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<br />] <br />] <br />] <br />J <br />] <br />J <br />] <br />] <br />] <br />] <br />] <br />] <br />'] <br />b <br /> <br />6. <br /> <br />7. <br /> <br />.r <br />J <br /> <br />'] <br />] <br />'] <br />IJ <br /> <br />. <br /> <br />. <br /> <br />deliver coal to the IPP project in western Utah <br />does not seem feasible unless the user of the <br />coal would pay for a considerable part of the <br />collection, storage, and pipeline system. Using <br />drainwater for tar sands development can remove <br />7 mg/l TDS at Imperial Dam at a cost of $627rOOO <br />per mg/l. It could be made particularly attrac- <br />tive if the user of the water would pay for the <br />O&M costs. However, there is considerable uncer- <br />tainty regarding the viability and timing of the <br />tar sands industry. The use of drainwa ter for <br />coal washing is not cost effective and there is <br />little salinity improvement, but if the user were <br />willing to bear part of the cost, it may be worth <br />considering further. <br /> <br />Selective Withdrawal and Treatment or Disposal. <br />None of the selective withdrawal options are cost <br />effective. Thus, unless a way can be found to <br />reduce cost, they are probably not worth con- <br />tinued evaluation. <br /> <br />Retire Farmland and Use the Fresh Water Saved for <br />Other Beneficial Use. The cost of all options <br />under this alternative is in the range of <br />$1,300,000 to $1,400,000 per mg/l. Whether these <br />options are viable is dependent on the extent of <br />cost sharing by industry. The salinity impact at <br />Imperial Dam would be &.6 mg/l for the tar sands <br />option. <br /> <br />UNRESOLVED ISSUES <br /> <br />During the development of <br />issues listed below could <br /> <br />the <br /> <br />Appraisal Level Design, the <br />be resolved because of lack <br /> <br />not <br /> <br />11-3 <br /> <br />'-; r""!'""- <br />lJUi.:;iiU <br />