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QU1k stop <br /> CCI Pro ect Ia 12i Cl°$tee <br /> Page 10 N° 12 l l S Report <br /> degrade the volatile <br /> methods compaun ds The follawin <br /> Review of 'anular Act g 1s a brxefexplanation pf the various remediation <br /> Activated carbon ads <br /> Although adsa °rptian is a widel <br /> cost effective rPtzon technology Y used technology <br /> and technic.]l gY is not 144 perce gY zn remedlatln <br /> Y feasible for this Percent effective g impacted <br /> Treatment b site zn treating MTBE srelat er <br /> cant Y granular activated c , 1t IS relatively <br /> discharging the°M the subsurface barbon (GAC) <br /> aced pum 1n renes On the rein <br /> water, 1t lacks naturae sorption <br /> to p g ground peal of t <br /> the site floe SanitarY sew water prior to he dissolvod <br /> extendlnlarge volumes ption to soil particles er $ecause MT trea ent above <br /> g the current Ofgroundwater c Due to the r BE is extremel ground a.tid <br /> feet), groundw Onsite extract ion ' anul oat Y soluble rn <br /> easily be extracted for <br /> atn extraction well to the ure of the Saturated <br /> (GPS) Based on � average rates could be bottom Of A�ove-ground tie sail at <br /> Pump rate of to erage MTBE co maintained Rnifer atrnent lg <br /> 1n-line I,OOp_ 3 GpA4, CCI esti ncentrafzon neof 3 at two to three (aPproximately 44 Y <br /> pound G mates carbon 4,044 microgragmslpnspei minute <br /> would be required *9C canisters image rates <br /> approximately a replacing the s of 2p to .per liter(u <br /> ately every 25 days petit carbon in one f Pounds per da�LUs1n�� <br /> Review flual-Phase vapor Extr <br /> action ee canisters <br /> Ifa permanent Dual Phase ;,a <br /> su mPound, with a 6th por Extraction <br /> pPIY the poker gh chain link fent Ystern 11'as installed <br /> consist of a Catal needed to fl <br /> Ytzc Gxidrzerperate the e and a single phase <br /> A (CAT QXYsteiri and grO�dwa 24Q-voltt elecdtrtc�i ire a 12�x l2' <br /> Z inch di ) Ystezn groundwater The S r line, which would <br /> TI�e manifold diameter puC sole and w°ued operate r 3 stern z;, <br /> would be gas rnanlfold n the folio <br /> wrn oued <br /> caflection pods complete would be installed g manner <br /> The inn ' with <br /> B°w gauges, thio inside the <br /> separator tonic nt gas mixture throttling treatment <br /> treatment system Liquid that collected Would pass g valvesand cOmpowid <br /> sanzt (three 1n_ through the inan, d flua vt s <br /> Y sewer The so <br /> v fine, 1,QQO�po tank would auto ample <br /> vacuum opals wouldund carbon beds maticallY be transfer apor liquid <br /> Technology S Powered by a 5 then pass t )for processing ned to the <br /> ski-mounted hp el"ectne motor dough an MD pne g and disposal to the a vacua of 1p0 stand , model A?M umatics,Made! 3245 <br /> OX, the soil d cubic per lop scfm CAT muf. Brand into a 1 <br /> a temperature would be Preheated <br /> reheat dtw minute{scfrn �X This ng Buck <br /> at 6-r unit is capable of <br /> enter a two_sta PProxz with electric 1iChcs of generating <br /> mately 500 de strip heaters rner�cury Inside the <br /> ge, honeycpmb catalyst, where a reenheit(F), The hea effluent Beat exch C`� ' <br /> action Would occur causing g the d.soll gas ould then ger to <br /> controlled <br />