High-temperature, low-temperature-gradient methods for (co-)electrolysis of water (soec) or for producing electricity within a reactor or fuel-cell stack (sofc) respectively
US-2018237924-A1 · Aug 23, 2018 · US
US12098470B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12098470-B2 |
| Application number | US-202117165684-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 2, 2021 |
| Priority date | Mar 21, 2017 |
| Publication date | Sep 24, 2024 |
| Grant date | Sep 24, 2024 |
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An electrochemical reaction device comprises: an anode to oxidize water; an electrolytic solution flow path facing on the anode and through which an electrolytic solution containing the water flows; a cathode including: a porous conductive layer having first and second surfaces; and a reduction catalyst layer having a third surface disposed on the first surface and containing a reduction catalyst to reduce carbon dioxide; a separator between the anode and the cathode; a power supply connected to the anode and the cathode; and a flow path plate including: a fourth surface on the second surface; and a flow path facing on the second surface and through which the carbon dioxide flows. A ratio of an area of an overlap of the second surface and the flow path to an area of the second surface is 0.5 or more and 0.85 or less.
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What is claimed is: 1. An electrochemical reaction device, comprising: an anode configured to oxidize water and thus generate oxygen; an electrolytic solution flow path facing the anode and through which an electrolytic solution comprising water flows; a cathode comprising a porous conductive layer and a reduction catalyst layer, wherein the porous conductive layer has a first surface and a second surface, wherein the reduction catalyst layer has a third surface on the first surface and comprises a reduction catalyst, and wherein the reduction catalyst is configured to reduce carbon dioxide and thus generate a carbon compound; a separator between the anode and the cathode; and a metallic plate, wherein: the metallic plate comprises a first metallic layer having an inlet and an outlet; and a second metallic layer having a first metallic region, a second metallic region, and a flow path through which the carbon dioxide flows, wherein the first metallic region is spaced from the first metallic layer and has a fourth surface on the second surface, wherein the second metallic region bends from the first metallic region to the first metallic layer in a cross section perpendicular to the fourth surface of the second metallic layer, wherein the second metallic region is in contact with the first metallic layer, wherein the flow path is disposed between the second metallic region and the second surface, and wherein the second metallic region has a first opening connected to the inlet and a second opening connected to the outlet, and a ratio of an area of an overlap of the second surface and the flow path to an area of the second surface is from 0.66 to 0.815, an overlap of the second and fourth surfaces is divided along first lines and second lines except for the overlap of the second surface and the flow path, the first lines are away from each other along a first direction of the fourth surface at intervals of 0.1 mm, the second lines are away from each other along a second direction perpendicular to the first direction along the fourth surface at intervals of 0.1 mm, the first lines and the second lines cross each other to define intersection points, and a standard deviation of shortest distances between each of the intersection points and the overlap of the second surface and the flow path is 0.695 or less, the flow path comprises a first part, a second part and a third part, the first part extends along the fourth surface, the third part extends along the first part, and the second part extends and bends from the first part to the third part, and a ratio of an average width of the first part to an average width between the first and third parts is from 1.86 to 2.33. 2. The device according to claim 1 , wherein the second surface is divided into a polygonal portion and a remainder portion, wherein the polygonal portion is formed by connecting vertexes of the overlap of the second surface and the flow path, wherein each of interior angles of the overlap corresponding to the vertexes is less than 180 degrees, and a ratio of an area of the remainder portion to the area of the second surface is ⅙ or less. 3. The device according to claim 1 , wherein the standard deviation is 0.663 or less. 4. The device according to claim 1 , wherein an overlap of the second and fourth surfaces is divided along first lines and second lines except for the overlap of the second surface and the flow path, wherein the first lines are away from each other along the first direction at intervals of 0.1 mm, and the second lines are away from each other along the second direction at intervals of 0.1 mm, wherein the first lines and the second lines cross each other to define intersection points, and shortest distances between each of 30% or less of the intersection points in a number ratio and the overlap of the second surface and the flow path are at least 0.5 mm. 5. The device according to claim 1 , wherein a ratio of an area of an overlap of the third surface and the flow path to an area of the third surface is from 0.5 to 0.85. 6. The device according to claim 5 , wherein the second surface is divided into a polygonal portion and a remainder portion, wherein the polygonal portion is formed by connecting vertexes of the overlap of the third surface and the flow path, wherein each of interior angles of the overlap corresponding to the vertexes is less than 180 degrees, and a ratio of an area of the remainder portion to the area of the third surface is ⅙ or less. 7. The device according to claim 5 , wherein an overlap of the third and fourth surfaces is divided along third lines and fourth lines except for the overlap of the third surface and the flow path, wherein the third lines are away from each other along the first direction at intervals of 0.1 mm, and the fourth lines are away from each other along the second direction at intervals of 0.1 mm, wherein the third lines and the fourth lines cross each other to define intersection points, and a standard deviation of shortest distances between each of the intersection points and the overlap of the third surface and the flow path is 0.8 or less. 8. The device according to claim 5 , wherein an overlap of the third and fourth surfaces is divided along third lines and fourth lines except for the overlap of the third surface and the flow path, wherein the third lines are away from each other along the first direction at intervals of 0.1 mm, and the fourth lines are away from each other along the second direction at intervals of 0.1 mm, wherein the third lines and the fourth lines cross each other to define intersection points, and shortest distances between each of 30% or less of the intersection points in a number ratio and the overlap of the third surface and the flow path are at least 0.5 mm. 9. An electrochemical reaction device, comprising: a first anode configured to oxidize water and thus generate oxygen; a first cathode configured to reduce carbon dioxide and thus generate a carbon compound; a first separator between the first anode and the first cathode; a second anode configured to oxidize the water and thus generate the oxygen; a second cathode configured to reduce the carbon dioxide and thus generate the carbon compound; a second separator between the second anode and the second cathode; a first metallic layer having an inlet and an outlet; a second metallic layer disposed between the first cathode and the first metallic layer; and a third metallic layer disposed between the first anode and the second cathode, wherein: the first cathode comprises a porous conductive layer having a first surface and a second surface, and a reduction catalyst layer having a third surface on the first surface and containing a reduction catalyst, wherein the reduction catalyst is configured to reduce the carbon dioxide and thus generate the carbon compound; the second metallic layer comprises a first metallic region spaced from the first metallic layer and having a fourth surface on the second surface, a second metallic region bending from the first metallic region to the first metallic layer in a cross section perpendicular to the fourth surface of the second metallic layer, being in contact with the first metallic layer, and having a first opening connected to the inlet and a second opening connected to the outlet, a first flow path disposed between the first metallic region and the first metallic layer, and through which an electrolytic solution containing the water and the carbon dioxide flows, and a second flow path disposed between the second metallic region and the second surface, facing the second surface, and through which the electrolytic solution flows; the first metallic region has a third
Porous electrodes · CPC title
of the filter-press type · CPC title
comprising ion-exchange membranes in or on which electrode material is embedded · CPC title
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