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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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3.7 ADSORPTION PROCESSES3.7.1 Activated AluminaActivated alumina (AA) is a physical/chemical process by which ions in the feed water aresorbed to the oxidized AA surface. Feed water is continuously passed through the bed to removecontaminants. The contaminant ions are exchanged with the surface hydroxides on the alumina.Disposable activated alumina (no regeneration) costs were developed using the following approach.Four sets <strong>of</strong> costs were developed - two <strong>for</strong> unadjusted pH <strong>and</strong> two where the pH has been adjustedto the optimal pH <strong>of</strong> 6. The costs <strong>for</strong> pH adjustment to optimal pH 6.0 are included as a separatemodule in these cost estimates since it is only used <strong>for</strong> two <strong>of</strong> the options.The three models routinely used to estimate unit costs are all based on regeneration <strong>of</strong> themedia, operation at optimal pH, <strong>and</strong> use <strong>of</strong> single columns. Most <strong>of</strong> the costs are based on fluorideremoval rather than arsenic removal. It was determined that the existing cost models could not be usedto estimate costs <strong>for</strong> disposable activated alumina. To estimate costs, it was assumed that the aluminawould be arrayed in small columns operated in series rather than in one larger column. This willprovide greater utilization <strong>of</strong> the media be<strong>for</strong>e disposal <strong>and</strong> is more consistent with the other designsusing disposable activated alumina.Design Assumptions: Capital <strong>Costs</strong> with Natural pHThe following assumptions were made to estimate the capital cost <strong>of</strong> activated alumina whenthe water is not adjusted <strong>for</strong> pH. The basis <strong>for</strong> these assumptions are provided in Appendix D.1. The pH will not be adjusted to operate the process at the optimal pH between 5.5 <strong>and</strong> 6.0.The activated alumina process will be operated at the natural pH <strong>of</strong> the system to simplify theprocess <strong>and</strong> avoid potential problems with lowering the pH. Two pH ranges will beevaluated 7.0 #pH < pH 8.0 <strong>and</strong> 8.0 # pH #8.3.2. The pH will not need to be adjusted after the activated alumina process. The activatedalumina process should not adversely affect the finished water pH. Those systems with highnatural water pH will not need a new pH adjustment process. Those systems with lowernatural water pH values will continue to rely on the existing corrosion control process.3-36

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