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Improvements relating to processes for the separation of components of mixtures containing rare earths and, if desired, yttrium

机译:与分离含稀土和钇(如果需要)的混合物的成分的方法有关的改进

摘要

Ethylenediamine tetraacetic acid is recovered from eluates from ion exchange columns containing complexes of said acid with rare earth metals, yttrium, and cadmium or zinc by acidifying with sufficient hydrochloric, nitric or sulphuric acid to provide an excess of at least 0,07 moles/1., agitating for 8-16 hours and altering. From the filtrate thus produced, rare earth metal and yttrium oxalates may be precipitated.ALSO:Individual rare earth metals and yttrium are partially separated either (a) by absorbing the metals in a cation exchange resin bed, eluting the bed with a solution of a watersoluble salt of an aminopolyacetic acid, passing the eluate through a bed of cation exchange resin in the zinc or cadmium form and collecting successive fractions or (b) by charging a cation exchange resin bed with a solution containing the mixture to be separated together with zinc or cadmium salts, eluting the bed with the above-mentioned eluting agent and collecting successive fractions. Satisfactory results are obtained with a ratio of Zn or Cd:rare earths of 5:1 to 1:3. Specified complexing agents are ethylenediamine tetraacetic acid (ammonium or sodium salt), nitrilotriaceticacid, hydroxyethylenediaminetriacetic acid, diethylenetriaminepentaacetic acid and diaminocyclohexanetetraacetic acid. The preferred resins are sulphonated copolymers of styrene and divinyl benzene having a cross linkage of 4% or less. Specified metals are Y and La, Pr, Nd, Sm, Dy, Ho, Er, Tm and Yb. Ethylenediaminetetraacetic acid may be recovered from the eluate by adding hydrochloric, nitric or sulphuric acid. The metals may be recovered from the resultant solutions as carbonates, fluorides, oxalates or hydroxides; or said solutions may be fed as such, or after mixing with the original feed solution, to cation exchange column for further fractionation.
机译:通过用足够的盐酸,硝酸或硫酸酸化以提供过量至少0,07摩尔/ 1的溶液,从含有所述酸与稀土金属,钇,镉或锌的络合物的离子交换柱的洗脱液中回收乙二胺四乙酸。,搅动8-16小时并改变。稀土金属和草酸钇可能会从生成的滤液中沉淀出来.ALSO:通过(a)在阳离子交换树脂床中吸收金属,并用一种氨基多乙酸的水溶性盐,使洗出液通过锌或镉形式的阳离子交换树脂床,并收集连续的馏分;或(b)通过在阳离子交换树脂床中装入含有待与锌一起分离的混合物的溶液或镉盐,用上述洗脱剂洗脱床层并收集连续的馏分。 Zn或Cd:稀土元素的比例为5:1至1:3可获得令人满意的结果。具体的络合剂是乙二胺四乙酸(铵盐或钠盐),次氮基三乙酸,羟基乙二胺三乙酸,二亚乙基三胺五乙酸和二氨基环己烷四乙酸。优选的树脂是交联度为4%或更小的苯乙烯和二乙烯基苯的磺化共聚物。指定的金属为Y和La,Pr,Nd,Sm,Dy,Ho,Er,Tm和Yb。乙二胺四乙酸可通过加入盐酸,硝酸或硫酸从洗脱液中回收。金属可以从所得溶液中以碳酸盐,氟化物,草酸盐或氢氧化物的形式回收;或者可以将所述溶液本身或与原始进料溶液混合后进料至阳离子交换塔中以进一步分馏。

著录项

  • 公开/公告号GB854926A

    专利类型

  • 公开/公告日1960-11-23

    原文格式PDF

  • 申请/专利权人 PAWEL KRUMHOLZ;KAZIMIERZ JOZEF BRIL;

    申请/专利号GB19580027659

  • 发明设计人

    申请日1958-08-28

  • 分类号B01J39/26;C01F17;

  • 国家 GB

  • 入库时间 2022-08-23 18:23:41

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