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在离子交换软化中再利用盐水:盐排放、硬度泄漏和容量权衡。

Brine reuse in ion-exchange softening: salt discharge, hardness leakage, and capacity tradeoffs.

机构信息

Department of Chemical and Biomolecular Engineering, University of Nebraska, Lincoln, NE 68588-0531, USA.

出版信息

Water Environ Res. 2012 Jun;84(6):535-43. doi: 10.2175/106143012x13373550427354.

Abstract

Ion-exchange water softening results in the discharge of excess sodium chloride to the aquatic environment during the regeneration cycle. In order to reduce sodium chloride use and subsequent discharge from ion-exchange processes, either brine reclaim operations can be implemented or salt application during regeneration can be reduced. Both result in tradeoffs related to loss of bed volumes treated per cycle and increased hardness leakage. An experimentally validated model was used to compare concurrent water softening operations at various salt application quantities with and without the direct reuse of waste brine for treated tap water of typical midwestern water quality. Both approaches were able to reduce salt use and subsequent discharge. Reducing salt use and discharge by lowering the salt application rate during regeneration consequently increased hardness leakage and decreased treatment capacity. Single or two tank brine recycling systems are capable of reducing salt use and discharge without increasing hardness leakage, although treatment capacity is reduced.

摘要

离子交换水软化在再生循环期间会将过量的氯化钠排放到水生态环境中。为了减少离子交换过程中氯化钠的使用和随后的排放,可以实施盐水回收操作,或者减少再生过程中的盐用量。这两种方法都会导致每周期处理的床层体积损失和硬度泄漏增加的权衡。使用经过实验验证的模型比较了在不同盐用量下同时进行的水软化操作,同时考虑了直接再利用废水和未经处理的自来水(典型的中西部水质)。这两种方法都能够减少盐的使用和随后的排放。通过降低再生过程中的盐用量,减少盐的使用和排放会导致硬度泄漏增加,处理能力降低。单罐或双罐盐水回收系统能够在不增加硬度泄漏的情况下减少盐的使用和排放,尽管处理能力会降低。

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