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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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Domestic sewage means untreated sanitary wastes that pass through a sewage system. Dischargesmeeting the above criteria are excluded from regulation as hazardous waste.Although the brine stream may be deemed a hazardous waste, such characterization would not,in itself, prevent disposal to a POTW since wastes that passes through a sewer system to a POTW areexempt from RCRA regulation. Discharge to the sanitary sewer may be limited by TBLLs <strong>for</strong> arsenicor TDS. The TDS is the more likely limiting factor since the arsenic TBLL would need to berecalculated since the background arsenic will change. The only net increase in arsenic is related tothe water loss from the drinking water treatment plant to the POTW. TDS is different. TDS is beingadded to the waste stream. Due to the potential <strong>for</strong> an increase in total dissolved solids, anionexchange would be favored in areas other than the southwest where the volume <strong>of</strong> brine is very smallrelative to the total volume <strong>of</strong> wastewater being treated at the POTW.Although one small system was reported to have disposed <strong>of</strong> its waste brine to the facility’sseptic tank (EPA October 2000), such disposal is likely to be regulated by local <strong>and</strong> State regulations<strong>and</strong> there<strong>for</strong>e was not considered in the cost analysis <strong>for</strong> the final rule.4.4.8 Activated AluminaActivated alumina (AA) can be operated with or without pH optimization <strong>and</strong> regeneration.Systems optimizing pH <strong>and</strong> regenerating will produce a regenerant waste solution with a pH <strong>of</strong>approximately 12 <strong>and</strong> high in dissolved solids, aluminum, <strong>and</strong> arsenic (AWWARF, 1998).Regeneration <strong>of</strong> AA is accomplished using 15 to 25 bed volumes (BV) <strong>of</strong> 2N NaOH, 7 BV <strong>of</strong> rinse,<strong>and</strong> 15 BV <strong>of</strong> 2N H 2 SO 4 <strong>for</strong> neutralization (approximately 42 BV per regeneration cycle). <strong>Arsenic</strong>is strongly adsorbed to the media, so only about 50 - 70% <strong>of</strong> the adsorbed arsenic is removed evenusing a strong base.. The brine stream produced by the regeneration process then requires disposal.The November 1999 Technology <strong>and</strong> Cost Document listed discharge to a sanitary sewer as thedisposal mechanism <strong>for</strong> the brines. It was noted that TBLLs <strong>for</strong> arsenic might restrict discharge <strong>of</strong>brine streams to the sanitary sewer. Since activated alumina run lengths are much longer than anionexchange, the arsenic concentrations in the brine stream would likely be much higher even withincomplete regeneration. Regeneration <strong>of</strong> activated alumina media is not recommended even <strong>for</strong>larger systems because disposal <strong>of</strong> the brine may be difficult, the regeneration process is incompletewhich reduces subsequent run lengths, <strong>and</strong> <strong>for</strong> most systems it will be cheaper to replace the mediarather than regenerate it. As a result, regeneration <strong>of</strong> AA was not considered <strong>for</strong> the final rule.4-19

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