US2019271089A1PendingUtilityA1
Metal hollow fiber electrode
Est. expiryNov 24, 2035(~9.4 yrs left)· nominal 20-yr term from priority
C25B 1/00C25B 11/02C25B 3/04C25B 11/0415C25B 11/035C25B 11/0447C25B 11/032C25B 3/03C25B 3/26C25B 3/07C25B 1/23C25B 11/057C25B 11/075C25B 3/25C25B 11/031
33
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Claims
Abstract
The invention is directed to a metal hollow fiber electrode, to a method of electrolyzing carbon dioxide in an aqueous electrochemical cell, to a method of converting carbon dioxide, to a method of preparing a metal hollow fiber, to a use of a metal hollow fiber electrode. The metal hollow fiber electrode comprises aggregated copper particles forming an interconnected three-dimensional porous structure, wherein said metal comprises copper.
Claims
exact text as granted — not AI-modified1 . A metal hollow fiber electrode, comprising aggregated copper particles forming an interconnected three-dimensional porous structure, wherein said metal comprises copper.
2 . The metal hollow fiber electrode according to claim 1 , wherein said metal is copper.
3 . The metal hollow fiber electrode according to claim 1 , wherein said fibers have an inner diameter of 0.1-10 mm.
4 - 5 . (canceled)
6 . The metal hollow fiber electrode according to claim 1 , wherein said fibers have an outer diameter of 0.1-10 mm.
7 - 8 . (canceled)
9 . The metal hollow fiber electrode according to claim 1 , wherein said fibers comprises or is composed of sintered copper particles.
10 . The metal hollow fiber electrode according to claim 1 , wherein said copper particles have an average particle diameter of 0.1-10 μm.
11 - 12 . (canceled)
13 . The metal hollow fiber electrode according to claim 1 , wherein a porous outer layer of the hollow fiber is more dense than a porous inner layer of the hollow fiber.
14 . The metal hollow fiber electrode according to claim 1 , wherein said outer layer has a thickness in the range of 5-20 μm.
15 - 16 . (canceled)
17 . A method of electrolyzing carbon dioxide in an aqueous electrochemical cell comprising an anode and a cathode, wherein the cathode comprises one or more metal hollow fiber electrodes according to claim 1 , said method comprising
applying a potential between said anode and cathode, and purging CO 2 or a gas mixture comprising CO 2 through the wall of the metal hollow fiber electrode.
18 . The method according to claim 17 , wherein said method is performed in an aqueous environment.
19 . The method according to claim 17 , wherein said method is performed at a temperature in the range of 5-80° C.
20 - 21 . (canceled)
22 . A method of converting carbon dioxide into one or more selected from the group consisting of carbon monoxide, formic acid, a formate, methanol, acetaldehyde, methane, ethylene and ethane, comprising electrolyzing CO 2 by a method according to claim 17 .
23 . The method according to claim 22 , wherein carbon dioxide is converted into carbon monoxide.
24 . A method of preparing a metal hollow fiber electrode according to claim 1 , comprising
spinning a mixture comprising copper particles, polymer and solvent together with a bore liquid to obtain hollow fibers; subjecting the hollow fibers to a thermal treatment such that copper particles are sintered together, thereby yielding hollow copper oxide fibers; hydrogenating the hollow copper oxide fibers.
25 . The method according to claim 24 , wherein said thermal treatment comprises subjecting the hollow fibers to a temperature of 500-800° C.
26 . (canceled)
27 . The method according to claim 24 , wherein the hollow fibers are subjected to said thermal treatment for a period of 1-6 hours.
28 . (canceled)
29 . The method according to claim 24 , wherein said hydrogenation comprises subjecting the hollow copper oxide fibers to a temperature of 200-400° C.
30 . (canceled)
31 . The method according to claim 24 , wherein the hollow copper oxide fibers are hydrogenated for a period of 30-120 minutes.
32 . (canceled)
33 . The method according to claim 24 , wherein the hollow copper oxide fibers are hydrogenated in a flow of hydrogen in the concentration range of 0-100 vol. %.
34 . The method according to claim 24 , wherein the hollow copper oxide fibers are hydrogenated in a flow of hydrogen in a concentration of 5 vol. % in a balance gas.
35 . (canceled)Cited by (0)
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