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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 most significant weakness <strong>of</strong> this technology appears to be its cost. Currently, GFH mediacosts approximately $4,000 per ton. However, if a GFH bed can be used several times longer thanan alumina bed, <strong>for</strong> example, it may prove to be the more cost effective technology. Indeed, the systempr<strong>of</strong>iled in the field study presented above tested AA as well as GFH <strong>and</strong> found that GFH wassufficiently more efficient that smaller adsorption vessels <strong>and</strong> less media could be used to achieve thesame level <strong>of</strong> arsenic removal (reducing costs). In addition, unlike AA, GFH does not require preoxidation.A treatment <strong>for</strong> leaching arsenic from the media to enable regeneration <strong>of</strong> GFH seems feasible,but it results in the generation <strong>of</strong> an alkaline solution with high levels <strong>of</strong> arsenate which requiresfurther treatment to obtain a solid waste. Thus, direct disposal <strong>of</strong> spent GFH should be favored.2.6.4 Iron FilingsIron filings <strong>and</strong> s<strong>and</strong> may be used to reduce inorganic arsenic species to iron co-precipitates,mixed precipitates <strong>and</strong>, in conjunction with sulfates, to arsenopyrites. This type <strong>of</strong> process isessentially a filter technology, much like greens<strong>and</strong> filtration, wherein the source water is filteredthrough a bed <strong>of</strong> s<strong>and</strong> <strong>and</strong> iron filings. Unlike some technologies, ion exchange <strong>for</strong> example, sulfateis actually introduced in this process to encourage arsenopyrite precipitation.This arsenic removal method was originally developed as a batch arsenic remediationtechnology. It appears to be quite effective in this use. Bench-scale tests indicate an average removalefficiency <strong>of</strong> 81% with much higher removals at lower influent concentrations. This method wastested to arsenic levels <strong>of</strong> 20,000 ppb, <strong>and</strong> at 2000 ppb consistently reduced arsenic levels to less than50 ppb (the current MCL). While it is quite effective in this capacity, its use as a drinking watertreatment technology appears to be limited. In batch tests a residence time <strong>of</strong> approximately sevendays was required to reach the desired arsenic removal. In flowing conditions, even though removalsaveraged 81% <strong>and</strong> reached greater than 95% at 2000 ppb arsenic, there is no indication that thistechnology can reduce arsenic levels below approximately 25 ppb, <strong>and</strong> there are no data to indicatehow the technology per<strong>for</strong>ms at normal source water arsenic levels. This technology needs to befurther evaluated be<strong>for</strong>e it can be recommended as an approved arsenic removal technology <strong>for</strong>drinking water.2-47

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