /> extrtctioneancentrallons of'approicfmatefyi`12;lXlb`ppm tveie3 eb�erved during[eats, ►al ozidiaer:will- <br /> i a la:nsed during the brat phage of site remodiationa <br /> i ' <br /> 44 Conrentu„i Resign <br /> Soil remediation will be accomplished by soil vapor extraction. Results of the soil vapor extraction test <br /> i a (which can be found in Section 3.5.2 and Appendices E and F of this report)indicate that soil venting is a <br /> (" feasible soil remediation method. Figure 9 shows the process flow sheet for the soil and ground water <br /> 15 remediation system. <br /> Initially, monitoring wells MW-2, MW-7, and MW-9 will be opened to the inlet side of a positive <br /> . ., displacement blcwer. Monitoring wells MW-2 and MW-7 were selected as active vapor extraction wells <br /> because of their relative locations within the free product plume. Monitoring well MW-9 was chosen as an <br /> active vapor extraction well because this soil boring contained high TPH concentrations(see Table 1). TO <br /> 3 <br /> maintain a proper vapor exchange rate in the soil,55 cf n per well must be achieved. For vapor exchange <br /> rate calculations,see Appendix F. 'Pira blosrertlet vrill-be directed toxtlt2 followitag emissivtt vontrol <br /> ,deviers-durfng the-coursa'cf system operation a•thermal oxidizer,`lintit-hydmmrbon-c�ncentmtiom fall- <br /> . � <br /> 1 s .bdow"3,w'ppm,.then.possibly-to a-'castalytic-oxldizer.-When-hydrocarbon concentrations-fall-below <br /> 14 <br /> approx1mately"150 ppm;soil test borings will be dolled to determine remaial S con=ntrations4wzoll:;Llf• <br /> closure cannot-be obtained at this time,the:od.vapor;,Wraction systemlmay:be.veatcd through,activatgd <br /> i carhowuntil•elosttre can be obtained through later confirmation bodngs..t 7401 specific-thermal•osidize� <br /> l: <br /> chown,for the fast ph.".of site remadlation v4ll be included in the final authority to construct penait from <br /> 5 the APCD.-ta5orizatfor.Teggrding all of the units will b6provided with thrs permittl to canssruet snd.apt:ca ceA <br /> If in the future,additional soil venting is required,monitoring wells MW-3,MW4,and MW-5 can be opened <br /> 11 for venting singe these wells are already manifolded. Figures 11 and 12 show the system layout. Figure 10 <br /> t <br /> shows the inferred vacuum influence of monitoring wells MW-2,MW-7,and MW-9. <br /> l <br /> Thhe_therma1.oxulizer and catalytic oxidizet.units,wili,he skid!.mounted,apd,w)[l,include ase arateblower, <br /> l�. <br /> 1 � <br /> r4 <br /> t <br />