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Technologies and Costs for Removal of Arsenic From Drinking Water

Technologies and Costs for Removal of Arsenic From Drinking Water

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systems could underestimate the need <strong>for</strong> roads <strong>and</strong> fences at some entry points. There<strong>for</strong>e,the 18% without treatment from the 1,001 - 3,300 category was applied to the four largersystem categories. The following table summarizes the percentage used <strong>for</strong> each <strong>of</strong> the sizecategories.Table D-3Assumed Percentage <strong>of</strong> Ground <strong>Water</strong> Systems with No TreatmentPopulation CategoryPercentage <strong>of</strong> GWS w/o any Treatment25 - 100 43%101 - 500 19%501 - 1,000 16%1,001 - 3,300 18%3,301 - 10,000 18%10,001 - 50,000 18%50,001 - 100,000 18%100,001 - 1 MIL 18%Thus, the cost <strong>of</strong> a road <strong>and</strong> fence was calculated <strong>and</strong> 43% <strong>of</strong> that total was included in the unitcost <strong>for</strong> activated alumina <strong>for</strong> systems serving between 25 <strong>and</strong> 100 people.13. The equation <strong>for</strong> process area, which is the key variable in estimating the costs <strong>for</strong> buildings,roads, <strong>and</strong> fences has been based on the design flow <strong>of</strong> the system. The equation used <strong>for</strong>process area is:Process Area = 726.6 * Design Flow + 59Basis. The basis <strong>for</strong> the cost equations <strong>for</strong> buildings, fence <strong>and</strong> road are described in Section4.0 <strong>of</strong> the Very Small Systems Document (10). The Very Small Systems Document providedcosts as a percentage <strong>of</strong> the capital costs <strong>for</strong> design flows from 0.024 to 0.65 mgd. Theprocess area was calculated from the building cost estimates by dividing by 40 (building costsD-8

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