首页> 外国专利> A method for the separation of uranium from uranium, zirconium and fission products, containing uranium fuel consumed elements

A method for the separation of uranium from uranium, zirconium and fission products, containing uranium fuel consumed elements

机译:从含铀燃料消耗元素的铀,锆和裂变产物中分离铀的方法

摘要

Uranium and zirconium are separated from spent nuclear fuel elements containing them by inserting the element within a fluidised bed of inert granular solids, introducing anhydrous hydrogen chloride to convert the zirconium to PICT:0925178/III/1 zirconium tetrachloride and recovering the latter, and thereafter introducing gaseous fluorine which reacts with the uranium and fission products to form a gaseous uranium hexafluoride-containing effluent gas which is fractionated to recover the uranium hexafluoride. The hydrochlorination of the zirconium may be carried out 350-450 DEG C. whilst the fluorination is suitably effected at 350-475 DEG C. As shown in Fig. 1 a jacketed reactor 10 is provided with a foraminous support 26 for supporting the zirconium clad uranium rod 22. The reactor is initially heated to 350-450 DEG C. by introducing liquid sodium into the jacket 16 whilst fluidising with a helium or argon stream; thereafter hydrogen chloride is introduced through line 28 whilst coolant is introduced through the jacket to control the exothermic reaction. Zirconium tetrachloride product is withdrawn via a filter 30 to line 32. Heated sodium is then passed through jacket 16 to raise the temperature to 400 DEG C. whereupon gaseous fluorine in a concentration of 5-100% of the gaseous phase is introduced through line 34; the uranium hexafluoride, plutonium hexafluoride and other volatile fission product fluorides are withdrawn through a line 36 to a distillation zone where uranium hexafluoride is recovered.
机译:通过将铀和锆与包含在其中的乏核燃料元素分离,方法是将其插入惰性颗粒状固体流化床中,引入无水氯化氢将锆转化为四氯化锆,并回收后者,然后引入气态氟,该气态氟与铀和裂变产物反应形成气态的含六氟化铀的流出气体,将其分馏以回收六氟化铀。锆的氢氯化反应可以在350-450℃下进行,而氟化反应则适宜在350-475℃下进行。如图1所示,夹套反应器10装有用于支撑包层锆的多孔载体26。铀棒22。通过将液态钠引入夹套16中,同时用氦或氩流流化,将反应器最初加热到350-450℃。然后通过管线28引入氯化氢,同时通过夹套引入冷却剂以控制放热反应。通过过滤器30将四氯化锆产物排出至管线32。然后将加热的钠通过夹套16,以将温度升高至400℃。随后,通过管线34引入浓度为气相的5-100%的气态氟。 ;六氟化铀,六氟化p和其他挥发性裂变产物氟化物通过管线36排出到蒸馏区,回收六氟化铀。

著录项

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号