首页> 外国专利> process for oxydieren of aqueous thallium (i) or cerium (iii) - saline solutions to thallium (iii). cerium (iv) saline solutions by using electrolysis

process for oxydieren of aqueous thallium (i) or cerium (iii) - saline solutions to thallium (iii). cerium (iv) saline solutions by using electrolysis

机译:aqueous(i)或铈(iii)-盐溶液制得(iii)的方法电解法制得铈(iv)盐溶液

摘要

1,209,991. Electrolytic oxidation. CINCINNATI MILLING MACHINE CO. Feb. 5, 1968 [Feb. 15, 1967], No.5620/68. Heading C7B. A solution of a thallium (I) or cerium (III) salt, e.g. the sulphate, is oxidized by passing the solution into the cathode compartment of a divided electrolyte cell, removing the cathodically generated hydrogen and passing the solution into the anode compartment of the cell in which oxidation of said metallic ion occurs to form the thallium (III) or cerium (IV) salt, removing the anodically generated oxygen and recovering the resultant oxidized metallic ion solution; the cell being divided by a membrane which whilst it impedes the back-migration of the oxydized metallic ion into the cathode compartment, permits transport of hydrogen ions through the membrane; and the electrode materials being essentially inert and such that the cathode has a sufficiently low hydrogen over-voltage to prevent reduction of the metallic ions, e.g. platinized platinum or platinized titanium, and such that the anode has a sufficiently high oxygen over-voltage to effect the oxydation of the metallic ions, e.g. lead, platinum, platinized platinum or platinized titanium. The electrodes may be supported between pairs of plastic grids. The membranes used may be of reinforced anion or cation exchange resin, microfibreglass matting or microporous membranes of polypropylene or P.T.F.E. Oxidation of the metal ions may result from an oxidizing agent formed at the anode-electrolyte interface, e.g. lead dioxide or activated oxygen. Cells may be assembled to operate in parallel, pumps and surge tanks being provided for passage of the electrolyte.
机译:1,209,991。电解氧化。辛辛那提铣床有限公司,1968年2月5日[Feb. 1967年第15号],第5620/68号。标题C7B。 ((I)或铈(III)盐的溶液,例如通过将溶液传递到分开的电解质电池的阴极隔室,除去阴极产生的氢并将溶液传递到其中发生所述金属离子氧化而形成form(III)的阳极隔室来氧化硫酸盐或铈(IV)盐,除去阳极产生的氧气并回收所得的氧化的金属离子溶液;电解池被膜分隔,该膜阻止了氧化的金属离子向阴极室的反迁移,但允许氢离子通过膜的传输。所述电极材料基本上是惰性的,并且所述阴极具有足够低的氢过电压以防止金属离子例如金属的还原。镀铂金或镀铂钛,并且使得阳极具有足够高的氧过电压以实现金属离子例如金属离子的氧化。铅,铂,镀铂金或镀铂钛。电极可以支撑在成对的塑料栅格之间。所用的膜可以是增强的阴离子或阳离子交换树脂,微纤维玻璃消光膜或聚丙烯或P.T.F.E的微孔膜。金属离子的氧化可以由在阳极-电解质界面处形成的氧化剂引起,例如,在阳极-电解质界面处。二氧化铅或活性氧。可以组装电池以使其并联运行,设置泵和缓冲罐以使电解质通过。

著录项

  • 公开/公告号CH505758A

    专利类型

  • 公开/公告日1971-04-15

    原文格式PDF

  • 申请/专利权人 THE CINCINNATI MILLING MACHINE COMPANY;

    申请/专利号CH19680002065

  • 发明设计人 H. FRYEALFRED;

    申请日1968-02-12

  • 分类号C01F17/00;C01G15/00;

  • 国家 CH

  • 入库时间 2022-08-23 09:59:49

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