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METHOD FOR CRYSTALLIZATION SEPARATION AND PURIFICATION OF URANYL NITRATE HEXAHYDRATE AND DEVICE FOR ITS IMPLEMENTATION

机译:结晶分离和纯化硝酸亚硝酸盐六水合物和装置的方法

摘要

FIELD: crystallization technologies. ;SUBSTANCE: group of inventions relates to heat and mass transfer processes in systems with liquid and solid phases, namely, to a method for crystallization separation and purification of uranyl nitrate hexahydrate, which includes the crystallization of uranyl nitrate hexahydrate from a concentrated nitric acid solution of uranyl nitrate, a feed stream with a composition corresponding to the ratio [UN]=78.49 - k[HNO3], where [UN] and [HNO3] are the concentrations of uranyl nitrate and nitric acid, wt. % ; where 78.49 is the concentration of uranyl nitrate in the crystalline uranyl nitrate hexahydrate, wt. %; k - the coefficient determining the position of the working line of the crystallization process and having a numerical value from 1.50 to 2.24, preferably from 1.57 to 1.80, separation of crystals of uranyl nitrate hexahydrate and the mother solution, countercurrent washing of crystals, collection of crystals of uranyl nitrate hexahydrate into a collection tank with simultaneous displacement of the washing solution from the tank into the washing zone and unloading of the purified product, and crystallization of uranyl nitrate hexahydrate from the feed stream, washing and collection of crystals it is carried out under isothermal conditions, while the initial, including the non-uranium composition of the washing solution meets the condition of the family of working lines 78.49=k1[HNO3], where [HNO3] is the content of nitric acid in the washing solution, wt. % and k1≤k, where k1 is the coefficient determining the position of the working line of the washing process, the mother solution and the spent washing solution are sent in a single stream to additional crystallization carried out at a temperature below the crystallization temperature with countercurrent movement of the liquid and solid phases, the crystals of uranyl nitrate hexahydrate of additional crystallization are washed together with the crystals obtained from the feed stream, and the mother solution of additional crystallization is removed from the process. In addition, a device for crystallization separation and purification of uranyl nitrate hexahydrate is described, containing an additional mold with a paddle agitator and a thermostatic case mounted on the outlet of the mother and washing solutions, while the axis of the additional mold is parallel to the axis of the mold. ;EFFECT: simplifying the technological process by achieving high and independent indicators for the operational yield and purification of the product, which can be used in hydrometallurgical technologies of the nuclear fuel cycle at the stages of refining natural or regenerated uranium. ;4 cl, 3 dwg, 1 tbl
机译:领域:结晶技术。 ;物质:本发明组涉及具有液相和固相的系统中的热量和传质方法,即,用于结晶分离和纯化硝酸铀酰六水合物的方法,其包括从浓硝酸溶液中结晶硝酸铀酸六水合物的结晶硝酸铀酰,含有对应于比率[UN] = 78.49-k [HNO3]的组合物的进料流,其中[接合UN3]是硝酸铀酰和硝酸的浓度,WT。 %;其中78.49是硝酸铀腈六水合物中的硝酸铀酰浓度,wt。 %; k - 系数确定结晶过程的工作线的位置,并具有从1.50至2.24的数值,优选1.57-1.80,分离亚硝酸叔丁酸六水合物和母溶液的晶体,晶体的逆流洗涤,收集亚硝酸铀酰六水合物中的晶体中的收集罐中的洗涤液与洗涤溶液同时置换到洗涤区和纯化产物的卸载,以及从进料流中的硝酸铀六水合物的结晶,洗涤和收集它的晶体在等温条件下,虽然包括洗涤溶液的非铀组成的初始,但是在78.49 = K1 [HNO3]的族的条件下,其中[HNO3]是洗涤溶液中硝酸的含量,而WT 。 %和K1≤k,其中K1是确定洗涤过程的工作线的位置的系数,母溶液和废洗涤溶液在单流中送至在低于结晶温度的温度下进行的额外结晶液体和固相的逆流运动,附加结晶硝酸铀酸六水合物的晶体与从进料流获得的晶体一起洗涤,并从该方法中除去额外结晶的母溶液。另外,描述了一种用于结晶分离和纯化硝酸亚硝酸亚己二醇的纯化的装置,其含有另外的模具,其具有桨搅拌器和安装在母体和洗涤溶液的出口上的恒温壳体,而另外模具的轴线平行于模具的轴线。 ;效果:通过实现高和独立指标来简化技术过程,以实现产品的运行产量和纯化,可用于精炼天然或再生铀的核燃料循环的核燃料循环的液态冶金技术。 ; 4 cl,3 dwg,1 tbl

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