Soec stack with integrated heater
US-2015368818-A1 · Dec 24, 2015 · US
US9574274B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9574274-B2 |
| Application number | US-201514690687-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 20, 2015 |
| Priority date | Apr 21, 2014 |
| Publication date | Feb 21, 2017 |
| Grant date | Feb 21, 2017 |
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Methods for simultaneous syngas generation by opposite sides of a solid oxide co-electrolysis cell are provided. The method can comprise exposing a cathode side of the solid oxide co-electrolysis cell to a cathode-side feed stream; supplying electricity to the solid oxide co-electrolysis cell such that the cathode side produces a product stream comprising hydrogen gas and carbon monoxide gas while supplying oxygen ions to an anode side of the solid oxide co-electrolysis cell; and exposing the anode side of the solid oxide co-electrolysis cell to an anode-side feed stream. The cathode-side feed stream comprises water and carbon dioxide, and the anode-side feed stream comprises methane gas such that the methane gas reacts with the oxygen ions to produce hydrogen and carbon monoxide. The cathode-side feed stream can further comprise nitrogen, hydrogen, or a mixture thereof.
Opening claim text (preview).
What is claimed: 1. A method for simultaneous syngas generation by opposite sides of a solid oxide co-electrolysis cell, comprising: exposing a cathode side of the solid oxide co-electrolysis cell to a cathode-side feed stream, wherein the cathode-side feed stream comprises water and carbon dioxide; supplying electricity to the solid oxide co-electrolysis cell such that the cathode side produces a product stream comprising hydrogen gas and carbon monoxide gas while supplying oxygen ions to an anode side of the solid oxide co-electrolysis cell; and exposing the anode side of the solid oxide co-electrolysis cell to an anode-side feed stream, wherein the anode-side feed stream comprises methane gas such that the methane gas reacts with the oxygen ions to produce hydrogen and carbon monoxide. 2. The method of claim 1 , wherein the cathode-side feed stream further comprises nitrogen. 3. The method of claim 1 , wherein the cathode-side feed stream further comprises hydrogen. 4. The method of claim 1 , wherein the cathode-side feed stream further comprises hydrogen and nitrogen. 5. The method of claim 1 , further comprising: exposing the cathode-side feed stream to heat such that the cathode-side feed stream has a temperature of about 650° C. and about 1000° C. when exposed to the cathode side of the solid oxide co-electrolysis cell. 6. The method of claim 1 , wherein the cathode-side feed stream has a flow ratio of carbon dioxide to water such that the product stream produced by has a ratio of hydrogen to carbon monoxide from about 1:1 to about 4:1. 7. The method of claim 1 , wherein the cathode-side feed stream has a flow ratio of carbon dioxide to water such that the product stream produced by has a ratio of hydrogen to carbon monoxide that is about 2 to 1. 8. The method of claim 1 , wherein the methane gas and the electrolysis current in the anode produce a ratio of hydrogen and carbon monoxide of about 1:1 to about 4:1. 9. The method of claim 1 , wherein the methane gas and the electrolysis current in the anode produce a ratio of hydrogen and carbon monoxide of about 2 to 1. 10. The method of claim 1 , further comprising: operating the cathode as an anode. 11. The method of claim 1 , further comprising: operating the anode as a cathode.
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