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Hydroxypyridinone Derivatives: A Low-pH Alternative to Polyaminocarboxylates for TALSPEAK-like Separation of Trivalent Actinides from Lanthanides

机译:羟基吡啶酮衍生物:用于从镧系元素的Talspeak样的多氨基羧酸盐的低pH替代物

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Separation of lanthanides (Ln) from actinides (An) is unanimously challenging in reprocessing used nuclear fuel despite of much dedicated efforts over the past several decades. The TALSPEAK process is the current reference method in the United States for Ln~(3+)/An~(3+) separation but suffers from several limitations, such as a narrow working pH window (3.5–4.0), costly pH buffers, and slow extraction kinetics. Studies aiming at improving TALSPEAK have so far focused on polyaminocarboxylates hold-back reagents. Here, a new class of water-soluble ligands comprising hydroxypyridinone metal-binding units are evaluated for Ln~(3+)/An~(3+) separation. The model octadentate chelator 3,4,3-LI(1,2-HOPO) (abbreviated as HOPO) was used in combination with several industry-relevant organic extractants to separate Gd from four transplutonium elements (Am, Cm, Bk, and Cf). Cyanex 301 GN and HDEHP worked best in combination with HOPO, whereas HEH[EHP], Cyanex 572, and ACORGA M5640 did not yield practical Ln~(3+)/An~(3+) separation. Separation factors between Gd~(3+) and Am~(3+) reach about 50 with the HOPO/Cyanex 301 GN system and 30 with the HOPO/HDEHP system. The results using HDEHP (SF_(Gd/Am) = 30, SF_(Gd/Cm) = 8.5, and SF_(Gd/Cf) = 773) are high enough for industrial applications, and the proposed system works at pH values as low as 1.5, which simplifies the process by eliminating the need for pH buffers. In contrast to previously proposed methods, the HOPO-based process is also highly selective at separating Bk from Ln~(3+) (SF_(Gd/Bk) = 273) owing to in situ , spontaneous oxidation of Bk(III) to Bk(IV) by HOPO. The optimal pH in the case of HOPO/Cyanex 301 GN is 3.6 (SF_(Am/Gd) = 50, SF_(Cm/Gd) = 23, SF_(Bk/Gd) = 1.4, and SF_(Cf/Gd) = 3.2), but this system has the advantage of extracting An ions into the organic phase while keeping Ln ions in the aqueous phase, which is opposite to the conventional TALSPEAK process. This study represents the first optimization of a TALSPEAK-like Ln/An separation method using a HOPO chelator and paves the avenue for further developments of analytical science and reprocessing of used nuclear fuel.
机译:尽管过去数十年来,尽管过去几十年来,但在后处理二十年的努力中,镧系元素(A)的分离是一致挑战。 Talspeak工艺是美国LN〜(3 +)/ AN〜(3+)分离的当前参考方法,但遭受了几个限制,例如窄的工作pH窗口(3.5-4.0),昂贵的pH缓冲液,和缓慢的提取动力学。目前旨在改善Talspeak的研究旨在聚焦在聚酰胺羧酸盐背后试剂上。这里,评估包含羟基吡啶酮金属结合单元的新一类水溶性配体,用于LN〜(3 +)/ An〜(3+)分离。八月螯合剂3,4,3-Li(1,2-Hopo)(ZHOS)(缩写为HOPO)与若干行业相关的有机萃取剂组合使用,以将GD分离出四种转蛋白元素(AM,CM,BK和CF )。 Cyanex 301 GN和HDehp与Hopo相结合,而Heh [EHP],Cyanex 572和ACORGA M5640没有产生实用的LN〜(3 +)/ AN〜(3+)分离。 GD〜(3+)和AM〜(3+)之间的分离因子达到大约50个,其中跳高/富雪斯301 GN系统和跳跃/ HDEHP系统30。使用HDEHP的结果(SF_(GD / AM)= 30,SF_(GD / CM)= 8.5和SF_(GD / CF)= 773)足够高,适用于工业应用,并且所提出的系统在pH值下工作至1.5,通过消除对pH缓冲液的需要简化了过程。与先前所提出的方法相比,跳跃的方法在分离LN〜(3+)(SF_(GD / BK)= 273)时也具有高度选择性,因为原位,自发氧化BK(III) )通过跳跃到BK(IV)。在Hopo / Cyanex 301 Gn的情况下的最佳pH值为3.6(SF_(AM / GD)= 50,SF_(CM / GD)= 23,SF_(BK / GD)= 1.4和SF_(CF / GD)= 3.2),但该系统具有将离子提取到有机阶段的优点,同时保持水相中的LN离子,这与传统的Talspeak工艺相反。本研究代表了使用Hopo Chelator的Talspeak样LN /分离方法的第一次优化,并为进一步发展的分析科学和二手核燃料再加工的进一步发展提供途径。

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