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)4NALCO <br /> NCPA Lodi <br /> Crystallizer Module <br /> CaCO3 <br /> Conduct Com, Combined Crystallizer Crystallizer Not Crystallizer Not <br /> Contaminant Units Co- Factors Evaporator Blowdown Influent Distillate Used 1 Used 2 <br /> Flow GPM 0.00 0.00 3.45 3.45 3.10 <br /> Alkalinity-Bicarbonate 0.72 0.82 1.40 1.40 0.00 <br /> Alkalinity-Carbonate m L 2.82 1.67 0.00 0.00 0.00 <br /> Alkalinit-P-BaC12 m91L 0.00 2.94 0.00 0.00 0.00 <br /> Barium m L 0.00 0.73 0.00 0.00 0.00 <br /> Chloride m9fL 2.14 1.41 19414.25 19414.25 2.91 <br /> Fluoride m L 1 0.00 2.63 1 0.00 0.00 0.00 <br /> Calcium m9fL 2.6 2.50 5868.94 5868.94 0.88 <br /> Magnesium m L 3.82 4.12 2170.06 2170.06 0.33 <br /> Ito m91L 0.00 2.69 2.24 2.24 0.00 <br /> Nitrate m L 1.15 0.81 9340.60 9340.60 1.40 <br /> H s.u. 0.00 0.00 6.00 6.00 7.00 <br /> Phosphate m L 0.00 1.58 100.69 100.69 1 0.02 <br /> Potassium m91L 1.84 1.28 3502.72 3502.72 0.53 <br /> Silica m L 0.00 0.83 1359.64 1359.64 0.20 <br /> Sodium 2.13 2.18 16820.92 20928.30 3.14 <br /> Sulfate m9/L 1.54 1.04 21082.03 21082.03 3.16 <br /> Total Dissolved Solids m L 79663.50 83770.88 12.57 0.00 0.00 <br /> Specific Conductance umhos/cm 150577.97 159326.69 23.90 0.00 0.00 <br /> Free CO2 m L 2.33 2.33 0.00 0.00 0.00 <br /> Total Cations mgfL CaCO3 64772.13 73726.22 11.06 0.00 0.00 <br /> Total Anions m LCaCO3 58154.04 58154.04 8.72 0.00 0.00 <br /> Total Hardness m L CaCO3 23613.00 23613.00 3.54 0.00 0 06 <br /> Crystallizer R covery Rate %of Influent 90.00% <br /> Crystallizer Ion Reject Rate %of Influent 99.99% <br /> Power Consumption MW/1000 Gal 0.20 <br /> Power Consumption MW-Hr/Day 0.99 <br /> Power Cost $/MW-Hr $35.00 <br /> Power Cost $/Day $34.75 <br /> Anti-Foam Feed ppm 0.50 <br /> Anti-Foam Cost $/Lb $2.50 <br /> Anti-Foam Cost $/Day $0.05 <br /> Caustic Feed Required? 1=Yes 1 <br /> Magnesium in Influent Moles/Min 1.1654 <br /> Magnesium in Effluent Moles/Min 0.0002 <br /> Magnesium Precipitated Moles/Min 1.1653 <br /> OH Precipitated Moles/Min 2.3305 <br /> Sodium Added m/L 4107.38 <br /> Caustic Feed Required m/L 7143.27 <br /> Caustic Feed Required Lb/Day 295.75 <br /> Caustic Cost $/Lb $0.15 <br /> Caustic Cost $/Day $44.36 <br /> Number of Crystallimrs 2 <br /> Capacity of Each Xtalizer % 50.00% <br /> Capacity of Each Xtalizer GPM 1.72 <br /> Xtal Equipment Cost $ $250,000 <br /> Structural Steel Cost $/Xtal $50,000 <br /> Xtal Structural Steel Cost $Total $100,000 <br /> Xtal Total Capital Cost $ $350,000 <br /> Required Storage Time Hrs 0.00 0.00 0.021 0.00 <br /> Required Storage Volume Gal 0 01 0 0 <br /> Required Storage Volume $Installed $0 $0 $0 $0 <br /> Total Dry Sludge Discharged Tons/Year 632.98 <br /> Sludge Solids % 70.00% <br /> Total Sludge Discharged Tons/Year 904.25 <br /> Bulk Density of Sludge Lbs/ftA3 55 <br /> Vol of Sludge Discharged FtA3/Year 32881.99 <br /> Sludge Disposal Cost1$/Wet Ton 1 $45.00 <br /> Sludge Disposal Cost1$/Day 1 $111.48 <br /> File:Copy of NCPA Lodi Water Balance Urne_MgO 15 COC Rev A 070708.xls Sheet:Crystallizer Page 1 of 1 Date:9/2/2008 <br />