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首页> 外文期刊>Desalination: The International Journal on the Science and Technology of Desalting and Water Purification >Effect of hydroxyl and nitrate ions on the sorption of ammonium ions by sulphonic cation exchangers
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Effect of hydroxyl and nitrate ions on the sorption of ammonium ions by sulphonic cation exchangers

机译:羟基和硝酸根离子对磺酸阳离子交换剂吸附铵离子的影响

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摘要

The sorption of ammonium ions and ammonia by the H+ form of sulphonic acid cation exchangers Amberlite 252,Lewatit 2629 and Relite C 360 from a solution containing NH_4NO_3 in the range of 0 to 0.214 equ/L and NH_3 in the range of 0.353 to 0 equ/L was investigated to establish the possibility of their application for the recovery of ammonium from caustic condensate generated in nitrogen fertilizer production.Breakthrough and elution curves were obtained,determining the concentration of ammonium with Nessler's reagent.The sorption of ammonium and ammonia depends on the concentration ratio of ammonia to ammonium nitrate [NH_3]/[NH_4NO_3].On decreasing [NH_3]/[NH_4NO_3],the concentration ratio of hydroxyl to nitrate ions [OH"]/[NO_3] and the effluent pH prior to NH_4 breakthrough also decrease.This results in a decrease in the NH_4 sorption because of a deficiency in the neutralization of hydrogen ions released(ordinary cation-exchange process).Thus,adverse circumstances create an unfavorable medium for NH_4 removal from the caustic condensate.Maximum sorption of NHJ is attained at [NH_3]/[NH_4NO_3]-1.2.A further decrease in [NH_3]/[NH_4NO_3] is followed by a significant decrease in the effluent pH,which leads to an increase in the concentration of protonated sulphonic acid groups(-SO_3H),resulting in a decrease in the ion-exchange ability of the cation exchangers under investigation with respect to NH_4 removal.The concentration(g/L)of NH_4NO_3 in the eluate from the cation-exchanger regeneration,carried out using 0.7 bed volumes(B V)of 20% HNO_3,amounts to 136.7 for Relite C 360,119.5 for Lewatit K 2629 and 96.7 for Amberlite 252.The content of undamaged beads after 100 cycles(each cycle comprises saturation with caustic condensate,containing ammonia and ammonium,successive regeneration with 20% nitric acid and washing)is from 97 to 99.8%.Resistance to boiling in 20% HNO_3 solution is from 97 to 99.8%.These are applicable for the recovery of NH_4NO_3 from the caustic condensate in the nitrogen fertilizers production,preventing economic damage and environmental contamination from nitrogen compounds.
机译:H +形式的磺酸阳离子交换剂Amberlite 252,Lewatit 2629和Relite C 360从NH_4NO_3的范围为0到0.214 equ / L和NH_3的范围为0.353到0 eq的溶液吸附铵离子和氨对/ L进行了研究,以确定其可用于从氮肥生产中产生的苛性冷凝物中回收铵的可能性。获得了穿透和洗脱曲线,使用Nessler试剂确定铵的浓度。铵和氨的吸附取决于氨与硝酸铵的浓度比[NH_3] / [NH_4NO_3]。当降低[NH_3] / [NH_4NO_3]时,羟基与硝酸根离子的浓度比[OH“] / [NO_3]以及NH_4突破前的出水pH减少。这导致NH_4吸附的减少,这是由于中和释放的氢离子不足(常规阳离子交换过程)所致。能够从苛性冷凝物中去除NH_4的介质。在[NH_3] / [NH_4NO_3] -1.2处获得最大的NHJ吸附。[NH_3] / [NH_4NO_3]进一步降低后,出水pH值显着降低,导致质子化磺酸基团(-SO_3H)的浓度增加,导致所研究的阳离子交换剂相对于NH_4去除的离子交换能力降低.NH_4NO_3在溶液中的浓度(g / L)阳离子交换再生液,使用0.7床体积(BV)的20%HNO_3进行洗脱,对于Relite C 360为136.7,对于Lewatit K 2629为119.5,对于Amberlite 252为96.7.100个循环(每个循环)后未损坏的珠含量含苛性冷凝物饱和,含氨和铵,用20%硝酸连续再生并洗涤)的比率为97-99.8%。在20%HNO_3溶液中的沸腾阻力为97-99.8%。这些可用于回收NH_4NO_3来自苛性碱氮肥生产中的冷凝水,可防止经济损失和氮化合物对环境的污染。

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