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<br />TABLE <br /> <br />I I 1-1 <br /> <br />111-2 <br /> <br />111-3 <br />I V-1 <br /> <br />100 <br /> <br />L 1ST OF TAStES <br /> <br />OEseR IPT I ON <br /> <br />Green River Ra w Water Qua I I ty <br /> <br />. . <br /> <br />. e, ._ " . <br /> <br />Stat Istl.ca I Analysis of B.I:g Sandy Seep and <br />Observai" fon We II Chem I str I es <br /> <br />. . <br /> <br />. . <br /> <br />Big Sandy Study Chemistries. . . . . . . . . <br /> <br />. <br /> <br />OptIon I Process Flow and Material Balance <br /> <br />. . <br /> <br />IV-2 Option II Process Flow and Material Balance - 7,500 gpm <br /> <br /> <br />IV-3 OptIon II Process Flow and MaterIal Balance - 5,000 gpm <br /> <br />IV-4 <br /> <br />IV-6 <br /> <br />IV-5 OptIon III Process Flow and Material Balance - 7,500 gpm <br /> <br />Option II Process Flow and Material Balance.. 2,500 gpm <br /> <br />IV-7 <br /> <br />IV-8 <br />IV-9 <br />IV-IO <br />V-1 <br />V-2 <br /> <br />V-3 <br /> <br />V-4 <br /> <br />V-5 <br />V-6 <br /> <br />V 1-1 <br />VI-2 <br /> <br />VI-3 <br /> <br /> <br />OptIon III Process Flow and MaterIal Balance - 5,000 gpm <br /> <br /> <br />OptIon III Process Flow and MaterIal Balance - 2,500 gpm <br /> <br /> <br />Option IV Process Flow and MaterIal Balance - 2,500 gpm <br /> <br />Process Summary . <br /> <br />'0 -. <br /> <br />. . . . . <br /> <br />. . <br /> <br />. . . . '0 . . . . <br /> <br />Option Equipment CapacItIes and Pond SIze Summary <br />Option Equipment and InstaHatlon Summary . <br />Base Case EconomIc ComparIson - 7,500 gpm . . . <br />Base Case. Economic Comparison - 5,000 gpm <br />Base Case Economic ComparIson - 2,500 gpm <br /> <br />. . . . <br /> <br />.. . <br /> <br />II. . . . <br /> <br />. . . ... . <br /> <br />. e. II. .. . <br /> <br />Option I-IV Levellzed Cost Summary <br /> <br />. . . <br /> <br />. <br /> <br />Results of SensItIvIty AnalysIs for Options III & IV <br /> <br /> <br />Base Case Level Ized Incremental Costs for OptIons III & IV <br /> <br /> <br />Levellzed Cost Per Ton Per Year of Salt Removed. <br /> <br />. . <br /> <br />Comparison of Cooling Tower Blowdown ChemIstries for FGD <br />DesIgn SpecifIcatIons and BIg Sandy Process OptIons <br /> <br />PAGE <br /> <br /> <br />. . <br /> <br />6 <br />a <br /> <br /> <br />. '. <br /> <br />'. <br /> <br /> 9 <br /> 14 <br /> . 17 <br /> . 20 <br /> 22 <br />. . 24 <br /> 26. <br />. 29 <br /> ..31 <br /> 33 <br />. . 34> <br /> 3Q <br />. . 36 <br /> <br />/. <br />k <br />1 <br />; <br /> <br />. <br /> <br />. . <br /> <br />.. <br /> <br />i <br />. ~ <br />t <br />~ <br />w <br />" <br />& <br />, <br />[ <br />~ <br />, <br />ii: <br />,~' <br /> <br />. <br /> <br />t, <br />J. <br /> <br />'" <br />, <br /> <br />. <br /> <br />38 <br />40 <br />42 <br />44 <br /> <br />. <br /> <br />. . <br /> <br />. . <br /> <br />45 <br /> <br />. . <br /> <br />45 <br /> <br />. <br /> <br />. <br /> <br />46 <br /> <br />. <br /> <br />ii <br /> <br />003107 <br /> <br />t: <br />