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method for separation of uranium, plutonium and fission products from depleted uranium nuclear fuel

机译:贫铀核燃料中铀,p和裂变产物的分离方法

摘要

A mixture of Pu/U/fission products, or a mixture of Fe, Co, and Ni are separated in solution by a graded concentration multi-stage extraction system. There is set up an array of vessels containing batches of an organic extractant for the species to be separated, or a solution of such extractant in an inert diluent, e.g. tributyl phosphate in CCl4 for U/Pu and trioctyl phosphine oxide in CCl4 for Fe, Co, Mi. The materials to be separated are in aqueous mineral acid solution, and a second series of vessels are prepared containing batches of aqueous mineral acid, each batch containing acid of different concentration, the concentration varying stepwise along the aqueous series, the final vessel of this series preferably containing water. The first aqueous batch, i.e. that containing the materials to be separated is mixed with the first batch of organic extractant, allowed to settle and separated, the aqueous layer is then shaken with the second organic batch, and separated and is then shaken in turn with all the remainder of the organic batches. The first aqueous batch is followed through the organic series by the second aqueous batch, i.e. an aqueous acid solution, and the third and subsequent aqueous batches until each aqueous batch has been treated with each organic batch. The net result of this procedure is that upon completion, the organic batches are uncontaminated and may be used again, whilst the mixture of solutes is so distributed through the aqueous series that each solute occupies almost exclusively a particular range of batches in the aqueous series and may thus be easily separated, e.g. 23 batches of aqueous nitric acid used in the separation of U/Pu/fission products batches 1-5 contained almost all the fission products, Pu 239 was contained in batches 6-10 and U was contained in batches 10-20, and similar results were obtained for Fe, Co and Mi using HCl solutions. If desired the concentration of extractant may be varied stepwise from batch to batch in the organic series.ALSO:In a graded concentration multistage extraction system, e.g for a mixture of Pu/U/fission products, or a mixture of Fe, Co, and Ni, there is set up an array of vessels containing batches of an organic extractant for the species to be separated or a solution of such extractant in an inert diluent e.g. tributyl phosphate in CCl4 for U/Pu and trioctyl phosphine oxide in CCl4 for Fe, Co, Mi. The materials to be separated are in aqueous mineral acid solution, and a second series of vessels are prepared containing batches of aqueous mineral acid, each batch containing acid of different concentration, the concentration varying stepwise along the aqueous series the final vessel of this series preferably containing water. The first aqueous batch i.e. that containing the materials to be separated is mixed with the first batch of organic extractant, allowed to settle and separated, the aqueous layer is then shaken with the second organic batch and separated, and is then shaken in turn with all the remainder of the organic batches. The first aqueous batch is followed through the organic series by the second aqueous batch, i.e. an aqueous acid solution, and the third and subsequent aqueous batches until each aqueous bath has been trated with each organic batch. The net result of this procedure is that upon completion, the organic batches are uncontaminated and may be used again, whilst the mixture of solutes is so distributed through the aqueous series that each solute occupies almost exclusively a particular range of batches in the aqueous series and may thus be easily separated e.g. of 23 batches of aqueous nitric acid used in the separation of U/Pu/fission products batches 1-5 contained almost all the fission products, Pu 239 was contained in batches 6-10 and U was contained in batches 10-20, and similar results were obtained for Fe, Co and Ni using HCl solutions. ]If desired the concentration of extractant may be varied stepwise from batch to batch in the organic series.
机译:Pu / U /裂变产物的混合物或Fe,Co和Ni的混合物通过分级浓度多级萃取系统在溶液中分离。设置了一系列容器,其中装有一批要分离的物种的有机萃取剂,或这种萃取剂在惰性稀释剂(例如盐酸)中的溶液。对于U / Pu,在CCl4中使用磷酸三丁酯;对于Fe,Co,Mi,在CCl4中使用三辛基氧化膦。待分离的物料在无机酸水溶液中,准备了第二批容器,其中装有一批无机酸水溶液,每批所含酸的浓度不同,浓度沿水性系列逐步变化,该系列的最终容器最好含有水。将第一批水,即含有要分离的物质的水与第一批有机萃取剂混合,使其沉降并分离,然后将水层与第二批有机物一起振摇,分离,然后依次与所有其余的有机批次。第一含水批料之后是有机系列,随后是第二含水批料,即酸水溶液,以及第三和随后的含水批料,直到每个含水批料已经用每个有机批料处理过。此过程的最终结果是,完成后,有机批次不受污染,可以再次使用,而溶质的混合物在水系列中分布得如此分散,以至于每个溶质在水系列中几乎都只占据特定范围的批次,并且因此可能容易分离,例如分离U / Pu /裂变产物1-5批中使用的23批硝酸水溶液几乎包含所有裂变产物,Pu 239包含在6-10批次中,U包含在10-20批次中,结果相似使用HCl溶液获得Fe,Co和Mi的元素。如果需要,萃取剂的浓度可以在有机系列的批次之间逐步变化。ALSO:在分级浓度的多级萃取系统中,例如,用于Pu / U /裂变产物的混合物,或Fe,Co和Fe的混合物镍,设置了一系列容器,其中包含用于待分离物种的一批有机萃取剂或此类萃取剂在惰性稀释剂中的溶液,例如对于U / Pu,CCl4中的磷酸三丁酯;对于Fe,Co,Mi,CCl4中的三辛基氧化膦。待分离的物料在无机酸水溶液中,并准备第二批容器,其中装有一批无机酸水溶液,每批中含有不同浓度的酸,浓度沿含水系列逐步变化,优选该系列的最终容器含有水。将第一批水,即含有待分离物料的水与第一批有机萃取剂混合,使其沉降并分离,然后将水层与第二批有机物一起振摇并分离,然后依次与所有有机物一起振摇。其余有机批次。第一水性批料之后是有机系列,随后是第二水性批料,即酸性水溶液,以及第三和随后的水性批料,直到每个水性浴已被每个有机批料处理过。此过程的最终结果是,完成后,有机批次不受污染,可以再次使用,而溶质的混合物在水系列中分布得如此分散,以至于每个溶质在水系列中几乎都只占据特定范围的批次,并且因此可能容易分离,例如用于U / Pu /裂变产物1-5分离的23批次硝酸水溶液中,几乎所有裂变产物都包含在其中,Pu 239包含在批次6-10中,U包含在批次10-20中,并且类似使用HCl溶液获得了Fe,Co和Ni的结果。 ]如果需要,萃取剂的浓度可以在有机系列的批次之间逐步变化。

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