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A method for the separation of thorium and uranium, thorium mass neutrons irradiated from a

机译:一种分离a和铀的方法,from辐照的mass质量中子。

摘要

In a liquid-liquid extraction process for recovering thorium and uranium values from a neutron-irradiated thorium composition by forming a nitrate ion-deficient aqueous solution from said composition and countercurrently contacting said solution with an aqueous immiscible organic solvent in a liquid-liquid extraction system containing a plurality of extraction stages divided into a first end extraction stage wherein said nitrate ion-deficient solution is introduced into said system, a plurality of intermediate extraction stages and a second end extraction stage for introduction of said organic solvent into said system, and a plurality of scrub stages preceding said first and extraction stage, the improvement consists in introducing an aqueous salting solution of nitric acid into any intermediate extraction stage of said system, countercurrently contacting said salting nitric acid solution with the solvent in said intermediate and succeeding extraction stages, passing thorium and uranium enriched solvent from each of said intermediate extraction stages to the first end extraction stage and thence to said scrub stages in countercurrent contact therein with an aqueous scrub to decontaminate said enriched solvent of residual amounts of fission products and protoactinium, cycling at least a portion of the thus contacted aqueous scrub to join the aqueous phase in said extraction stages and thereafter removing the decontaminated thorium and uranium enriched solvent from the scrub stages and the protoactinium and fission product-containing aqueous raffinate from said extraction stages. The aqueous scrub may be selected from the group consisting of water and an aqueous solution of nitric acid, the solution being no greater than 4 molar in nitric acid. Preferably the scrub solution contains a small amount of phosphate ions. The salting nitric acid solution should preferably be 13 to 16 molar. The organic extractant may be tributyl phosphate in a paraffinic hydrocarbon diluent. Specification 865,011 is referred to.
机译:在用于从中子辐照的composition组合物中回收composition和铀值的液-液萃取方法中,通过从所述组合物形成缺乏硝酸根离子的水溶液并使该溶液与不混溶的有机水溶液在液-液萃取系统中逆流接触包含多个萃取步骤,所述多个萃取步骤分为将所述硝酸根离子缺乏溶液引入所述系统的第一末端萃取步骤,用于将所述有机溶剂引入所述​​系统的多个中间萃取步骤和第二末端萃取步骤,以及在所述第一萃取阶段和萃取阶段之前的多个洗涤阶段,改进之处在于将硝酸的盐溶液引入所述系统的任何中间萃取阶段,在所述中间萃取阶段和随后的萃取阶段中使所述盐酸盐硝酸溶液与溶剂逆流接触, th和乌拉努m从每个所述中间萃取阶段到第一最终萃取阶段的浓缩溶剂,然后到所述洗涤阶段,在其中与含水洗涤液逆流接触,以净化残留量的裂变产物和原act的所述浓缩溶剂,循环至少一部分如此接触的含水洗涤液在所述萃取阶段加入水相,然后从洗涤阶段除去去污染的富含or和铀的溶剂,并从所述萃取阶段除去含有原act和裂变产物的萃余液。含水洗涤液可以选自水和硝酸水溶液,该溶液在硝酸中的浓度不大于4摩尔。优选地,洗涤溶液包含少量的磷酸根离子。盐酸盐硝酸溶液应优选为13至16摩尔。有机萃取剂可以是链烷烃稀释剂中的磷酸三丁酯。参考规范865011。

著录项

  • 公开/公告号DE1170918B

    专利类型

  • 公开/公告日1964-05-27

    原文格式PDF

  • 申请/专利权人 ATOMIC ENERGY COMMISSION;

    申请/专利号DE1961U007997

  • 发明设计人 RAINEY ROBERT HAMRIC;MOORE JOHN GREENE;

    申请日1961-05-04

  • 分类号C01F15;C01G43;C22B60/02;G21C19/46;

  • 国家 DE

  • 入库时间 2022-08-23 16:32:47

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