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离子交换与电化学还原相结合用于饮用水中硝酸盐的去除。第一部分:使用碳酸氢盐形式的选择性阴离子交换剂去除硝酸盐并回用再生剂溶液。

A combination of ion exchange and electrochemical reduction for nitrate removal from drinking water. Part I: nitrate removal using a selective anion exchanger in the bicarbonate form with reuse of the regenerant solution.

作者信息

Jelínek Ludek, Parschová Helena, Matejka Zdenek, Paidar Martin, Bouzek Karel

机构信息

Department of Power Engineering, Institute of Chemical Technology, Prague, Czech Republic.

出版信息

Water Environ Res. 2004 Nov-Dec;76(7):2686-90.

PMID:16042116
Abstract

The process of selective nitrate removal from drinking water by means of ion exchange was studied. A commercial strong base anion exchanger with triethylammonium (-N+Et3) functional groups was used in the bicarbonate (HCO3-) and carbonate (CO3(2-)) form. The aim of this study was to optimize ion-exchanger regeneration in view of the subsequent electrochemical reduction of nitrates in the spent regenerant solution. The effects of ion-exchanger form, concentration of regenerant solution, and presence of nitrates, chlorides, and sulphates in the regenerant solution were studied. The strong base anion exchanger in HCO3- form that was investigated was able to treat 270 bed volumes of model water solution containing 124 mg dm(-3) nitrates. To achieve adequate regeneration of the saturated anion exchanger, it is necessary to use approximately 30 bed volumes of fresh 1-M sodium bicarbonate (NaHCO3) regenerant solution. The presence of residual 50-mg dm(-3) nitrates in the regenerant solution, treated by electrolysis, resulted in an increase in the dose of regenerant solution to 35 bed volumes and a decrease in the subsequent sorption run of approximately 13%. The volume of applied regenerant solution was high, but the consumption of NaHCO3 for regeneration was low.

摘要

研究了通过离子交换从饮用水中选择性去除硝酸盐的过程。使用了具有三乙铵(-N⁺Et₃)官能团的市售强碱性阴离子交换剂,其呈碳酸氢根(HCO₃⁻)和碳酸根(CO₃²⁻)形式。本研究的目的是鉴于后续对废再生液中硝酸盐进行电化学还原,优化离子交换剂的再生过程。研究了离子交换剂形式、再生液浓度以及再生液中硝酸盐、氯化物和硫酸盐的存在对其的影响。所研究的呈HCO₃⁻形式的强碱性阴离子交换剂能够处理270床体积含有124 mg dm⁻³硝酸盐的模拟水溶液。为使饱和阴离子交换剂实现充分再生,需要使用约30床体积的新鲜1 M碳酸氢钠(NaHCO₃)再生液。经电解处理的再生液中残留50 mg dm⁻³硝酸盐,导致再生液剂量增加至35床体积,后续吸附运行量减少约13%。所施加的再生液体积较大,但用于再生的NaHCO₃消耗量较低。

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