Co2 electroreduction to multi-carbon products in strong acid
US-2024093390-A1 · Mar 21, 2024 · US
US11118274B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11118274-B2 |
| Application number | US-202016741038-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 13, 2020 |
| Priority date | Sep 8, 2014 |
| Publication date | Sep 14, 2021 |
| Grant date | Sep 14, 2021 |
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Described herein is a process for the reduction of carbon dioxide comprising: providing an electrochemical device comprising an anode, a cathode, and a polymeric anion exchange membrane therebetween, wherein the polymeric anion exchange membrane comprises an anion exchange polymer, wherein the anion exchange polymer comprises at least one positively charged group selected from a guanidinium, a guanidinium derivative, an N-alkyl conjugated heterocyclic cation, or combinations thereof; introducing a composition comprising carbon dioxide to the cathode; and applying electrical energy to the electrochemical device to effect electrochemical reduction of the carbon dioxide.
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What is claimed is: 1. A cathode membrane assembly for an electrolyzer, comprising a porous, electrically conductive substrate, at least one catalytically active element in electrical contact with the electrically conductive substrate, and an anion exchange polymer in contact with the at least one catalytically active element wherein the anion exchange polymer comprises at least one positively charged group selected from a guanidinium, a guanidinium analog, an N-alkyl conjugated heterocyclic cation, or combinations thereof. 2. The cathode membrane assembly of claim 1 , wherein the N-alkyl conjugated heterocyclic cation is selected from N,N′-disubstituted imidazoliums, 1,2,3-tri substituted imidazoliums, N-substituted pyridiniums, N-substituted isoquinoliniums, N-disubstituted pyrrolidiniums, or combinations thereof. 3. The cathode membrane assembly of claim 1 , wherein the anion exchange polymer is the reaction product of at least an alkyl-substituted vinyl imidazolium monomer. 4. The cathode membrane assembly of claim 1 , wherein the anion exchange polymer forms a polymeric anion exchange membrane layer that is porous. 5. The cathode membrane assembly of claim 1 , wherein the anion exchange polymer forms a polymeric anion exchange membrane layer that is dense. 6. The cathode membrane assembly of claim 1 , wherein the at least one catalytically active element is selected from V, Cr, Mn, Fe, Co, Ni, Cu, Sn, Zr, Nb, Mo, Ru, Rh, Pd, Ag, Cd, Hf, Ta, W, Re, Ir, Pt, Au, Hg, Al, Si, In, Tl, Pb, Bi, Sb, Te, U, Sm, Tb, La, Ce, Nd, and alloys or combinations thereof. 7. The cathode membrane assembly of claim 6 , wherein the at least one catalytically active element is selected from silver, gold, copper, or combinations thereof. 8. The cathode membrane assembly of claim 1 , wherein the porous, electrically conductive substrate comprises at least one of a carbon paper, carbon cloth, or a metal mesh. 9. A system for electrochemically reducing carbon dioxide comprising: (a) an electrochemical device comprising (i) an anode electrode, (ii) the cathode membrane assembly of claim 1 adjacent the anode electrode, and (iii) a cathode flow field adjacent to the cathode membrane assembly opposing the anode electrode; and (b) a carbon dioxide input, wherein the carbon dioxide input is configured to provide a composition comprising carbon dioxide to the cathode flow field for reduction of the carbon dioxide at the cathode electrode; and (c) an external energy source, wherein the negative terminal of the external energy source is connected to the cathode and the positive terminal of the external energy source is connected to the anode. 10. The system of claim 9 , further comprising a polymeric cation exchange membrane between the cathode membrane assembly and the anode electrode. 11. The system of claim 9 , wherein the cathode membrane assembly is substantially free of a liquid electrolyte. 12. The system of claim 9 , wherein the electrochemical cell is substantially free of a liquid electrolyte. 13. The system of claim 9 , further comprising a catalytically active extended surface area catalyst-based electrode such as a nanostructured thin film electrode, a coated nanotube electrode, a porous sponge electrode, or a two dimensional polycrystalline film electrode. 14. A process for the electrochemical reduction of carbon dioxide comprising: providing the system of claim 9 ; introducing a composition comprising carbon dioxide to the cathode membrane assembly; and applying electrical energy to the electrochemical device to effect electrochemical reduction of the carbon dioxide. 15. The process of claim 14 , wherein the cathode membrane assembly is substantially free of a liquid electrolyte. 16. The process of claim 14 , wherein water is introduced to the anode electrode as a reactant. 17. The process of claim 14 , wherein the cathode membrane assembly is operated at a potential equal to or more negative than −0.2 V with respect to a standard hydrogen electrode. 18. The process of claim 14 , wherein the process has a carbon monoxide selectivity of greater than 2%. 19. A process for producing hydrogen from water, comprising: a. providing the system of claim 9 ; b. introducing a composition comprising water to the anode electrode; and c. applying electrical energy to the electrochemical device to effect electrochemical splitting of water. 20. An electrolyzer, comprising: a cathode membrane, wherein the cathode membrane comprises a porous, electrically conductive substrate, at least one catalytically active element in electrical contact with the electrically conductive substrate, and an anion exchange polymer in contact with the at least one catalytically active element, and an anode, wherein the potential of the cathode membrane's catalytically active element in electrical contact with the electrically conductive substrate is more negative than the anode.
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