首页> 外文期刊>Water Environment Research >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
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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

机译:离子交换和电化学还原相结合的方法从饮用水中去除硝酸盐第一部分:使用重碳酸盐形式的选择性阴离子交换剂去除硝酸盐并重复利用再生液

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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~+Et_3) functional groups was used in the bicarbonate (HCO_3~-) and carbonate (CO_3~(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 HCO_3~- 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 (NaHCO_3) 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 percent. The volume of applied regenerant solution was high, but the consumption of NaHCO_3 for regeneration was low.
机译:研究了通过离子交换选择性去除饮用水中硝酸盐的过程。使用具有三乙铵(-N〜+ Et_3)官能团的商业强碱阴离子交换剂,以碳酸氢盐(HCO_3〜-)和碳酸盐(CO_3〜(2-))的形式使用。鉴于废旧再生溶液中硝酸盐的后续电化学还原,本研究的目的是优化离子交换剂的再生。研究了离子交换剂形式,再生溶液浓度以及再生溶液中硝酸盐,氯化物和硫酸盐的存在的影响。研究的HCO_3-型强碱阴离子交换剂能够处理270床体积的含124 mg dm〜(-3)硝酸盐的模型水溶液。为了使饱和阴离子交换剂充分再生,必须使用约30床体积的新鲜1-M碳酸氢钠(NaHCO_3)再生溶液。经过电解处理后,再生溶液中存在残留的50 mg dm〜(-3)硝酸盐,导致再生溶液剂量增加至35床体积,随后的吸附运行减少约13%。施加的再生溶液体积大,但再生所需的NaHCO_3消耗量低。

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