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i <br /> SODIUM HYPOCHLORITE CONVERSION <br /> 1 <br /> Facility Process Component <br /> DisinfectionlOutfall <br /> i <br /> $4,713,000 <br /> Total Cost <br /> i <br /> PRIOR <br /> Costs ~ EXPEND- 2005-06 2006-07 2007-08* 2008-09 2009-10 'TOTAL <br /> ITURES <br /> Construction 4,713 000 4 713,000 <br /> TOTAL 0 0 0 4 713 000 0 0 4 713 000 <br /> FUNDING SOURCE <br /> Capital Reserve 4 713 000 4,713,000 <br /> TOTAL 0 0 0 4,713,000 0 0 4,713,000 <br /> * Inflated from 2004 by 6.3% to FY05-06 dollars (Engineering News Record factor) and 4% thereafter <br /> i <br /> PROJECT: Sodium Hypochlorite Conversion <br /> DESCRIPTION: Convert existing chlorine gas system to sodium hypochlorite for the base flow. Retain the <br /> existing chlorine contact basins. Install system with capability for high rate disinfection of <br /> PE diversion assuming high dosages of chlorine into a 72-inch pipe and small chlorine <br /> contact basin. <br /> JUSTIFICATION: Liquid sodium hypochlorite and sodium bisulfate system will replace the existing chlorine <br /> sulfur dioxide gas systems and increase the disinfection capacity from 175 mgd to 277 <br /> mgd. <br /> PROJECT DRIVER: Operator and community safety issues. <br /> PROJECT TRIGGER: Phasing with other related projects. <br /> TYPE OF PROJECT: 50% Capacity; 50% Performance <br /> ESTIMATED PROJECT COST $4,100,000 s <br /> (FY 2004-05 Dollars): - <br /> INFLATED PROJECT COST $4,713,000 <br /> (FY 2007-08 Dollars): j <br /> i. <br /> j PHASING: Budgeted for FY 2007/08 <br /> i <br /> <br /> . 1. <br /> Page 73 FY OS-06 BUDGET AND CTP ' <br /> <br />