Oxidation electrode and photoelectrochemical device
US-10100418-B2 · Oct 16, 2018 · US
US2018142365A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018142365-A1 |
| Application number | US-201715693475-A |
| Country | US |
| Kind code | A1 |
| Filing date | Sep 1, 2017 |
| Priority date | Nov 24, 2016 |
| Publication date | May 24, 2018 |
| Grant date | — |
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The present invention provides a method for reducing carbon dioxide electrochemically to generate ethylene selectively. In the present method, a carbon dioxide reduction catalyst comprising a crystalline copper phthalocyanine is used to generate ethylene selectively by reducing carbon dioxide electrochemically on a cathode electrode.
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1 . A method for reducing carbon dioxide electrochemically to generate ethylene selectively, the method comprising: (a) preparing an electrolysis device comprising: a cathode container; an anode container; a cathode electrode; an anode electrode; and a solid electrolysis membrane; wherein a first electrolysis solution is stored in the cathode container; the first electrolysis solution contains the carbon dioxide; a second electrolysis solution is stored in the anode container; the cathode electrode is in contact with the first electrolysis solution; the cathode electrode comprises a carbon dioxide reduction catalyst; the carbon dioxide reduction catalyst comprises a crystalline copper phthalocyanine; the anode electrode is in contact with the second electrolysis solution; and the cathode container and the anode container are separated from each other with the solid electrolysis membrane; and (b) applying a voltage to the cathode electrode and the anode electrode in such a manner that an electric potential of the cathode electrode is negative with regard to an electric potential of the anode electrode to generate ethylene selectively due to electrochemical reduction of the carbon dioxide on the cathode electrode. 2 . The method according to claim 1 , wherein at least a part of the crystalline copper phthalocyanine is α-type crystalline. 3 . The method according to claim 1 , wherein at least a part of the crystalline copper phthalocyanine is β-type crystalline. 4 . The method according to claim 1 , wherein at least a part of the crystalline copper phthalocyanine is a 1,2,3,4,8,9,10,11,15,16,17,18,22,23,24,25-hexadecafluorophthalocyanine copper crystal. 5 . The method according to claim 1 , wherein at least a part of the crystalline copper phthalocyanine is a 2,3,9,10,16,17,23,24-octafluorophthalocyanine copper crystal. 6 . The method according to claim 1 , wherein at least a part of the crystalline copper phthalocyanine is a 2,9,16,23-tetra-tert-butyl phthalocyanine copper crystal. 7 . The method according to claim 1 , wherein at least a part of the crystalline copper phthalocyanine is a 5,9,14,18,23,27,32,36-octabutoxy-2,3-naphthalocyanine copper crystal. 8 . An electrolysis device for generating ethylene selectively due to reduction of carbon dioxide electrochemically; the electrolysis device comprising: a cathode container; an anode container; a cathode electrode; an anode electrode; and a solid electrolysis membrane; wherein a first electrolysis solution is stored in the cathode container; the first electrolysis solution contains the carbon dioxide; a second electrolysis solution is stored in the anode container; the cathode electrode is in contact with the first electrolysis solution; the cathode electrode comprises a carbon dioxide reduction catalyst; the carbon dioxide reduction catalyst comprises a crystalline copper phthalocyanine; the anode electrode is in contact with the second electrolysis solution; and the cathode container and the anode container are separated from each other with the solid electrolysis membrane. 9 . The electrolysis device according to claim 8 , wherein at least a part of the crystalline copper phthalocyanine is α-type crystalline. 10 . The electrolysis device according to claim 8 , wherein at least a part of the crystalline copper phthalocyanine is β-type crystalline. 11 . The electrolysis device according to claim 8 , further comprising a reference electrode disposed in the cathode container, wherein the reference electrode is in contact with the first electrolysis solution; and the reference electrode has a region of silver/silver chloride. 12 . The electrolysis device according to claim 8 , wherein the anode electrode is formed of a material selected from the group consisting of carbon, platinum, gold, silver, copper, titanium, iridium oxide, and an alloy thereof. 13 . The electrolysis device according to claim 8 , wherein at least a part of the crystalline copper phthalocyanine is a 1,2,3,4,8,9,10,11,15,16,17,18,22,23,24,25-hexadecafluorophthalocyanine copper crystal. 14 . The electrolysis device according to claim 8 , wherein at least a part of the crystalline copper phthalocyanine is a 2,3,9,10,16,17,23,24-octafluorophthalocyanine copper crystal. 15 . The electrolysis device according to claim 8 , wherein at least a part of the crystalline copper phthalocyanine is a 2,9,16,23-tetra-tert-butyl phthalocyanine copper crystal. 16 . The electrolysis device according to claim 8 , wherein at least a part of the crystalline copper phthalocyanine is a 5,9,14,18,23,27,32,36-octabutoxy-2,3-naphthalocyanine copper crystal. 17 . A carbon dioxide reduction electrode capable of converting carbon dioxide into ethylene selectively by application of a voltage, comprising: crystalline copper phthalocyanine. 18 . The carbon dioxide reduction electrode according to claim 17 , wherein at least a part of the crystalline copper phthalocyanine is α-type crystalline. 19 . The carbon dioxide reduction electrode according to claim 17 , wherein at least a part of the crystalline copper phthalocyanine is β-type crystalline. 20 . The carbon dioxide reduction electrode according to claim 17 , wherein at least a part of the crystalline copper phthalocyanine is a 1,2,3,4,8,9,10,11,15,16,17,18,22,23,24,25-hexadecafluorophthalocyanine copper crystal. 21 . The carbon dioxide reduction electrode according to claim 17 , wherein at least a part of the crystalline copper phthalocyanine is a 2,3,9,10,16,17,23,24-octafluorophthalocyanine copper crystal. 22 . The carbon dioxide reduction electrode according to claim 17 , wherein at least a part of the crystalline copper phthalocyanine is a 2,9,16,23-tetra-tert-butyl phthalocyanine copper crystal. 23 . The carbon dioxide reduction electrode according to claim 17 , wherein at least a part of the crystalline copper phthalocyanine is a 5,9,14,18,23,27,32,36-octabutoxy-2,3-naphthalocyanine copper crystal. 24 . A carbon dioxide reduction catalyst comprising: crystalline copper phthalocyanine. 25 . The carbon dioxide reduction catalyst according to claim 24 , further comprising carbon black, wherein the crystalline copper phthalocyanine is mixed with the carbon black. 26 . The carbon dioxide reduction catalyst according to claim 24 , wherein at least a part of the crystalline copper phthalocyanine is α-type crystalline. 27 . The carbon dioxide reduction catalyst according to claim 24 , wherein at least a part of the crystalline copper phthalocyanine is β-type crystalline. 28 . The carbon dioxide reduction catalyst according to claim 24 , wherein at least a part of the crystalline copper phthalocyanine is a 1,2,3,4,8,9,10,11,15,16,17,18,22,23,24,25-hexadecafluorophthalocyanine copper crystal. 29 . The carbon dioxide reduction catalyst according to claim 24 , wherein at least a part of the crystalline copper phthalocyanine is a 2,3,9,10,16,17,23,24-octafluorophthalocyanine copper crystal. 30 . The carbon dioxide reduction catalyst according to claim 24 , wherein at least a part of the crystalline copper phthalocyanine is a 2,9,16,23-tetra-tert-butyl phthalocyanine copper crystal. 31 . The ca
Chemistry & Metallurgy · mapped topic
Crystalline forms, e.g. polymorphs · CPC title
Chemistry & Metallurgy · mapped topic
Chemistry & Metallurgy · mapped topic
Chemistry & Metallurgy · mapped topic
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