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    • 1. 发明专利
    • COATING FOR METALLIC CELL ELEMENT MATERIALS OF AN ELECTROLYSIS CELL
    • CA2824173A1
    • 2012-07-19
    • CA2824173
    • 2011-11-29
    • THYSSENKRUPP UHDE GMBHBAYER IP GMBH
    • WOLTERING PETERKIEFER RANDOLFWEBER RAINERBULAN ANDREAS
    • C25B9/17
    • The invention relates to a cathode half-shell of an electrolytic cell, comprising metallic cell-element components, comprising ° a metallic support structure (2) welded to the rear wall of the cathode half shell (1), and at least one metallic spring element (4) arranged thereon in a plane-parallel manner, ° an oxygen-consuming cathode arranged on the at least one metallic spring element and comprising a perforated metallic carrier (5) and a catalyst strip (6), mechanically pressed thereonto, consisting of PTFE and silver oxide, the silver oxide being reduced in the electrolysis operation to obtain silver and therefore producing a uniform connection, characterised in that it is highly conductive, between the components of the oxygen-consuming cathode and the at least one spring element, at least one of the metallic components being provided with an electrically conductive coating comprising at least two layers, ° one first layer, which is applied directly to the cell-element materials, being selected from a group which contains Au, B-doped nickel, Ni-sulphide, and mixtures thereof, this first layer having a layer thickness of between 0.005 and 0.2 µm, and ° a second layer, applied to the first layer, consisting of silver and having a layer thickness of between 0.1 to 30 µm.
    • 2. 发明申请
    • ELECTROCHEMICAL CELL HAVING A FRAME SEAL FOR ALTERNATIVE SEALING AGAINST MARGINAL LEAKAGES OF THE ELECTROLYTE
    • 与盖章替代品密封RANDLÄUFIGKEITEN电解液电化学电池,
    • WO2012152367A3
    • 2013-04-25
    • PCT/EP2012001682
    • 2012-04-19
    • THYSSENKRUPP UHDE GMBHBAYER MATERIALSCIENCE AGKIEFER RANDOLFWOLTERING PETERWEBER RAINERBULAN ANDREASGROSSHOLZ MICHAEL
    • KIEFER RANDOLFWOLTERING PETERWEBER RAINERBULAN ANDREASGROSSHOLZ MICHAEL
    • C25B9/08C25B9/20
    • C25B9/08C25B9/20H01M8/0273H01M8/0276H01M8/04283H01M8/08H01M8/083H01M2008/1095
    • The invention relates to an electrochemical cell, comprising an anode half-shell (14) and a cathode half-shell (15) which are separated from one another by a membrane (8), having the corresponding electrodes, and the anode half-shell (14) and the cathode half-shell (15) each have an outer wall (12, 13), each outer wall having in the contact region of the two half-shells flange regions (16, 17) which are designed as a frame, and the flange regions (16 and 17) have assembly holes (4) which mark an inner region (23) and an outer region (24) of the electrochemical cell and a gas diffusion electrode (6) which rests on a support system (7), and a porous medium (9) which lies on the gas diffusion electrode (6), and devices for delivering and removing gas (18, 19) and electrolyte (20, 21). The invention is in particular characterised in that at least one peripheral frame seal (3) is provided in the contact region of the two half-shells between the frame-like flange regions (16 and 17) of the outer walls (12 and 13) of the two half-shells, and said seal lies on the membrane (8), wherein the porous medium (9) and the gas diffusion electrode (6) lie on the frame-like cathodic flange region (17) and in said region the peripheral frame seal (3) overlaps the porous medium (9) and the gas diffusion electrode (5), wherein said overlap region (2) has at least two profiled areas (1), wherein the peripheral frame seal has at least one further profiled area (22) in the contact region of the two half-shells between the frame-like flange regions (16 and 17) outside the overlap region of the porous medium (9) and the gas diffusion electrode (6) and/or at least one deformable sealing cord (5) is arranged, wherein the further profiled area (22) and/or the deformable sealing cord (5) is disposed in the inner region (23) of the electrochemical cell.
    • 本发明涉及一种电化学电池,包括阳极(14)和阴极半壳(15),它们彼此通过一个隔膜(8),其包括各自的电极分离,将阳极(14)和所述阴极半壳(15) 在每种情况下的外壁(12,13)分别具有在两个半壳的凸缘部分(16,17),这是框架状的结构的接触面积,和凸缘部(16和17)的安装孔(4),内部部分(23) 和电化学电池标记的外部区域(24)和一支撑系统(7)搁置在一个气体扩散电极(6),和(9)的多孔介质,其搁置在气体扩散电极(6) ,以及用于供给和气体(18,19)的放电和电解质(20,21)的装置。 更具体地,本发明的特征在于,至少一个周边框架的密封件(3)在两个半壳的外壁(12和13)的框状的凸缘部(16和17)之间的两个半壳的接触区域被设置在所述膜(8)搁 其中位于所述多孔介质(9),并且在框状的阴极凸缘部分(17)的气体扩散电极(6)和周边框架密封件(3)在这个区域与(9)的多孔介质和气体扩散 电极(6)重叠,所述重叠区域(2)具有至少两个配置文件(1),其中所述外围框架密封在多孔介质(9)和气体扩散的重叠区域以外的边框式凸缘部分(16和17)之间的两个半壳的接触区域 电极(6)具有至少一个附加的轮廓(22)和/或至少一个可变形密封件(5)线布置, 其中,所述另一轮廓(22)和/或在电化学电池的内部区域(23)的可变形的密封带(5)设置。
    • 3. 发明申请
    • ALTERNATIVE INSTALLATION OF A GAS DIFFUSION ELECTRODE IN AN ELECTROCHEMICAL CELL HAVING PERCOLATOR TECHNOLOGY
    • 气体扩散电极与PERCOLATORTECHNOLOGIE电化学电池备选团
    • WO2012139741A2
    • 2012-10-18
    • PCT/EP2012001533
    • 2012-04-07
    • THYSSENKRUPP UHDE GMBHBAYER MATERIALSCIENCE AGWOLTERING PETERKIEFER RANDOLFWEBER RAINERBULAN ANDREAS
    • WOLTERING PETERKIEFER RANDOLFWEBER RAINERBULAN ANDREAS
    • C25B9/02C25B9/08C25B9/18H01M4/86H01M8/0273H01M8/0276H01M8/028H01M8/1007H01M8/241H01M8/2483Y02E60/50
    • The invention relates to an electrochemical cell comprising an anode half shell (12) and a cathode half shell (11) which are separated from one another by means of a membrane (5) and having the corresponding electrodes, the anode half shell (12) and the cathode half shell (11), which each have an outer wall (13) and each have flange regions (14a, 14b, 15a, 15b) in the contact region of the two half shells, which flange regions are configured in the form of a frame, and a gas diffusion electrode (3) which consists of a liquid-permeable support which is coated with a catalyst material, where the gas diffusion electrode (3) has a region at its outer margin (17) which is not coated with catalyst and projects at the lower end of the electrochemical cell (16) in the contact region of the two half shells between the flange regions of the outer wall of the cathode half shell (15b) and the flange regions of the outer wall of the anode half shell (14b) and a porous medium (8) is arranged parallel between the gas diffusion electrode (3) and the membrane (5), and also facilities for the introduction and discharge of gas (20, 21) and electrolyte (9, 10), where a gas space (22) is separated from an electrolyte space (7) by appropriate means (23). In particular, the present invention is characterized in that profile internals (1), into which an upper margin (19) of the gas diffusion electrode (3) projects, on which a seal (2) which fixes the gas diffusion electrode (3) into the profile internals (1) is installed, are provided in the electrolyte space (7) in the cathode half shell (11), where the gas diffusion electrode (3) has a bending radius a of
    • 本发明涉及一种电化学电池,包括阳极(12)和阴极半壳体(11),它们彼此通过膜(5)包括在各电极分开,并且所述阳极(12)和所述阴极半壳(11) 每个具有外壁(13),并且每个在两个半壳的接触区域的凸缘部分(14A,14B,15A,15B),它们是框架状的结构,并且它由一个液体的气体扩散电极(3) 可透过的载体涂覆有催化剂材料,其中所述的气体扩散电极(3)在其下边缘(17)具有在所述两个半壳的接触区域的电化学电池(16)的下端部的非涂覆催化剂的区域 阴极半壳的所述外壁的所述凸缘部分(15B)和所述阳极半壳体(14B)和一个多孔介质(8)的对的外壁的凸缘部分之间延伸 帕RA LLE升插在气体扩散电极(3)和所述膜(5)之间,并且用于通过供给和去除气体(20,21)和电解质(9,10),其中的气体空间(22)的设备 电解质空间(7)通过相应的装置(23)被限定。 更具体地,本发明的特征在于在(7)在所述阴极半壳(11)轮廓的部件(1)提供的电解质的空间,到其中的气体扩散电极(3)的上边缘(19)延伸,在其上 所述密封件(2)被安装时,固定所述的气体扩散电极(3)在简档组件(1),其特征在于,气体扩散电极(3)具有弯曲半径的<90°相对于张紧天然气的垂直 具有扩散电极。
    • 5. 发明专利
    • ALTERNATIVE INSTALLATION OF A GAS DIFFUSION ELECTRODE IN AN ELECTROCHEMICAL CELL HAVING PERCOLATOR TECHNOLOGY
    • CA2833182A1
    • 2012-10-18
    • CA2833182
    • 2012-04-07
    • THYSSENKRUPP UHDE GMBHUHDENORA SPA
    • WOLTERING PETERKIEFER RANDOLFWEBER RAINERBULAN ANDREAS
    • C25B9/19
    • The invention relates to an electrochemical cell comprising an anode half shell (12) and a cathode half shell (11) which are separated from one another by means of a membrane (5) and having the corresponding electrodes, the anode half shell (12) and the cathode half shell (11), which each have an outer wall (13) and each have flange regions (14a, 14b, 15a, 15b) in the contact region of the two half shells, which flange regions are configured in the form of a frame, and a gas diffusion electrode (3) which consists of a liquid-permeable support which is coated with a catalyst material, where the gas diffusion electrode (3) has a region at its outer margin (17) which is not coated with catalyst and projects at the lower end of the electrochemical cell (16) in the contact region of the two half shells between the flange regions of the outer wall of the cathode half shell (15b) and the flange regions of the outer wall of the anode half shell (14b) and a porous medium (8) is arranged parallel between the gas diffusion electrode (3) and the membrane (5), and also facilities for the introduction and discharge of gas (20, 21) and electrolyte (9, 10), where a gas space (22) is separated from an electrolyte space (7) by appropriate means (23). In particular, the present invention is characterized in that profile internals (1), into which an upper margin (19) of the gas diffusion electrode (3) projects, on which a seal (2) which fixes the gas diffusion electrode (3) into the profile internals (1) is installed, are provided in the electrolyte space (7) in the cathode half shell (11), where the gas diffusion electrode (3) has a bending radius a of
    • 6. 发明专利
    • BR102012024229A2
    • 2013-08-06
    • BR102012024229
    • 2012-09-24
    • BAYER IP GMBHSTARCK H C GMBH
    • BULAN ANDREASWEBER RAINERALBRECHT SVENMEESE-MARKTSCHEFFEL JULIANEOBRICH ARMIN
    • C25B11/04C25B11/08
    • A silver oxide is precipitated at 20-80[deg] C by simultaneously adding an aqueous sodium-hydroxide solution and silver nitrate solution to receiver vessel, using a mechanical stirrer to introduce stirring energy of 0.01-10 W/l, and pH is maintained constant to 10-12. The precipitated silver oxide is removed from the suspension. The silver oxide is dried at 80-200[deg] C. The silver oxide is processed with an electroconductive carrier material to obtain a flat oxygen-consuming electrode. A silver oxide is precipitated at 20-80[deg] C by simultaneously adding an aqueous sodium-hydroxide solution and silver nitrate solution to receiver vessel, using a mechanical stirrer to introduce stirring energy of 0.01-10 W/l, and pH is maintained constant to 10-12. The precipitated silver oxide is removed from the suspension. The silver oxide is dried at 80-200[deg] C, optionally under reduced pressure and under inert gas atmosphere. The silver oxide is processed with an electroconductive carrier material, catalyst comprising silver particles, and finely-divided fluorinated polymer to obtain a flat oxygen-consuming electrode. An independent claim is included for electrolysis cell for electrolysis of alkali metal chloride, which comprises oxygen-consuming electrode as cathode.