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A method for the separation of europium of other lanthanides and / or actinides

机译:分离其他镧系元素和/或act系元素的p的方法

摘要

Europium values are separated from other rare-earth values (as defined) by contacting, e.g. at 25 DEG C., a solution of an acidic ester of phosphoric or phosphonic acid in carbon tetrachloride or aromatic water-immiscible hydrocarbons, with an aqueous solution containing a chromium III salt, e.g. CrCl3; either of which solutions may contain the rare earth and Eu values and to this solution is added a zinc amalgam with subsequent separation of the organic phase containing the trivalent rare earth from the aqueous phase containing Eu. Rare earths are defined as (a) lantanide rare earths, (b) Sc & Y, and (c) actinide rare earths which are trivalent in their principal valence state or in their normal valence state in aqueous solution, such as Am, Cm & Cf. The chromic chloride solution may have a concentration of 0.001 to 0.01M and sufficient Zn amalgam, e.g. containing 0.5% Hg, may be added to reduce all Eu present. Examples of the aromatic hydrocarbons are benzene, xylene, but preferably toluene. The acidic esters may be present in concentrations of 0.01 to 1.5F (Formality) and may be of the type (RO)2 PO(OH) and (G1O)(G)PO(OH) where R is alkyl, aryl and alkaryl, G an organic group or radical, and G1 an organic group; R, G and G1 preferably having at least 4C atoms each, to obtain a compound that has high water immiscibility, e.g. 2 ethyl-hexyl, n-octyl, monochloro-methyl and phenyl. Both the organic and aqueous solutions whose volume ratio may range from 20 : 1 to 1 : 20 may be flushed with an inert gas, e.g. N2 to remove all O2 and the contacting process carried out in an inert atmosphere. The rare earths in the organic solution may be back extracted into an aqueous solution by treatment with 2.5N HCl and Zn present in the aqueous solution may be removed by contact with tributyl phosphate. Likewise Eu may be separated from Cr in the aqueous solution by oxidation with air and extraction with an organic solution of an acidic ester of phosphoric or phosphonic acid. The separation of Eu from Pm, Sm, lanthanides including Y; 241Am, Cm and Cf are disclosed.ALSO:Europium values are separated from other rare-earth values (as defined) by contacting, e.g. at 25 DEG C., a solution of an acidic ester of phosphoric or phosphonic acid in carbon tetrachloride or aromatic water-immiscible hydrocarbons, with an aqueous solution containing a chromium III salt, e.g. CrCl3; either of which solutions may contain the rare earth and Eu values and to this solution is added a zinc amalgam with subsequent separation of the organic phase containing the trivalent rare earth from the aqueous phase containing Eu. Rare-earths are defined as (a) lanthanide rare-earths, (b) Sc and Y, and (c) actinide rare-earths which are trivalent in their principal valence state or in their normal valence state in aqueous solution, such as Am, Cm and Cf. The chromic chloride solution may have a concentration of 0.001 to 0.01 M and sufficient Zn amalgam, e.g. containing 0.5% Hg, may be added to reduce all Eu present. Examples of the aromatic hydrocarbons are benzene, xylene, but preferably toluene. The acidic esters may be present in concentrations of 0.01 to 1.5 F (Formality) and of the type (RO)2PO(OH) and (G1O)(G)PO(OH) where R is alkyl, aryl and alkaryl, G an organic group or radical, and G1 an organic group; R, G and G1 preferably having at least 4C atoms each, to obtain a compound that has high water immiscibility, e.g. 2 ethylhexyl, n-octyl, monochloro-methyl and phenyl. Both the organic and aqueous solutions whose volume ratio may range from 20 : 1 to 1 : 20 may be flushed with an inert gas, e.g. N2 to remove all O2 and the contacting process carried out in an inert atmosphere. The rare-earths in the organic solution may be back extracted into an aqueous solution by treatment with 2.5 N HC1 and Zn present in the aqueous solution may be removed by contact with tributyl phosphate. Likewise Eu may be separated from Cr in the aqueous solution by oxidation with air and extraction with an organic solution of an acidic ester of phosphoric or phosphonic acid. The separation of Eu from Pm, Sm, lanthanides including Y; 241Am, Cm and Cf are disclosed.
机译:contact值通过与其他稀土元素的接触来分离(如定义)。在25℃下,将磷酸或膦酸的酸性酯在四氯化碳或芳族水不混溶的烃中的溶液与含铬Ⅲ盐的水溶液,例如NaCl 3混合。 CrCl3;两种溶液都可以含有稀土和Eu值,并向该溶液中添加锌汞齐,然后从含有Eu的水相中分离出含有三价稀土的有机相。稀土定义为(a)镧系元素稀土,(b)Sc和Y和(c)act系元素稀土,它们在水溶液中的主价态或正常价态为三价,例如Am,Cm和cf.氯化铬溶液的浓度可以为0.001至0.01M,并具有足够的锌汞齐。可以添加含0.5%Hg的汞以减少所有存在的Eu。芳族烃的实例是苯,二甲苯,但优选甲苯。酸性酯的存在浓度为0.01至1.5F(形式),并且可以为(RO)2 PO(OH)和(G1O)(G)PO(OH)类型,其中R为烷基,芳基和烷芳基, G为有机基团或基团,而G1为有机基团; R,G和G1优选各自至少具有4C个原子,以获得具有高水不混溶性的化合物,例如H,G和G1。 2乙基己基,正辛基,一氯甲基和苯基。体积比可在20:1至1:20范围内的有机溶液和水溶液都可以用惰性气体冲洗,例如N 2去除所有O 2并在惰性气氛中进行接触过程。通过用2.5N HCl处理可以将有机溶液中的稀土反萃取到水溶液中,并且可以通过与磷酸三丁酯接触除去存在于水溶液中的锌。同样,可以通过用空气氧化并用磷酸或膦酸的酸性酯的有机溶液萃取将Eu从水溶液中的Cr中分离出来。 Eu从Pm,Sm,镧系元素(包括Y)中的分离;还公开了241Am,Cm和Cf。ALSO:通过例如接触接触将from值与其他稀土值(定义)分开。在25℃下,将磷酸或膦酸的酸性酯在四氯化碳或芳族水不混溶的烃中的溶液与含铬Ⅲ盐的水溶液,例如NaCl 3混合。 CrCl3;两种溶液都可以含有稀土和Eu值,并向该溶液中添加锌汞齐,然后从含有Eu的水相中分离出含有三价稀土的有机相。稀土被定义为(a)镧系元素稀土,(b)Sc和Y和(c)act系元素稀土,它们在水溶液(例如Am)中的主价态或正常价态是三价的,厘米和厘米。氯化铬溶液可具有0.001至0.01M的浓度和足够的Zn汞齐,例如0.1mg / ml。可以添加含0.5%Hg的汞以减少所有存在的Eu。芳族烃的实例是苯,二甲苯,但优选甲苯。酸性酯的存在浓度为0.01至1.5 F(形式),类型为(RO)2PO(OH)和(G1O)(G)PO(OH),其中R为烷基,芳基和烷芳基,G为有机基团或基团,G1为有机基团; R,G和G1优选各自至少具有4C个原子,以获得具有高水不混溶性的化合物,例如H,G和G1。 2乙基己基,正辛基,一氯甲基和苯基。体积比可在20:1至1:20范围内的有机溶液和水溶液都可以用惰性气体冲洗,例如N 2去除所有O 2并在惰性气氛中进行接触过程。通过用2.5N HCl处理可以将有机溶液中的稀土反萃取到水溶液中,并且可以通过与磷酸三丁酯接触除去存在于水溶液中的Zn。同样,可以通过用空气氧化并用磷酸或膦酸的酸性酯的有机溶液萃取将Eu从水溶液中的Cr中分离出来。 Eu从Pm,Sm,镧系元素(包括Y)中的分离;公开了241Am,Cm和Cf。

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