Oxygen-enriched combustion for natural gas combined cycle operation
US-2024017204-A1 · Jan 18, 2024 · US
US2020340471A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2020340471-A1 |
| Application number | US-202016925371-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jul 10, 2020 |
| Priority date | Jan 24, 2019 |
| Publication date | Oct 29, 2020 |
| Grant date | — |
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An electrochemical hydrogen pump includes an electrolyte membrane, an anode catalyst layer in contact with one primary surface of the electrolyte membrane, a cathode catalyst layer in contact with the other primary surface of the electrolyte membrane, an anode gas diffusion layer in contact with the anode catalyst layer, a cathode gas diffusion layer in contact with the cathode catalyst layer, and a voltage applicator that applies a voltage between the anode catalyst layer and the cathode catalyst layer. Application of the voltage by the voltage applicator causes hydrogen in a hydrogen-containing gas supplied to above the anode catalyst layer to move above the cathode catalyst layer and to be pressurized. The anode gas diffusion layer includes a porous carbon sheet that has a smaller porosity in a first surface layer, which is on the anode catalyst layer side, than in the inside layer deeper than the first surface layer.
Opening claim text (preview).
What is claimed is: 1 . An electrochemical hydrogen pump comprising: an electrolyte membrane; an anode catalyst layer in contact with one primary surface of the electrolyte membrane; a cathode catalyst layer in contact with the other primary surface of the electrolyte membrane; an anode gas diffusion layer in contact with the anode catalyst layer; a cathode gas diffusion layer in contact with the cathode catalyst layer; and a voltage applicator that applies a voltage between the anode catalyst layer and the cathode catalyst layer, wherein: the electrochemical hydrogen pump is configured to, through application of the voltage by the voltage applicator, cause hydrogen in a hydrogen-containing gas supplied to above the anode catalyst layer to move above the cathode catalyst layer and to be pressurized, and the anode gas diffusion layer includes a porous carbon sheet that has a smaller porosity in a first surface layer, which is on an anode catalyst layer side, than in an inside layer deeper than the first surface layer. 2 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet has a higher density in the first surface layer than in the inside layer deeper than the first surface layer. 3 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet has a higher density in a second surface layer, opposite the first surface layer, than in an inside layer deeper than the second surface layer. 4 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet has a smaller carbon particle diameter in the first surface layer than in the inside layer deeper than the first surface layer. 5 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet has a smaller carbon particle diameter in a second surface layer, opposite the first surface layer, than in an inside layer deeper than the second surface layer. 6 . The electrochemical hydrogen pump according to claim 1 , wherein the first surface layer of the porous carbon sheet has a peak pore diameter smaller than a thickness of the electrolyte membrane. 7 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet has a porosity of 20% or more in the first surface layer. 8 . The electrochemical hydrogen pump according to claim 7 , wherein the porous carbon sheet has a porosity of 20% or more in a second surface layer, opposite the first surface layer. 9 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet has a porosity of 45% or less in the first surface layer. 10 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet has a porosity of 39% or less in the first surface layer. 11 . The electrochemical hydrogen pump according to claim 9 , wherein the porous carbon sheet has a porosity of 45% or less in a second surface layer, opposite the first surface layer. 12 . The electrochemical hydrogen pump according to claim 10 , wherein the porous carbon sheet has a porosity of 39% or less a second surface layer, opposite the first surface layer. 13 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet contains a water-repellent layer in the first surface layer. 14 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet contains a water-repellent layer on the first surface layer. 15 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet contains a water-retaining layer in a second surface layer, opposite the first surface layer. 16 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet contains a water-retaining layer on a second surface layer, opposite the first surface layer.
comprising ion-exchange membranes in or on which electrode material is embedded · CPC title
in electrochemical cells · CPC title
Carbon · CPC title
Gas diffusion electrodes · CPC title
Pressure cells · CPC title
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