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Stripping dispersion hollow fiber liquid membrane containing PC-88A as carrier and HCl for transport behavior of trivalent dysprosium

机译:剥离分散中空纤维液膜,含有pC-88a作为载体和HCl,用于三价镝的输送行为

摘要

The transport of Dy(3+) through stripping dispersion hollow fiber liquid membrane system (SDHFLM) containing dispersion phase with HCl solution as stripping solution and 2-ethyl hexyl phosphoric acid-mono-2-ethyl hexyl ester (PC-88A) dissolved in kerosene as membrane solution, has been studied. Many factors of the interface chemical reaction and composition of the liquid membrane including pH value, initial concentration of Dy(3+), different ionic strength of feed phase, volume ratio of membrane solution to stripping solution (O/W), HCl concentration, carrier concentration, different stripping agents of dispersion phase, hydrodynamic characteristic (flow rates, stability) and hollow fiber structure parameters (inner diameter of fibers, membrane thickness, porosity, etc.) on Dy(3+) transport with SDHFLM were investigated. The advantages of SDHFLM compared to the traditional HFLM was investigated too. Experimental results indicated that the optimum transport conditions of Dy(3+) were that HCl concentration was 4.00 mol/L, PC-88A concentration was 0.150 mol/L, O/W was 0.5 in the dispersion phase, and pH value was 5.00 in the feed phase. Ionic strength had no obvious effect on transport of Dy(3+). When initial Dy(3+) concentration was 1.50 x 10(-4) mol/L, the transport efficiency of Dy(3+) was up to 95.4% in 170 min. The kinetic equation was developed in terms of the law of mass diffusion and the theory of interface chemistry. The results were in good agreement with the literature data. (C) 2011 Elsevier B.V. All rights reserved.
机译:Dy(3+)通过以HCl溶液为溶出液的分散相中含有分散相的溶出分散中空纤维液膜系统(SDHFLM)的传输和溶解在其中的2-乙基己基磷酸-单-2-乙基己酯(PC-88A)煤油作为膜溶液已被研究。界面化学反应和液膜组成的许多因素包括pH值,Dy(3+)的初始浓度,进料相的离子强度不同,膜溶液与汽提溶液的体积比(O / W),HCl浓度,通过SDHFLM研究了载流子浓度,分散相的不同脱模剂,流体力学特性(流速,稳定性)和中空纤维结构参数(纤维内径,膜厚度,孔隙率等)。与传统的HFLM相比,SDHFLM的优势也得到了研究。实验结果表明,Dy(3 +)的最佳迁移条件为分散相中HCl浓度为4.00 mol / L,PC-88A浓度为0.150 mol / L,O / W为0.5,pH值为5.00。进料阶段。离子强度对Dy(3+)的运输没有明显的影响。当Dy(3+)的初始浓度为1.50 x 10(-4)mol / L时,Dy(3+)的运输效率在170分钟内高达95.4%。根据质量扩散定律和界面化学理论建立了动力学方程。结果与文献数据吻合良好。 (C)2011 Elsevier B.V.保留所有权利。

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