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Technologies and Costs for Removal of Arsenic From Drinking Water

Technologies and Costs for Removal of Arsenic From Drinking Water

Technologies and Costs for Removal of Arsenic From Drinking Water

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two technologies. Redundancy <strong>for</strong> the lower cost components would be covered by the conservativeassumptions used in deriving the capital costs.Recommended St<strong>and</strong>ards <strong>for</strong> <strong>Water</strong> Works (Great Lakes Upper Mississippi River Board <strong>of</strong>State Public Health <strong>and</strong> Environmental Managers, 1997), <strong>of</strong>ten referred to as the Ten State St<strong>and</strong>ards,presents a comprehensive discussion <strong>of</strong> redundancy <strong>and</strong> recommended redundant items <strong>for</strong> watertreatment facilities in those States. Systems may incur additional costs if additional redundant itemsare required by the State.3.4 COSTS FOR MULTIPLE REMOVAL PERCENTAGESCapital <strong>and</strong> O&M cost estimates are presented <strong>for</strong> the maximum achievable removal in thisdocument. Table 3-12 presents a removal technology matrix which identifies maximum removalpercentages <strong>for</strong> the technologies <strong>for</strong> which costs have been estimated. <strong>Costs</strong> <strong>for</strong> facilities requiringless than the maximum removal to meet the arsenic MCL target, can be estimated using the blendingapproach discussed in Section 3.4.2.3.4.1 <strong>Removal</strong> <strong>and</strong> Accessory <strong>Costs</strong>Both the April 1999 <strong>and</strong> the November 1999 drafts <strong>of</strong> the Technology <strong>and</strong> Cost Documentincluded costs <strong>for</strong> accessories in Appendix D. Accessory costs included raw <strong>and</strong> finished waterpumping, <strong>and</strong> clearwell storage. <strong>Removal</strong> costs include any process item directly associated with theremoval <strong>of</strong> a particular contaminant, e.g., the ion exchange bed in ion exchange processes. Inclusion<strong>of</strong> accessory costs was not based on a recommendation <strong>of</strong> the Technical Design Panel. A detailedexamination <strong>of</strong> Section 3.11 <strong>of</strong> the November 1999 Technology <strong>and</strong> Cost Document revealed theapparent source <strong>of</strong> the accessory costs. Section 3.11 compared the costs in the November 1999Technology <strong>and</strong> Cost Document with the costs from the 1993 Technology <strong>and</strong> Cost Document(Malcolm Pirnie, 1993a) <strong>and</strong> Evaluation <strong>of</strong> Central Treatment Options as Small System Compliance<strong>Technologies</strong> (SAIC, 1999). There is a statement in bold at the end <strong>of</strong> Section 3.11.1 that states thatthe 1993 estimates are greater than the 1999 estimates <strong>for</strong> many technologies. It further states that thisis because the 1993 estimates included accessory costs; i.e., raw <strong>and</strong> finished water pumping <strong>and</strong>clearwell storage.3-16

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