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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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The arsenic loaded onto the column is:As loading = [(305,177)(0.375)(1/1000)](0.375)(1/1000)(750)(1000)As loading = 0.41 mg As/g AA {Table 2 <strong>of</strong> Phase 3 Report lists 0.43 mg As/g AA}B. Using the bed volume size <strong>of</strong> 16,032 liters, yields the following adsorptive capacities:As ads = (92,052 Fg*BV/L)(16,032 L/BV)(1 gram/10 6 Fg) = 1476 gramsAs tot = (98,040)(16,032)(1/10 6 ) = 1572 gramsIt appears that the adsorptive capacity <strong>of</strong> 1573 grams in the <strong>Arsenic</strong> Treatment EvaluationReport is based on total arsenic instead <strong>of</strong> the adsorbed arsenic.C. The maximum run length will be based on an adsorptive capacity <strong>of</strong> 1476 grams in the secondcolumn. For this step <strong>of</strong> the analysis, it will be assumed that all <strong>of</strong> the arsenic passing throughthe first column will be adsorbed by the second column. This is a very conservative estimatebecause the second column will also have leakage through it <strong>and</strong> concentrations will rise untilbreakthrough is reached at 2 Fg/L. This is balanced by the fact that when the polishing columnis moved into the roughing column position, some <strong>of</strong> its capacity will have already been usedwhen it was the polishing column. Both <strong>of</strong> these factors will be addressed later. The integralequation in step 2 is again utilized to estimate the amount <strong>of</strong> arsenic passing through the firstcolumn. When this value is equal to 1476 grams, then the maximum run length can bedetermined.For a run length <strong>of</strong> 18,500 BV:As pass = (2*10 -8 )/3*(18500) 3 + 0.0001*(18500) 2 + 0.8394*18500As pass = 1474 gramsD-16

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