High-temperature, low-temperature—gradient methods for (CO-)electrolysis of water (SOEC) or for producing electricity within a reactor or fuel-cell stack (SOFC) respectively
US-10480082-B2 · Nov 19, 2019 · US
US2016369412A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016369412-A1 |
| Application number | US-201414902376-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jul 15, 2014 |
| Priority date | Jul 17, 2013 |
| Publication date | Dec 22, 2016 |
| Grant date | — |
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The invention relates to an electrochemical cell partitioned by a cation-exchange membrane suitable for production of high purity hydrogen and oxygen by electrolysis of alkaline solutions comprising a cathode in form of porous web including a platinum or palladium catalyst. The cell can be used as an element of a modular filter-press electrolyser.
Opening claim text (preview).
1 . Electrolysis cell partitioned by a cation-exchange membrane into an anodic and a cathodic compartment each provided with means for feeding and for discharging an alkaline solution, said anodic compartment containing an anode suitable for oxygen evolution, said cathodic compartment containing a cathode suitable for hydrogen evolution comprising a porous web in intimate contact with said membrane through a catalytically-activated layer containing at least one noble metal selected between platinum and palladium. 2 . The cell according to claim 1 wherein said cathode suitable for hydrogen evolution comprises a second layer consisting of carbon or metal powders and polymer binders, adjacent said catalytically-activated layer on the side opposite the membrane and having less hydrophilic characteristics with respect to said catalytically-activated layer. 3 . The cell according to claim 1 wherein said cation-exchange membrane is a non-reinforced monolayer sulphonic membrane. 4 . The cell according to claim 1 wherein said cathode is put in electrical contact with said cathodic wall by means of a current collector consisting of a porous metal structure, optionally a nickel or steel foam. 5 . The cell according to claim 1 wherein said anode suitable for oxygen evolution is put in electrical contact with said anodic wall by means of a current collector consisting of a porous metal structure, optionally a nickel or steel foam or mat. 6 . The cell according to claim 1 wherein said anode suitable for oxygen evolution consists of a substrate made of a nickel or steel mesh or expanded or punched sheet, optionally activated with a catalytic coating, in direct contact with said membrane. 7 . Electrolyser of alkali solutions consisting of a modular arrangement of cells according to claim 1 , electrically connected through said anodic and cathodic walls according to a bipolar or monopolar configuration. 8 . Process of electrolysis in a cell according to claim 1 comprising the following simultaneous or sequential steps: feeding an electrolyte consisting of an alkali metal hydroxide solution to said anodic and cathodic compartments; connecting said cathodic compartment to the negative pole and said anodic compartment to the positive pole of a power unit, with subsequent supply of direct electrical current; carrying out cathodic evolution of hydrogen within said catalytically-activated layer and discharging said hydrogen from said cathodic compartment; carrying out evolution of oxygen on the surface of said anode. 9 . The process according to claim 8 wherein said electrolyte consists of an aqueous solution of caustic soda at 10 to 20% by weight concentration.
Hydrogen production from non-carbon containing sources, e.g. by water electrolysis · CPC title
Chemistry & Metallurgy · mapped topic
Chemistry & Metallurgy · mapped topic
Chemistry & Metallurgy · mapped topic
Chemistry & Metallurgy · mapped topic
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