Integrated process for the sustainable and autonomous co2-emission-free production of hydrogen and related system
US-2024200017-A1 · Jun 20, 2024 · US
US2025361637A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2025361637-A1 |
| Application number | US-202218866566-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jul 15, 2022 |
| Priority date | Jul 15, 2022 |
| Publication date | Nov 27, 2025 |
| Grant date | — |
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A methane synthesis system according to the present disclosure includes: a co-electrolysis part that obtains hydrogen and carbon monoxide by electrolyzing water and carbon dioxide, a methanation reaction part that obtains a product gas containing methane by a methanation reaction that uses the hydrogen and the carbon monoxide, and a cooler having a distribution channel in which a refrigerant capable of phase transition, is distributed. The cooler cools the methanation reaction part using heat of vaporization from vaporizing at least a portion of the refrigerant on an inside of the distribution channel.
Opening claim text (preview).
What is claimed is: 1 . A methane synthesis system comprising: a co-electrolysis part that obtains hydrogen and carbon monoxide by electrolyzing water and carbon dioxide; a methanation reaction part that obtains a product gas containing methane by a methanation reaction that uses the hydrogen and the carbon monoxide; and a cooler having a distribution channel in which a refrigerant capable of phase transition, is distributed, wherein the cooler cools the methanation reaction part using heat of vaporization from vaporizing at least a portion of the refrigerant on an inside of the distribution channel, and lowers a temperature at an outlet of the methanation reaction part, more than a temperature at an inlet thereof. 2 . The methane synthesis system according to claim 1 , wherein the refrigerant is a fluid that contains water. 3 . The methane synthesis system according to claim 2 further comprising: a supply route that guides the refrigerant as the water, which passes through the cooler, to the co-electrolysis part. 4 . The methane synthesis system according to claim 3 , wherein an ejector that takes in the carbon dioxide, with the water as a working fluid, is provided on the supply route. 5 . The methane synthesis system according to claim 2 further comprising: a separator that separates water from the product gas, and a capture route that guides the water separated at the separator as the refrigerant to the cooler. 6 . The methane synthesis system according to claim 5 , wherein a heat exchanger is provided on the capture route, and heats the water by conducting heat exchange with oxygen produced by co-electrolysis of the water and the carbon dioxide at the co-electrolysis part. 7 . The methane synthesis system according to claim 1 further comprising: a separator that separates a fluid that contains the methane from the product gas, and a methane purifier that purifies the methane contained in the fluid, and obtains a purified product gas. 8 . The methane synthesis system according to claim 7 further comprising: a return route that returns a residual gas obtained from separating the purified product gas from the fluid that contains the methane, to the methanation reaction part.
Recycling of a stream within the process or apparatus to reuse elsewhere therein · CPC title
Applying an electric field or inclusion of electrodes in the apparatus · CPC title
Heat exchange, direct or indirect · CPC title
Production of synthetic natural gas · CPC title
the change of state being from liquid to vapour or vice versa · CPC title
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