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'Synergistic use of ion exchange and RO technologies in multicontaminant removal applications in drinking water'

机译:“在饮用水中多污染物去除应用中协同使用离子交换和反渗透技术”

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Some drinking water sources have a number of contaminants such as nitrate, sulfate,hardness and total organic carbon (TOC) that need to be reduced either to comply withmaximum contaminant level (MCL) regulations, to meet secondary guidelines, or tocontrol disinfection byproducts on subsequent disinfection of the water. Individualreduction of each contaminant by ion exchange is technically possible but the overallcost is becoming prohibitive, especially for regions where disposal of high concentrationspent brine is regulated. RO technology, because of its broad‐based salt rejectioncapability is an attractive alternative for simultaneous removal of such contaminants,but the challenge of disposing of relatively large volumes of concentrate (typically 25 to30 percent of total) has significantly limited its use. If concentrate volumes can bereduced to more manageable volumes, say 5 to 10% of total or lower, then disposal viadeep well injection and evaporation ponds becomes increasingly attractive. In addition,regions served by rapidly depleting aquifers can conserve more on scarce supplies.Synergistic use of ion exchange and RO technologies has the potential to reduceconcentrate volumes to less than 5 to 10 percent when use is made of a relatively newtechnology called cyclic ion exchange. Ion exchange softening of the RO feed allowshigher recovery rates by minimizing the potential for scaling of the RO membranes. Thehigher recovery rate results in higher brine concentrations in the RO reject, and this isturn is used in the cyclic ion exchange process to periodically regenerate the softeners.Recent advances in the technology now allows regeneration with brine concentrationsas low as 0.2% (2000 mg/l), allowing extended application of the technology to feedwaters with total dissolved solids (TDS) typical of that for drinking water. This paperexamines the technical and economic feasibility of the technology for treating drinkingwater with multiple contaminants, such as hardness, nitrate, sulfate, fluoride and TOC.
机译:一些饮用水源含有许多污染物,例如硝酸盐,硫酸盐, 需要降低硬度和总有机碳(TOC)以符合 最高污染物水平(MCL)法规,以满足二级准则,或 在随后对水进行消毒时,控制消毒副产物。个人 通过离子交换减少每种污染物在技术上是可行的,但总的来说 成本变得令人望而却步,特别是对于那些高浓度处置的地区 废盐水受到监管。反渗透技术,因为它具有广泛的除盐能力 功能是同时去除此类污染物的极具吸引力的替代方案, 但面临的挑战是处理相对大量的精矿(通常为25至 占总数的30%)已大大限制了其使用。如果精矿量可以 减少到更易于管理的数量,例如总量的5%到10%或更低,然后通过 深井注水和蒸发池变得越来越有吸引力。此外, 含水层迅速枯竭的地区可以节省更多的稀缺水源。 协同使用离子交换和反渗透技术有可能减少 使用相对较新的产品时,将浓缩量降低到不足5%到10% 该技术称为循环离子交换。反渗透进料的离子交换软化允许 通过最大程度地减少反渗透膜结垢的可能性,提高回收率。这 较高的回收率会导致反渗透废品中的盐水浓度更高,这是 循环离子交换过程中使用了有机硅来定期再生软化剂。 该技术的最新进展现在允许在浓盐水中进行再生 低至0.2%(2000 mg / l),可延长该技术在饲料中的应用 具有饮用水中典型的总溶解固体(TDS)的水。这篇报告 检验该技术用于治疗饮酒的技术和经济可行性 具有多种污染物(例如硬度,硝酸盐,硫酸盐,氟化物和TOC)的水。

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