{"title":"Optimal Extraction and Separation of Europium and Samarium from Nitrate Medium Using Binary Mixture of Cyanex 572 and Tertiary Amine Extractants","authors":"Soad E. Rizk, Rasha Gamal, Naglaa E. El-Hefny","doi":"10.1080/07366299.2023.2271049","DOIUrl":null,"url":null,"abstract":"ABSTRACTExtraction and separation of rare-earth elements (Eu(III) and Sm(III)) from nitrate solutions were studied using Cyanex 572 and Alamine 336 type extractants, as well as their binary mixtures in kerosene. Separate studies were carried out on the parameters that influence the extraction process. According to the slope analysis method, the composition of extracted species in the organic phase is [MNO3A2(HA)2][R3NH.NO3]2(Org). The mixture loading capacity towards Eu(III) and Sm(III), as well as the stripping of their loads from the organic phases, were also tested. After being treated with a NaOH solution, the stripped binary mixture was regenerated. The FT-IR spectra of the binary mixture organic phase, the organic phase loaded with metals, the stripped organic phase, and the regenerated organic phase were identified and compared. The separation method is based on a combined reduction-precipitation process in which europium is reduced to its bivalent state by commercial zinc metal, followed by the precipitation of its sparingly soluble europous sulphate. The developed method was used to separate a synthetic mixture of Eu(III) and Sm(III) from an analogous solution in nitrate medium to that expected from spent nuclear fuel leach liquor. Extraction and separation processes for Eu(III) and Sm(III) were detailed in a flowchart.KEYWORDS: Alamine 336Cyanex 572Europium(III)Samarium(III)solvent extraction AcknowledgmentsThe authors would like to thank Cytec Industries for supplying a commercial sample of Cyanex 572. The Egyptian Atomic Energy Authority funded this research, which received no specific funding from public, commercial, or non-profit funding agencies.Disclosure statementNo potential conflict of interest was reported by the author(s).","PeriodicalId":22002,"journal":{"name":"Solvent Extraction and Ion Exchange","volume":"151 2","pages":"0"},"PeriodicalIF":1.8000,"publicationDate":"2023-10-26","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Solvent Extraction and Ion Exchange","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.1080/07366299.2023.2271049","RegionNum":4,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"CHEMISTRY, MULTIDISCIPLINARY","Score":null,"Total":0}
引用次数: 0
Abstract
ABSTRACTExtraction and separation of rare-earth elements (Eu(III) and Sm(III)) from nitrate solutions were studied using Cyanex 572 and Alamine 336 type extractants, as well as their binary mixtures in kerosene. Separate studies were carried out on the parameters that influence the extraction process. According to the slope analysis method, the composition of extracted species in the organic phase is [MNO3A2(HA)2][R3NH.NO3]2(Org). The mixture loading capacity towards Eu(III) and Sm(III), as well as the stripping of their loads from the organic phases, were also tested. After being treated with a NaOH solution, the stripped binary mixture was regenerated. The FT-IR spectra of the binary mixture organic phase, the organic phase loaded with metals, the stripped organic phase, and the regenerated organic phase were identified and compared. The separation method is based on a combined reduction-precipitation process in which europium is reduced to its bivalent state by commercial zinc metal, followed by the precipitation of its sparingly soluble europous sulphate. The developed method was used to separate a synthetic mixture of Eu(III) and Sm(III) from an analogous solution in nitrate medium to that expected from spent nuclear fuel leach liquor. Extraction and separation processes for Eu(III) and Sm(III) were detailed in a flowchart.KEYWORDS: Alamine 336Cyanex 572Europium(III)Samarium(III)solvent extraction AcknowledgmentsThe authors would like to thank Cytec Industries for supplying a commercial sample of Cyanex 572. The Egyptian Atomic Energy Authority funded this research, which received no specific funding from public, commercial, or non-profit funding agencies.Disclosure statementNo potential conflict of interest was reported by the author(s).
期刊介绍:
Solvent Extraction and Ion Exchange is an international journal that publishes original research papers, reviews, and notes that address all aspects of solvent extraction, ion exchange, and closely related methods involving, for example, liquid membranes, extraction chromatography, supercritical fluids, ionic liquids, microfluidics, and adsorption. We welcome submissions that look at: The underlying principles in solvent extraction and ion exchange; Solvent extraction and ion exchange process development; New materials or reagents, their syntheses and properties; Computational methods of molecular design and simulation; Advances in equipment, fluid dynamics, and engineering; Interfacial phenomena, kinetics, and coalescence; Spectroscopic and diffraction analysis of structure and dynamics; Host-guest chemistry, ion receptors, and molecular recognition.