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利用季铵盐(Aliquat 336)为反应剂,在较宽的pH值条件下,研究了对氨基苯磺酸稀溶液的萃取相平衡特性;测定了反应剂浓度、稀释剂种类、盐的存在以及溶液pH值对反应萃取平衡分配系数的影响;提出了反应剂与对氨基苯磺酸负离子的阴离子交换反应机理,建立了平衡分配系数D值的表达式。结果表明,极性稀释剂不利于对氨基苯磺酸的萃取,惰性稀释剂能提供较大的萃取平衡分配系数,其顺序为:苯>四氯化碳>氯仿>正辛醇;盐的存在会降低Aliquat 336的萃取效率;与三烷基胺(Alamine 336)相比,Aliquat 336具有更宽的pH值适用范围。 相似文献
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对氨基酚稀溶液的络合萃取 总被引:19,自引:2,他引:19
络合萃取法分离极性有机物稀溶液具有高效性和高选择性。本文在原有工作的基础上,利用三正辛胺、磷酸三丁酯或P204为络合剂,正辛醇或煤油为稀释剂,在不同的PH值条件下实验测定了对氨基酚稀溶液的萑取相平稳分析系数。 相似文献
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络合萃取法处理高浓度有机废水 总被引:18,自引:1,他引:18
介绍了高浓度有机废水的来源和处理现状。提出了高浓度有机废水的络合萃取处理方法的研究方向。阐述了络合萃取法处理高浓度有机废水的高效性 相似文献
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In this study, extraction of p-cresol from the simulated wastewater has been studied using centrifugal extractors and QH-1 extractant. The distribution ratio of p-cresol was approximately 308.5 in the QH-1-p-cresol (pH =2.0) system. The extraction stage efficiency of the single-stage centrifugal extractor was higher than 92%, and the extraction rate of the three-stage cascade was higher than 99%. When 15% NaOH was used for the stripping of p-cresol in QH-1 solution, the stripping rate of the three-stage cascade reached 100%. A mathematical model of multistage countercurrent extraction process that considers the phase volume change, extraction stage efficiency, and phase entrainment was used to simulate the extraction of p-cresol using centrifugal extractors. The calculated results using this model were in good agreement with the experimental results. 相似文献
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