Department of Chemistry , Colorado School of Mines , Golden , Colorado 80401 , United States.
Nuclear Science and Engineering Program , Colorado School of Mines , Golden , Colorado 80401 , United States.
J Phys Chem B. 2019 Oct 10;123(40):8550-8558. doi: 10.1021/acs.jpcb.9b06224. Epub 2019 Sep 30.
The Actinide-Lanthanide Separation Process (ALSEP) is a solvent extraction approach for separating relevant trivalent minor actinides (e.g., americium and curium) from used nuclear fuel. However, relatively slow kinetics in the stripping step of the process restricts process throughput when scaled for industrial implementation. To assist in identifying specific kinetic barriers associated with the separation, the solvation and dynamic behaviors of the two organic extractants in the current ALSEP implementation, ,,','-tetra(2-ethylhexyl)diglycolamide (T2EHDGA) and 2-ethylhexylphosphonic acid mono-2-ethylhexyl ester (HEHEHP), were probed through molecular dynamics (MD) simulations. The simulations examined the effects of extractant and nitric acid concentration on the interfacial behavior of the extractants in three solvent systems (-dodecane, water, and -dodecane + water). Solvation analyses of T2EHDGA revealed expected amphiphilic behavior in pure solvent systems. In a nitric-acid-free biphasic solvent, it was found that T2EHDGA expressed similar interfacial conformations as HEHEHP, suggesting that a parallel-like configuration, relative to the interface, is adopted at low concentrations. When HNO was introduced to biphasic systems containing a single molecule of extractant, HEHEHP was observed to retain a relatively parallel orientation while the T2EHDGA orientation was no longer affected by the presence of the interface. At bulk extractant concentrations, representative of the ALSEP process, the presence of nitric acid had minimal impact on the ligand orientation. Calculated diffusion constants showed that only some systems involving T2EHDGA were affected by the presence of acid.
锕系-镧系分离工艺(ALSEP)是一种溶剂萃取方法,用于从乏核燃料中分离相关的三价次锕系元素(如镅和锔)。然而,该工艺在汽提步骤中的动力学相对较慢,限制了工业实施时的处理量。为了帮助确定与分离相关的特定动力学障碍,通过分子动力学(MD)模拟研究了当前 ALSEP 实施中两种有机萃取剂,即二(2-乙基己基)膦酸单-2-乙基己基酯(HEHEHP)和四(2-乙基己基)二甘醇酰胺(T2EHDGA)在溶剂中的溶剂化和动态行为。模拟研究了萃取剂和硝酸浓度对三种溶剂体系(-十二烷、水和-十二烷+水)中萃取剂界面行为的影响。T2EHDGA 的溶剂化分析表明,在纯溶剂体系中表现出预期的两亲性行为。在无硝酸的双相溶剂中,发现 T2EHDGA 表现出与 HEHEHP 相似的界面构象,表明在低浓度下,它采用相对平行的构象相对于界面。当将 HNO 引入含有单个萃取剂分子的双相体系中时,观察到 HEHEHP 保持相对平行的取向,而 T2EHDGA 的取向不再受界面的影响。在代表 ALSEP 工艺的代表萃取剂浓度下,酸的存在对配体取向的影响很小。计算得到的扩散常数表明,只有一些涉及 T2EHDGA 的体系受到酸的存在的影响。