Method for producing peroxodisulfate
    1.
    发明专利
    Method for producing peroxodisulfate 有权
    生产过氧化脂肪酸的方法

    公开(公告)号:JP2013136842A

    公开(公告)日:2013-07-11

    申请号:JP2013038806

    申请日:2013-02-28

    CPC classification number: C25B1/285

    Abstract: PROBLEM TO BE SOLVED: To provide an industrial method for producing ammonium peroxodisulfate and alkali metal peroxodisulfate which is capable of completely eliminating the use of accelerators and is implemented when an electrolysis is of low current density.SOLUTION: In the case of the method for producing the peroxodisulfate, for example, ammonium peroxodisulfate, sodium peroxodisulfate, and potassium peroxodisulfate by anodically oxidizing an electrolyte containing sulfate and/or hydrogensulfate, a diamond layer, which is arranged on a conductive carrier and is made conductive by doping using a trivalent or pentavalent element, is used as an anode, and the accelerators are not added to an anolyte.

    Abstract translation: 要解决的问题:提供一种能够完全消除促进剂的使用的过氧二硫酸铵和碱金属过硫酸氢盐的工业方法,并且在电解电流密度低时实施。解决方案:在生产方法的情况下 过氧二硫酸盐,例如过二硫酸铵,过二硫酸钠和过二硫酸钾,通过阳极氧化含有硫酸盐和/或硫酸氢盐的电解质,金刚石层,其布置在导电载体上并通过使用三价或五价元素掺杂而导电 ,用作阳极,并且加速剂不加入阳极电解液。

    METHOD FOR PREPARING PEROXODISULFATE

    公开(公告)号:JP2002004073A

    公开(公告)日:2002-01-09

    申请号:JP2001119889

    申请日:2001-04-18

    Applicant: DEGUSSA

    Abstract: PROBLEM TO BE SOLVED: To provide an industrial method for preparing ammonium peroxodisulfate and alkaline metal peroxodisulfate which is capable of completely omitting the use of accelerators and is implemented when an electrolysis is of low current density. SOLUTION: In the case of the method for preparing the peroxodisulfate, for example, ammonium peroxodisulfate, sodium peroxodisulfate and potassium peroxodisulfate by anodically oxidizing an electrolyte containing sulfate and/or hydrogensulfate, a diamond layer which is arranged on a conductive carrier and is made conductive by doping using a tervalent or pentavalent element is used as an anode and the accelerators are not added to an anolyte.

    ELECTROLYTIC BATH FOR REMOVING ELECTROCHEMICALLY CONVERTIBLE IMPURITY FROM GAS AND METHOD

    公开(公告)号:JPH1028833A

    公开(公告)日:1998-02-03

    申请号:JP8897197

    申请日:1997-04-08

    Applicant: DEGUSSA

    Abstract: PROBLEM TO BE SOLVED: To ellectrochemically purify gas using a simple electrtolytic bath by making a counter electrode a gas diffusion electrode and installing a chamber having a gas supplying device and a gas discharging device on the opposite side of a fixed bed electrode of the counter electrode. SOLUTION: Gas to be purified and liquid electrolyte are led in a counter current or parallel current through the fixed bed electrode 10 of an electrolytic bath 1, and impurities are reacted at effective elctrolytic bath voltage, and electrochemically convertible impurities are removed electrolytically from gas. The electrolytic bath 1 is composed of the fixed electrode 10, a counter electrode 2 separated from the electrode 10 by a separator 4, liquid electrolyte supplying and discharging devices 17, 18, a raw gas inlet 19, a raw gas outlet 20, and a chamber 6 having a gas supplying and discharging devices 7, 8 to be attached to the counter electrode 2. The fixed electrode 10 is used as a dropping bed, raw gas is introduced from the inlet 19, electrolyte is introduced from the device 17 to be contacted in a parallel current or a counter current. In this process, hydrogen is supplied to a gas diffusion electrode 2 during reductive purification, while oxygen is supplied during oxidative purification.

    9.
    发明专利
    未知

    公开(公告)号:DE3603986A1

    公开(公告)日:1987-08-13

    申请号:DE3603986

    申请日:1986-02-08

    Applicant: DEGUSSA

    Abstract: 1. A process for working up the solution - remaining after separation of the enzyme - from the enzymatic racemate resolution of an N-acetyl-DL-amino-carboxylic acid in the presence of an L-amino acid acylase by electrodialysis, characterized in that the electrodialysis unit used consists of a plurality of 3-chamber packs of which each in turn consists of a feed and diluate chamber (1), a concentrate chamber (2) on the cathode side and a concentrate chamber (3) on the anode side, each 3-chamber pack being separated from each of the two adjacent packs by a device (4) in which water is split into OH-ions and H+ ions and in that, on completion of electrodialysis, an aqueous solution of the L-amino acid and at most 50% of the anions originally present in the form of their salts is run off from the diluate chambers (1), an aqueous solution of the cations originally present in the form of hydroxides is run off from the concentrate chambers (2) on the cathode side and an aqueous solution of N-acetyl-D(L)-amino acid and acetic acid in the form of the free acids is run off from the concentrate chambers (3) on the anode side.

    10.
    发明专利
    未知

    公开(公告)号:ES2187108T3

    公开(公告)日:2003-05-16

    申请号:ES99117862

    申请日:1999-09-10

    Applicant: DEGUSSA

    Abstract: An electrolysis cell has filled liquid electrolyte and oxidizing or reducing gas compartments, separated by a gas diffusion electrode on which an ion exchanging separator is formed (on the electrolyte side) by single- or multi-stage application of a solution of an ion exchanger material in a solvent, with at least partial evaporation of the solvent after each coating stage. An electrolysis cell for carrying out chemical reactions includes a liquid electrolyte compartment and an oxidizing or reducing gas compartment, having inlet and outlet lines for electrolyte and gas respectively. The two compartments each contain electrically conductive filler and are separated by a gas diffusion electrode (GDE), combined with an ion exchanging separator (IES) on the electrolyte side. A current collector for the GDE is provided. The filler in the electrolyte compartment serves as counter-electrode. The novel feature is that IES is applied to GDE by single- or multi-stage coating of the electro-catalytic layer of GDE with a solution of an ion exchanger material in a solvent, with at least partial evaporation of the solvent after each coating stage.

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