首页> 外国专利> PROCESS FOR THE FINE PURIFICATION, BY LOTS, OF URANIUM OR PLUTONIUM WHICH MUST BE RECOVERED IN AN OPERATION FOR THE PROCESSING OF NUCLEAR FUELS AND / OR IRRADIATED FERTILE MATERIALS

PROCESS FOR THE FINE PURIFICATION, BY LOTS, OF URANIUM OR PLUTONIUM WHICH MUST BE RECOVERED IN AN OPERATION FOR THE PROCESSING OF NUCLEAR FUELS AND / OR IRRADIATED FERTILE MATERIALS

机译:大量纯化铀或P的过程,必须在操作过程中回收铀或P,以进行核燃料和/或辐照的金属材料的加工

摘要

Process for the batch purification of uranium recovered in a reprocessing process, after a first separation of impurities, in which for each batch an aqueous, nitric acid uranyl-nitrate solution (UNH original solution), which still contains residual amounts of impurities, is cooled to crystallize out purified UO2(NO3)2x6H2O (UNH) from the solution and the resulting crystals are separated out of their mother liquor and washed. The original solution is adjusted to a specified uranium concentration and the adjusted solution is cooled to below 0 DEG C. to bring about the crystallization. The duration between starting and ending the crystallization is held between 0.1 and 10 hours. The amount of the UNH crystals which is crystallized out corresponds to at least about 80 weight % of the uranium content introduced. The ratio of the volume of the crystals formed to the volume of the remaining mother liquor is not larger than 0.5. A final concentration of nitric acid is estabilished in the mother liquor between 6 and 12 mol/l HNO3 at room temperature. A joint crystallizing out of UNH with water as ice and/or with nitric acid trihydrate (HNO3x 3H2O) is avoided. The resulting mother liquor is separated from the crystals and then recycled. The separated crystals are washed at least one time with an HNO3 solution having a similar acid content and similar temperature to that of the separated mother liquor at the end of the crystallization procedure. A batch process for purifying plutonium or plutonium and uranium is also disclosed.
机译:在第一次分离杂质之后,对在后处理过程中回收的铀进行分批提纯的方法,在该方法中,每批都冷却仍含有残留杂质的硝酸铀酰硝酸铀酸酯水溶液(UNH原始溶液)从溶液中结晶出纯化的UO2(NO3)2x6H2O(UNH),然后将所得晶体从母液中分离出来并洗涤。将原始溶液调节至指定的铀浓度,并将调节后的溶液冷却至低于0℃以引起结晶。开始和结束结晶之间的持续时间保持在0.1至10小时之间。结晶出的UNH晶体的量对应于引入的铀含量的至少约80重量%。所形成的晶体的体积与剩余母液的体积之比不大于0.5。在室温下,确定母液中硝酸的终浓度为6至12 mol / l HNO3。避免了用水,冰和/或硝酸三水合物(HNO3x 3H2O)从UNH中结晶出来的接头。将所得母液与晶体分离,然后再循环。在结晶过程结束时,用酸含量和温度与分离的母液相似的HNO 3溶液洗涤分离的晶体至少一次。还公开了用于纯化p或p和铀的间歇方法。

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