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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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Vickers et al. (1997) reported that micr<strong>of</strong>iltration exhibited excellent arsenic removalcapability. This report is corroborated by pilot studies conducted by Clif<strong>for</strong>d (1997), which foundthat coagulation assisted micr<strong>of</strong>iltration could reduce arsenic levels below 2 Fg/L in waters with apH <strong>of</strong> between 6 <strong>and</strong> 7, even when the influent concentration <strong>of</strong> Fe(III) is approximately 2.5 mg/L.These studies also found that the same level <strong>of</strong> arsenic removal could be achieved by this treatmentprocess even if source water sulfate <strong>and</strong> silica levels were high. Further, coagulation assistedmicr<strong>of</strong>iltration can reduce arsenic levels to an even greater extent at a slightly lower pH (approximately5.5).Addition <strong>of</strong> a coagulant did not significantly affect the membrane cleaning interval, althoughthe solids level to the membrane system increased substantially. With an iron <strong>and</strong> manganese removalsystem, it is critical that all <strong>of</strong> the iron <strong>and</strong> manganese be fully oxidized be<strong>for</strong>e they reach themembrane to prevent fouling (Muilenberg, 1997).2.2.4 Enhanced CoagulationThe Disinfectant/Disinfection Byproduct (D/DBP) Rule requires the use <strong>of</strong> enhancedcoagulation treatment <strong>for</strong> the reduction <strong>of</strong> disinfection byproduct (DBP) precursors <strong>for</strong> surface watersystems which have sedimentation capabilities. The enhanced process involves modifications to theexisting coagulation process such as increasing the coagulant dosage, reducing the pH, or both.Cheng et al. (1994) conducted bench, pilot, <strong>and</strong> demonstration scale studies to examine As(V)removals during enhanced coagulation. The enhanced coagulation conditions in these studies includedincrease <strong>of</strong> alum <strong>and</strong> ferric chloride coagulant dosage from 10 to 30 mg/L, decrease <strong>of</strong> pH from 7 to5.5, or both. Results from these studies indicated the following:# Greater than 90 percent As(V) removal can be achieved under enhanced coagulationconditions. As(V) removals greater than 90 percent were easily attained under all conditionswhen ferric chloride was used.# Enhanced coagulation using ferric salts is more effective <strong>for</strong> arsenic removal than enhancedcoagulation using alum. With an influent arsenic concentration <strong>of</strong> 5 µg/L, ferric chlorideachieved 96 percent As(V) removal with a dosage <strong>of</strong> 10 mg/L <strong>and</strong> no acid addition. Whenalum was used, 90 percent As(V) removal could not be achieved without reducing the pH.# Lowering pH during enhanced coagulation improved arsenic removal by alum coagulation.With ferric coagulation pH does not have a significant effect between 5.5 <strong>and</strong> 7.0.2-9

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