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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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RegenerationRegeneration <strong>of</strong> AA beds is usually accomplished using a strong base solution, typicallyconcentrated NaOH. Relatively few BV <strong>of</strong> regenerant are needed. After regeneration with strongbase, the AA medium must be neutralized using strong acid; typically two percent sulfuric acid.<strong>Arsenic</strong> is more difficult to remove during regeneration than other ions such as fluoride (Clif<strong>for</strong>d <strong>and</strong>Lin, 1995). Because <strong>of</strong> this, slightly higher base concentrations are used; typically 4 percent NaOH.Even at this increased concentration , however, not all arsenic may be eluted. Clif<strong>for</strong>d <strong>and</strong> Lin (1986)found only 50 to 70 percent <strong>of</strong> arsenic was removed from the AA columns during regeneration. Otherresearchers have also documented the difficult regeneration <strong>of</strong> AA <strong>for</strong> arsenic. Regeneration testsconducted by Benjamin et al. (1998) indicated that exposure <strong>of</strong> the AA medium to 0.1 N NaCl or 0.2N NaOH did not regenerate the AA to a significant extent. <strong>Arsenic</strong> recovery was limited <strong>and</strong> in mostcases was less than 50 percent <strong>of</strong> the sorbed arsenic. Higher recoveries have been reported, however.Hathaway <strong>and</strong> Rubel (1987) found that 80 percent <strong>of</strong> the adsorbed arsenic was eluted using 1.0 to 1.25M NaOH solution. Simms <strong>and</strong> Azizian (1997) found that up to 85% <strong>of</strong> the capacity <strong>of</strong> an AA bedcould be recovered using NaOH.Regeneration also affects successive bed life <strong>and</strong> efficiency. Bed life is shortened <strong>and</strong>adsorption efficiency is decreased by regeneration. Benjamin et al. (1998) found that arsenicbreakthrough patterns from the AA columns using regenerated media were qualitatively similar tothose using fresh media, but the removal efficiency declined slightly after each <strong>of</strong> two regenerations.Clif<strong>for</strong>d (1986) demonstrated that regeneration has a clearly negative effect on the adsorptioncapacity <strong>of</strong> activated alumina. The unrecovered As(V) <strong>and</strong> changes in the AA surface induced by theregeneration process may cause the length <strong>of</strong> the adsorption runs to decrease by 10 to 15 percent aftereach regeneration.Field StudiesSeveral field studies have demonstrated that arsenic may be reduced to below 3 Fg/L usingactivated alumina filtration. For example, Stewart (1991) reports on the success <strong>of</strong> a small waterutility in treating <strong>for</strong> arsenic. This utility, which serves 89 households in Bow, New Hampshire,relies on 2 wells <strong>for</strong> its source water. Each <strong>of</strong> the wells is characterized by a high level <strong>of</strong> arseniccontamination (mean arsenic concentrations <strong>of</strong> 62 Fg/L <strong>and</strong> 57 Fg/L). However, the utility was ableto reduce arsenic levels below the current MCL <strong>of</strong> 50 Fg/L <strong>for</strong> 106 days while producing an average2-17

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