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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
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 (CO32−) form. The aim of this study was to optimize ion‐exchanger regeneration in view of the sub‐ sequent electrochemical reduction of nitrates in the spent regenerant so‐ lution. 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.
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
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 (CO32−) form. The aim of this study was to optimize ion‐exchanger regeneration in view of the sub‐ sequent electrochemical reduction of nitrates in the spent regenerant so‐ lution. 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.
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
Jelínek, Luděk (author) / Parschová, Helena (author) / Matějka, Zdeněk (author) / Paidar, Martin (author) / Bouzek, Karel (author)
Water Environment Research ; 76 ; 2686-2690
2004-11-01
5 pages
Article (Journal)
Electronic Resource
English
Nitrate Removal by Anion‐Exchange Resins
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