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a — <br /> 15 April 1996 - r <br /> AGE-NC P <br /> Paa ,lect No 95-0121 <br /> g of 9 , <br /> no more than 20 feet and, there fore, selected S VE <br /> independent screened intervals wells may , <br /> Y be dual-completed with two (or mare) { <br /> 3 12 SYSTEM LOCATION AND DE - <br /> SIGN <br /> It is proposed that the <br /> Construction Com VES,unit will be !o }� <br /> Pany b6ildin located near the southeast carrier of th <br /> to install the system A g This location'will reduce the <br /> ` gated enclosure a amount af'trenchin e Nortte]Iiru <br /> Two-inch PVC i PProhimately I S by 20 feet, wi!! sec ge the iping needed <br /> _ VES tinct <br /> p Piping wiI! be insta!!ed from all VES v►, <br /> carrzr by dre�carbnn vapors <br /> ells to a <br /> r <br /> underground A P °rs from the VES well h ' VES dropout VC' bat! v cads to the VES unit pout drum The piping will <br /> well Inde a valve will be installed in each line so that al ars C <br /> P ndently A plan of the piping wall be installed <br /> depicted in Figure 6'-Pro prop ch pipingsystem A can be drawn from each <br /> posed Plje Piping Systeriry and enclosed VES unit location are <br /> 3 13 SLTPFlE1tMNTAL FUEL <br /> f <br /> SuPPleinental f[Iel is <br /> module adjusts for the optimalrequireelfor the o <br /> peratrnn of the selected <br /> Natural gas is reads! combustion parameters b VES tinct A n automatic air dilution <br /> that will be connected ulth he on-site Y adding oxygen an <br /> Representatives OFp,G & E or su <br /> monitor su VES unit will instal! a dedicated ptal,fuel <br /> PPlemental fuel cne <br /> onsuin within the Proposed enclosure <br /> ption A meter will be installedas to <br /> 1 4 tMONIToRING , <br /> The VES will be 9 <br /> destruction of recove�diored weekly using a photo-ionization <br /> be recorded from the hydrocarbon vapors, and to detector (per <br /> VES unit at the is, an nt monitor cleanup to ensure optimal <br /> destruction Optimal destruction as well as readingsp befa ss pID <br /> readings'wrll <br /> temperature, volume Ofpracessed va depend on four _ re and after catalytic <br /> Por, oxygen level Operational p parameters <br /> .A» samples and the lorver explosive limits3(/LEL)st1Qn< <br /> pies will be collected o� <br /> transported to a state certified laboratory basis ` <br /> x s , and diesel(TPII g and TP _ for analys s o f total 1es will be collected in Tedlar <br /> gasoline <br /> Xyle BTE&X d), arid-volatile aromatics(benzene hydrocarbons bags and <br /> correlating in accardancc with EPA , toluene, ethyl quantified <br /> as <br /> S PID readings and determining aPProved methods The analytical results b a and <br /> r S when to advance confirmation sol <br /> During the"'start-up- rII assist in <br /> P"period for the SVE s l borings <br /> Ystem, organic vapor monitoring will perform <br /> ed an at least ' <br /> j M y <br />