Ehyaie Darya, Zaheri Parisa, Samadfam Mohammad, Zahakifar Fazel
Department of Energy Engineering, Sharif University of Technology, P.O. Box 11365-8639, Tehran, Iran.
Nuclear Fuel Cycle Research School, Nuclear Science and Technology Research Institute, P.O. Box: 11365-8486, Tehran, Iran.
Sci Rep. 2024 Dec 30;14(1):31897. doi: 10.1038/s41598-024-83397-1.
This study describes the use of the emulsion liquid membrane (ELM) technique to recover thorium (Th(IV)) from an aqueous nitrate solution. The components of the ELM were kerosene as a diluent, sorbitan monooleate (span 80) as a surfactant, bis(2,4,4-trimethylpentyl)phosphinic acid (Cyanex 272) as an extractant, and HSO solution as a stripping reagent. Th(IV) was more successfully extracted and separated under the following favorable conditions: Cyanex272 concentration of 0.11 mol/L; 0.65 mol/L HSO as a stripping phase (internal phase); feed phase (external phase) pH of 1; internal-to-membrane phase volume ratio of 1; emulsion-to-external phase volume ratio of 0.4; contact time of 25 min; and agitation speed of 300 rpm. Under these conditions, the membrane transferred Th(IV) selectively from the real leach liquor without appreciable emulsion breakage or swelling.
本研究描述了使用乳化液膜(ELM)技术从硝酸盐水溶液中回收钍(Th(IV))的方法。ELM的组成成分包括:作为稀释剂的煤油、作为表面活性剂的脱水山梨醇单油酸酯(司盘80)、作为萃取剂的双(2,4,4-三甲基戊基)膦酸(Cyanex 272)以及作为反萃剂的HSO溶液。在以下有利条件下,Th(IV)能更成功地被萃取和分离:Cyanex272浓度为0.11 mol/L;作为反萃相(内相)的HSO浓度为0.65 mol/L;料液相(外相)pH值为1;内相与膜相的体积比为1;乳液与外相的体积比为0.4;接触时间为25分钟;搅拌速度为300转/分钟。在这些条件下,膜能从实际浸出液中选择性地转移Th(IV),且不会出现明显的乳液破裂或膨胀现象。