1.
    发明专利
    未知

    公开(公告)号:DE59903382D1

    公开(公告)日:2002-12-19

    申请号:DE59903382

    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.

    2.
    发明专利
    未知

    公开(公告)号:DE50106427D1

    公开(公告)日:2005-07-14

    申请号:DE50106427

    申请日:2001-04-14

    Applicant: DEGUSSA

    Abstract: Production of ammonium-, Na- or K-peroxodisulfate involves anodic oxidation of an aqueous electrolyte containing the corresponding sulfate and/or hydrogen sulfate in an electrolytic cell with analyte and catholyte chambers with a separator or a gas diffusion cathode. The anode comprises an electrically-conductive carrier with a diamond layer made conductive by doping with a tri- or penta-valent element. The analyte has no added promoter.

    4.
    发明专利
    未知

    公开(公告)号:DE59702074D1

    公开(公告)日:2000-08-31

    申请号:DE59702074

    申请日:1997-03-06

    Applicant: DEGUSSA

    Abstract: The cell removes a pollutant from gases, converting it by electrolytic action. It comprises a solid bed electrode (10) and complementary electrode (2), with an intervening separator (4). There is a system supplying (17) and distributing (15) a fluid electrolyte onto the solid bed electrode, which is collected (14) and flows away (18). An inlet and outlet (19, 20) are included for the gas. The complementary electrode is a gas diffusion electrode and on the side away from the bed, there is a chamber (6) with connections (7, 8) for gas flow. Also claimed is the removal of a pollutant from gases. The gas to be cleaned flows in co- or counter current to the liquid electrolyte over the solid bed, converting the impurity with an effective cell potential. The cell is operated as an irrigated bed reactor. The bed is cathodic with an oxidisable gas supplied to the gas diffusion electrode, or anodic for a reducible gas.

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