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McCABE-THIELE ANALYSIS FOR EVALUATION OF EXTRACTION SEPARATION OF Co (II) AND Ni (II)

机译:用于萃取分离Co(II)和Ni(II)的McCABE-THIELE分析

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摘要

Industrial solvent extraction for the separation and recovery of metal ions is often carried out during the countercurrent multistage process. The determination of the operating conditions is performed by McCabe-Thiele analysis, which obtains the equilibrium extraction isotherms from extraction experiments. In such an analysis, it is possible to analyze the extraction condition of metal ions. In the case of a mixed solution of Co (II) and Ni (II), however, the analysis is very complicated. This is because, under the conditions in which the extraction of Co (II) takes place, the stripping of Ni (II) happens at the same time. When considering the separation of metal ions in a multicomponent system, it is optimal to establish an analytical method to provide important guidelines for the actual operation. In this study, the conditions in which Co (II) is extracted and Ni (II) is stripped are considered. The extraction behavior of Co (II) and the stripping behavior of Ni (II) can be estimated from the extraction isotherms. On the basis of the estimated results of each metal ion, the separation performance of each can be evaluated using the purity as an indicator. Through experiments that vary the phase ratio and stage number, the extraction and stripping behavior of the respective metal ions can be reasonably estimated.
机译:用于分离和回收金属离子的工业溶剂萃取通常在逆流多阶段过程中进行。通过McCabe-Thiele分析确定操作条件,该分析从萃取实验中获得平衡萃取等温线。通过这种分析,可以分析金属离子的提取条件。但是,在Co(II)和Ni(II)混合溶液的情况下,分析非常复杂。这是因为,在进行Co(II)萃取的条件下,Ni(II)的汽提同时发生。考虑多组分系统中金属离子的分离时,最好建立一种分析方法,为实际操作提供重要指导。在这项研究中,考虑了提取Co(II)和剥离Ni(II)的条件。从萃取等温线可以估算出Co(II)的萃取行为和Ni(II)的汽提行为。基于每种金属离子的估计结果,可以使用纯度作为指标评估每种金属的分离性能。通过改变相比和级数的实验,可以合理地估计相应金属离子的萃取和汽提行为。

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  • 来源
    《Technology Reports of Kansai University》 |2015年第57期|141-148|共8页
  • 作者单位

    Department of Chemical, Energy and Environmental Engineering, Kansai University, Suita, Osaka 564-8680, Japan;

    Department of Chemical, Energy and Environmental Engineering, Kansai University, Suita, Osaka 564-8680, Japan;

    Department of Chemical, Energy and Environmental Engineering, Kansai University, Suita, Osaka 564-8680, Japan;

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