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Selective separation of praseodymium(III) by di-(2-ethylhexyl) phosphoric acid using the complexing agent

机译:使用络合剂通过二(2-乙基己基)磷酸选择镨(III)的选择性分离

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It is a main problem that environment can be polluted by discharge of wastewater containing NH_4~+, Ca~(2+) and Na~+, when rare earths (REs) are extracted in a saponified system using di-(2-ethylhexyl) phosphoric acid (D2EHPA). Pointing to this problem, the selective separation of Pr(III) by liquid–liquid extraction using D2EHPA in the presence of a complexing agent of lactic acid (LA) has been studied. Results are shown that the maximum of separation factor (β) between Pr/Ce is 2.04 and extraction selectivity is also enhanced when compared with that of D2EHPA-HCl system. The thermodynamic function △H is determined as exothermically driven. The cation exchange mechanism is discussed by IR spectra. Thus, the results suggest that highly selective separation and extraction of Pr(III) from a Pr/Ce solution is possible, providing a simple and environment-friendly complexing method for extraction-separation rare earths, and promoting the sustainable development in rare earths practices.
机译:这是一种主要问题,即在使用二甲基化系统中萃取稀土(2-乙基己基),通过含有NH_4〜+,Ca〜+,Ca〜+,Ca〜(2+)和Na +的废水排出的主要问题磷酸(D2ehpa)。指向该问题,已经研究了在存在乳酸(1a)络合剂存在下使用D2ehpa的液液提取的Pr(III)的选择性分离。结果表明,与D2EhPA-HCl系统相比,Pr / Ce之间的分离因子(β)和萃取选择性也增强。热力学功能△H被确定为放热驱动。阳离子交换机制由IR光谱讨论。因此,结果表明,可以从PR / CE解决方案中获得高度选择性分离和提取Pr(III),为提取分离稀土,并促进稀土实践中的可持续发展,提供简单和环保的络合方法。 。

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