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s <br /> Evaluation continued from pages Cost: The present-worth cost would treat contaminants only if <br /> of this alternative is estimated at they arrive in concentrations above <br /> most effective way to treat them is $103 million. Present-worth costs drinking water standards at drink- <br /> at several different surface facilities are a way to compare costs of pro- ing water wells that are in use. The <br /> on the LLNL site.The treatment jects that extend over different actual treatment technology would <br /> technology for each location is time periods. be decided at the time the treatment <br /> designed to treat a slightly different GW Altemative No.2 is needed. In the meantime,moni- <br /> combination of compounds. toring and a public awareness pro- <br /> The main difference between this gram to limit new well drilling <br /> Seven treatment system locations alternative and Alternative No.1 is would be used to prevent human <br /> (called A to G—see Figure 2)are the number and placement of the contact with contaminated ground <br /> described in the PRAP. They were extraction wells. Ground water water. <br /> selected to minimize the length of would be extracted at approximately <br /> piping required from the extraction 10 locations,primarily at the west- Estimated Cleanup Time: It is <br /> wells to the treatment facilities and ern and southern edges of the con- likely to take over 200 years,if ever, <br /> to provide efficient discharge routes taminated water,to stop further for contaminants from LLNL to <br /> for treated ground water. migration. The water would be reach currently used water wells in <br /> Facilities A,B,C,E,and G are treated at four treatment facilities downtown Livermore in concentra- <br /> near areas where only VOCs need on-site. Facilities A,B,and F would tions above drinking water stan- <br /> treatment. Facility D is near use UV light/oxidation. Air strip- dards. It is estimated to take about <br /> in would be used at Facility C. 30 years to reduce the concentra- <br /> ground water that contains both ping tq tions to below drinking water stan- <br /> VOCs and chromium. Treatment Following treatment,the water g <br /> would be returned to the subsurface dards using air stripping after <br /> Facility F is near ground water that If left untreatedg�ins. <br /> contains VOCs,FHCs,and lead or used at LLNL. treatment be , <br /> above cleanupstandards. studies show that natural processes <br /> Estimated Cleanup Time: It will would reduce the VOC concentra- <br /> GW Alternative No.l (The Pre- probably take more than 90 years to tions everywhere to below drinking <br /> ferred Alternative) reduce all contaminant concentra- water standards in about 300 years <br /> This alternative involves tions to levels below drinking water from now. <br /> round water at 18 initial standards under this alternative. <br /> pumping g Cost: The present-worth cost of <br /> locations for treatment at seven Cost: The present-worth cost of this alternative is between$12 millon <br /> treatment facilities. Four facilities this alternative is about$99 million. (monitoring only)and$87 million <br /> (A,B,E,and F)would use UV/ GW AltNo.3 (monitoring and cleanup,assuming <br /> oxidation as the primary treatment the use of air stripping technology). <br /> process. Air stripping would be This is a "delayed action'altema- <br /> used at Facilities C,D,and G,due live. Under this alternative,LLNL <br /> to the presence of compounds such <br /> as chloroform,carbon tetrachloride <br /> and Freon 113,which are less effec- <br /> . <br /> '. <br /> lively treated by UV/oxidation. At �e ,� r <br /> all facilities,exhaust air would be aa°,.,n.m.mr.ex — <br /> filtered through activated carbon ®r«..b•� .,,..,. --___ ..,,„„nem awa <br /> prior to release to the atmosphere to .�« ccNc <br /> remove contaminants. The treated •^••��. _ � o__ o� <br /> water would be returned to the sub- c� <br /> surface or used at the LLNL site. y°°^A, <br /> The extraction systems will be r rg e <br /> designed to prevent concentrations l l`� f �] 17 c <br /> of tritium above Federal and State <br /> drinking water standards from 1 Jf ! •� 'p - '>__ "!�`l <br /> entering the treatment facilities. rr`9+�\ '"°j` p ��a• oo'°' °•" .y I <br /> – rout <br /> This alternative results in the r • ^• o i aw°I <br /> complete removal of the contami- �; , r <br /> nated water and the most rapid "� ��' ` o` ' ":''•' e <br /> practical remediation of contami- <br /> nants in the ground water. / y <br /> �Bnln(lwa wlM <br /> Estimated Cleanup Time:Under <br /> this alternative,currently it is estimat- <br /> ed to take about 50 years to reduce all <br /> contaminant concentrations in the Figure 2. Preliminary ground water extraction and treatment facility locations with shaded areas <br /> affected ground water to levels below showing where VOCs are above drinking water standards in ground water. <br /> drinking water standards. <br />