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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 use <strong>of</strong> evaporation ponds <strong>and</strong> drying beds involve the discharge <strong>of</strong> brine waste to a pond<strong>for</strong> storage <strong>and</strong> dewatering via the natural process <strong>of</strong> evaporation. Typically, such ponds are designedto have large surface areas to maximize evaporation <strong>of</strong> residual water by the sun <strong>and</strong> wind. Pond sizeis determined by waste flow <strong>and</strong> storage capacity requirements.As previously mentioned, evaporation ponds <strong>and</strong> drying beds are used primarily <strong>for</strong> brinewastes generated by RO <strong>and</strong> IX. Such processes produce large volumes <strong>of</strong> liquid wastescharacterized by high levels <strong>of</strong> total dissolved solids (TDS), <strong>for</strong> which mechanical dewateringprocesses, such as filter presses, are impractical. Depending on the solids concentration <strong>of</strong> the brinewaste stream, intermittent removal <strong>of</strong> solids may be required. For brines with a TDS content rangingfrom 15,000 to 35,000 mg/L, solids will accumulate in an evaporation pond at a rate <strong>of</strong> ½ to 1½inches per year (DPRA, 1993a). When the depth <strong>of</strong> the solids in the pond reaches a predeterminedlevel, discharge to the pond is halted <strong>and</strong> evaporation is allowed to continue until the solidsconcentration <strong>of</strong> the waste is suitable <strong>for</strong> disposal.The use <strong>of</strong> evaporation ponds is extremely l<strong>and</strong> intensive, requiring shallow basins with largesurface areas. This can be an important consideration in densely populated regions. Reverse osmosisprocesses produce very large volumes <strong>of</strong> liquid wastes which increases l<strong>and</strong> requirements <strong>and</strong>ultimately construction costs. As a result, evaporation ponds may not be suitable <strong>for</strong> large watersystems utilizing RO. Evaporation ponds <strong>and</strong> drying beds have few O&M requirements, but are onlyfeasible in regions with favorable climatic conditions, i.e., high temperatures, low humidity, <strong>and</strong> lowprecipitation (DPRA, 1993a). Waste streams with low TDS concentrations can be discharged to thesame pond <strong>for</strong> several years (assuming adequate total capacity) be<strong>for</strong>e solids accumulation warrantsremoval.4.2.4 Storage LagoonsLagoons are the most common, <strong>and</strong> <strong>of</strong>ten least expensive, method to thicken or dewatertreatment sludges. However, lagoons, like evaporation ponds, are l<strong>and</strong> intensive (DPRA, 1993a).Storage lagoons are lined ponds designed to collect, retain, <strong>and</strong> dewater sludge <strong>for</strong> a predeterminedperiod <strong>of</strong> time. Dewatering occurs through the evaporation <strong>and</strong> decanting <strong>of</strong> the supernatant. Lagoonsize is determined based on the volume <strong>of</strong> sludge that must be h<strong>and</strong>led <strong>and</strong> the desired storage time.As with evaporation ponds, when a lagoon reaches its design capacity, solids can be removed bymeans <strong>of</strong> heavy equipment <strong>and</strong> shipped <strong>for</strong> disposal.4-4

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