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首页> 外文期刊>Desalination: The International Journal on the Science and Technology of Desalting and Water Purification >Ion-exchange membrane processes for Br ~- and BrO3 ion removal from water and for recovery of salt from waste solution
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Ion-exchange membrane processes for Br ~- and BrO3 ion removal from water and for recovery of salt from waste solution

机译:离子交换膜工艺,用于从水中去除Br〜-和BrO3离子以及从废液中回收盐

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摘要

The applicability of Donnan dialysis with an anion-exchange membrane for bromide and bromate ion removal was studied. The rate of bromide, bromates and associated ion (HCO_3~- SO_4~(2-)) removal with the use of Selemion AMV and Neosepta ACS membranes at different salt concentrations in the receiver was analyzed. The process of anion exchange through the Neosepta ACS membrane allows effective bromides removal (90%), at a relatively low salt concentration in the receiving solution (100 mM NaCl). In order to achieve a similar effect of bromide removal by using the Selemion AMV membrane (91%) three times higher salt concentration in the receiver is required. Moreover, the potential of electrodialysis to recover NaCl from waste receiving solution after the Donnan dialysis and the usefulness of recovered solution to remove bromides and bromates was examinated. The best results of the process, i.e. required salt concentration in the concentrate (100 mM NaCl), and possible minimum contamination of the ballast ions (Br~- or BrO_3~- and HCO_3~- and SO_4~(2-)) were obtained at a current density of 50 A/m~2. Depending on a modification method of the recovered salt solution, it was obtained from 61 to 78% removal of bromides and from 79 to 86% removal of bromates.
机译:研究了用阴离子交换膜对Donnan透析进行溴化物和溴酸根离子去除的适用性。分析了在接收器中使用不同盐浓度的Selemion AMV和Neosepta ACS膜去除溴化物,溴酸盐和相关离子(HCO_3〜-SO_4〜(2-))的速率。通过Neosepta ACS膜进行阴离子交换的过程可以在接收溶液中相对较低的盐浓度(100 mM NaCl)中有效去除溴化物(90%)。为了通过使用Selemion AMV膜(91%)获得类似的溴化物去除效果,需要在接收器中将盐浓度提高三倍。此外,检验了Donnan透析后电渗析从废物接收溶液中回收NaCl的潜力,以及回收溶液去除溴化物和溴酸盐的有用性。该过程的最佳结果,即浓缩物中所需的盐浓度(100 mM NaCl)以及镇流离子(Br〜-或BrO_3〜-和HCO_3〜-和SO_4〜(2-))的可能最小污染得到了电流密度为50 A / m〜2。取决于回收的盐溶液的改性方法,从61至78%的溴化物去除和从79至86%的溴酸盐去除获得。

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