US2020318247A1PendingUtilityA1
Method and Device for the Electrochemical Utilization of Carbon Dioxide
Est. expiryMay 31, 2036(~9.8 yrs left)· nominal 20-yr term from priority
C25B 3/25C25B 9/23C25B 11/075C25B 11/031C25B 13/08C25B 1/00C25B 11/0447C25B 3/04C25B 11/035C25B 9/10
40
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Claims
Abstract
Various embodiments may include an electrolyzer for electrochemical utilization of carbon dioxide comprising: an electrolysis cell defining an anode space and a cathode space; an anode; a cathode; a first cation-permeable membrane disposed between the anode space and the cathode space; and a layer comprising an anion-selective polymer disposed between the first membrane and the cathode. The anode directly adjoins the first cation-permeable membrane and the layer covers at least part of the cathode but not all of the cathode.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . An electrolyzer for electrochemical utilization of carbon dioxide, the electrolyzer comprising:
an electrolysis cell defining an anode space and a cathode space; an anode in the anode space; a cathode in the cathode space; a first cation-permeable membrane disposed between the anode space and the cathode space; wherein the anode directly adjoins the first cation-permeable membrane; and a layer comprising an anion-selective polymer disposed between the first cation-permeable membrane and the cathode; wherein the layer covers at least part of the cathode but not all of the cathode.
2 . The electrolyzer as claimed in claim 1 , wherein the layer covers a surface area of the first membrane within a range from 20% to 85%.
3 . The electrolyzer as claimed in claim 1 , wherein the cathode comprises at least one element selected from the group consisting of: silver, copper, lead, indium, tin, and zinc.
4 . The electrolyzer as claimed in claim 1 , wherein the cathode comprises a gas diffusion electrode.
5 . A method of operating an electrolyzer for electrochemical utilization of carbon dioxide, the method comprising:
decomposing carbon dioxide at a cathode disposed in a cathode space of an electrolysis cell; forming at least one of carbonate and hydrogencarbonate from unconverted carbon dioxide and hydroxide ions at the cathode; transporting hydrogen ions from an anode disposed in an anode space of the electrolysis cell through a first cation-permeable membrane disposed between the anode space and the cathode space; wherein the anode directly adjoins the first cation-permeable membrane and a layer comprising an anion-selective polymer is disposed between the first cation-permeable membrane and the cathode; reacting the hydrogen ions and the at least one of carbonate or hydrogencarbonate to produce carbon dioxide and water in a contact region of the layer and the first cation-permeable membrane; and releasing the carbon dioxide through flow channels and/or pores in the layer.
6 . The method as claimed in claim 5 , wherein the electrolyzer is operated with pure water.
7 . The method as claimed in claim 5 , further comprising producing at least one of carbon monoxide, ethylene, or formic acid.
8 . (canceled)Join the waitlist — get patent alerts
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