Structural design of an electrochemical cell

Patent metadata

Field	Value
Publication number	US-2025019842-A1
Application number	US-202218711089-A
Country	US
Kind code	A1
Filing date	Nov 9, 2022
Priority date	Nov 16, 2021
Publication date	Jan 16, 2025
Grant date	—

Abstract

The present invention relates to an electrochemical cell ( 0 ) comprising an anode ( 1 ), a cathode ( 2 ) and an anion-conducting membrane ( 3 ) located between the anode ( 1 ) and the cathode ( 2 ). The invention also relates to the use of the cell ( 0 ) in a method for preparing hydrogen (H 2 ) and oxygen (O 2 ) by electrochemically splitting water (H 2 O). Moreover, the invention relates to an electrolyser ( 6, 8 ) comprising a multiplicity of the cells ( 0 ), and to a method for producing the electrolyser ( 6, 8 ). The aim of the invention is to provide an electrochemical cell ( 0 ) by means of which anion-exchange-membrane-based water splitting can be carried out on an industrial scale. The aim is also for the cell to be inexpensive in terms of production and to allow for the energy-efficient preparation of hydrogen and oxygen. The aim is achieved in that at least part of the anode is in the form of a first textile fabric comprising catalytically active textile line structures, and in that the first textile fabric directly contacts the membrane.

First claim

1 . An electrochemical cell comprising an anode, a cathode and an anion-conducting membrane disposed between anode and cathode, where the anode is at least partly executed as a first textile fabric comprising catalytically active linear textile structures, and in that the first textile fabric is in direct contact with the membrane, where the first textile fabric and is a felt or nonwoven, characterized in that the felt or nonwoven comprises at least two types of catalytically active linear textile structure, where one type has a higher catalytic activity than the other type, and in that the type of catalytically active linear textile structure having higher catalytic activity is concentrated in a region of the textile fabric more closely adjoining the membrane than a region of the textile fabric in which the type of catalytically active linear textile structure having lower catalytic activity is concentrated.

2 . The electrochemical cell according to claim 1 , wherein the catalytically active linear textile structures consist of a nickel-containing material.

3 . The electrochemical cell according to claim 2 , wherein the nickel-containing material is selected from the group consisting of the following materials: nickel, nickel-containing alloys, especially Hastelloy, Chronin, Monel, Inconel, Incoloy, Invar, Kovar; steel containing nickel, stainless steel containing nickel, steel of steel types AISI 301, AISI 301L, AISI 302, AISI 304, AISI 304L, AISI 310, AIS1310L, AIS1316, AISI 316L, AISI 317, AISI 317L, AISI 321.

4 . The electrochemical cell according to claim 1 , wherein the catalytically active linear textile structures comprise a substrate provided with a catalytically active coating, where the catalytically active coating contains at least one element selected from the group consisting of Au, Pt, Ir, Rh, Ru, Pd, Ag, Ni, Co, Cu, Fe, Mn, Mo, or a compound, especially an oxide, mixed oxide, hydroxide, mixed hydroxide, spinel or perovskite, of the selected element.

5 . The electrochemical cell according to claim 4 , wherein the catalytically active coating is free of polymers, especially free of an ion-conducting polymer.

6 . The electrochemical cell according to claim 4 , wherein the substrate material is selected from the group consisting of the following materials: nickel, nickel-containing alloys, especially Hastelloy, Chronin, Monel, Inconel, Incoloy, Invar, Kovar; steel containing nickel, stainless steel containing nickel, steel of steel types AISI 301, AISI 301L, AISI 302, AISI 304, AISI 304L, AISI 310, AIS1310L, AIS1316, AISI 316L, AISI 317, AISI 317L, AISI 321; titanium, carbon.

7 . The electrochemical cell according to claim 1 , wherein the cathode is at least partly executed as a second textile fabric.

8 . The electrochemical cell according to claim 7 , wherein the second textile fabric comprises catalytically active linear textile structures.

9 . The electrochemical cell according to claim 8 , wherein the second textile fabric is in direct contact with the membrane.

10 . The electrochemical cell according to claim 7 , wherein a catalyst layer is disposed between the second textile fabric and the membrane.

11 . The electrochemical cell according to claim 1 , wherein the second textile fabric is a felt or nonwoven.

12 . The electrochemical cell according to claim 1 , wherein the felt or nonwoven is formed from at least two felt or nonwoven layers, where the fibres and/or filaments of the first layer differ with regard to their diameter from the fibres and/or filaments of the second layer, and where the layer having finer fibres and/or filaments is disposed closer to the membrane than the layer having coarser fibres and/or filaments.

13 . The electrochemical cell according to claim 10 , wherein the catalyst layer contains catalytically active particles and/or catalytically active coating, where the catalytically active particles and/or catalytically active coating contain(s) elements selected from the group consisting of the following elements: Au, Pt, Ru, Rh, Pd, Ag, C, S, Se, Ni, Mo, Mn, Co, Cu, Fe or compounds of the selected elements.

14 . The electrochemical cell according to claim 13 , wherein the catalytically active particles are embedded in an anion-conducting polymer.

15 . The electrochemical cell according to claim 14 , wherein the anion-conducting polymer is likewise present in the membrane.

16 . The electrochemical cell according to claim 1 , wherein the first textile fabric and/or the second textile fabric is at least electrically contacted, preferably electrically and mechanically contacted, with a bipolar plate on its side remote from the membrane.

17 . The electrochemical cell according to claim 16 , wherein the bipolar plate consists of a material selected from the group consisting of the following materials: nickel; nickel-containing alloys, especially Hastelloy, Chronin, Monel, Inconel, Incoloy, Invar, Kovar; steel containing nickel, stainless steel containing nickel, steel of steel types AISI 301, AISI 301L, AISI 302, AISI 304, AISI 304L, AISI 310, AIS1310L, AIS1316, AISI 316L, AISI 317, AISI 317L, AISI 321; nickel-plated steel, nickel-plated stainless steel, nickel-plated titanium, nickel-plated brass, carbon.

18 . The process for producing hydrogen and oxygen by electrochemical splitting of water, having the following steps:
providing at least one electrochemical cell according to claim 1 ; providing water or an aqueous electrolyte having a pH of 7 to 14; providing an electrical voltage source; soaking and permeating at least one textile fabric with water or aqueous electrolyte; contacting anode and cathode with an electrical voltage drawn from the electrical voltage source; drawing off oxygen from the first textile fabric; drawing off hydrogen from the second textile fabric.

19 . The process according to claim 18 , having the following steps:
a) passing water or electrolyte through the first textile fabric; b) passing water or electrolyte through the second textile fabric; c) drawing off water or electrolyte enriched with oxygen and/or gaseous oxygen from the first textile fabric; d) drawing off water or electrolyte enriched with hydrogen and/or gaseous hydrogen from the second textile fabric; e) optionally separating hydrogen from the hydrogen-enriched water or from the hydrogen-enriched electrolyte; f) optionally separating oxygen from the oxygen-enriched water or from the oxygen-enriched electrolyte.

20 . The process according to claim 18 , having the following steps:
a) passing water or electrolyte through the first textile fabric; b) drawing off gaseous hydrogen from the second textile fabric; c) drawing off water or electrolyte enriched with oxygen and/or gaseous oxygen from the first textile fabric; d) optionally separating oxygen from the oxygen-enriched water or from the oxygen-enriched electrolyte.

21 . The process according to claim 18 , having the following steps:
a) passing water or electrolyte through the second textile fabric; b) drawing off gaseous oxygen from the first textile fabric; c) drawing off water or electrolyte enriched with hydrogen and/or gaseous hydrogen from the second textile fabric; d) optionally separating hydrogen from the hydrogen-enriched water or from the hydrogen-enriched electrolyte.

22 . An electrolyser comprising at least two electrochemical cells according to claim 16 that share a common bipolar plate.

23 . A process for producing a

Assignees

• Evonik Operations Gmbh

Inventors

• Maljusch Artjom

Classifications

• C25B1/04 Primary

  by electrolysis of water · CPC title

• C25B11/031

  Porous electrodes · CPC title

• C25B11/061

  Metal or alloy · CPC title

• Y02E60/36

  Hydrogen production from non-carbon containing sources, e.g. by water electrolysis · CPC title

• C25B15/023

  Measuring, analysing or testing during electrolytic production · CPC title