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Isolation of ethylenediamine from industrial solution of ethylenediamine hydrochloride by electrodialysis

机译:电渗析法从乙二胺盐酸盐工业溶液中分离乙二胺

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摘要

An industrial solution of ethylenediamine hydrochloride which contains about 18% chloride and 12% amine was electrodialysed in a five-compartment cell to obtain pure ethylenediamine. Different parameters such as alkali concentration and current density were studied to optimise conditions of maximum current efficiency for amine recovery and chloride removal from the feed solution. The Suitabilities of different ion-exchange membranes for electrodialysis were compared. Variation in current efficiency for amine recovery with increases in the concentration of amine during electrodialysis was also studied. Current efficiency for amine recovery and chloride removal is about 78% and 91% respectively under optimum conditions. The amount of electrical energy consumed is 12.1 kWh kg(-1) for ethylenediamine recovery and 8.6 kWh kg(-1) for chloride removal. The concentration of pure amine obtained after the electrodialysis was around 20%. The results are encouraging for industrial applications whereby ethylenediamines free from chlorides can be isolated. (C) 2003 Society of Chemical Industry.
机译:在五室电解槽中将含有约18%氯和12%胺的乙二胺盐酸盐的工业溶液进行电渗析,以获得纯乙二胺。研究了诸如碱浓度和电流密度之类的不同参数,以优化用于从进料溶液中回收胺和去除氯的最大电流效率的条件。比较了不同离子交换膜对电渗析的适用性。还研究了在电渗析过程中,随着胺浓度的增加,胺回收电流效率的变化。在最佳条件下,目前用于胺回收和去除氯的效率分别约为78%和91%。回收乙二胺所消耗的电能为12.1 kWh kg(-1),而去除氯气所消耗的电能为8.6 kWh kg(-1)。电渗析后获得的纯胺浓度约为20%。该结果对于工业应用是令人鼓舞的,由此可以分离出不含氯化物的乙二胺。 (C)2003年化学工业协会。

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