Droplet operations device
US-2016370317-A9 · Dec 22, 2016 · US
US2021285427A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2021285427-A1 |
| Application number | US-202117332063-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 27, 2021 |
| Priority date | Dec 19, 2018 |
| Publication date | Sep 16, 2021 |
| Grant date | — |
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An electrochemical hydrogen pump includes an electrolyte membrane, an anode on a first primary surface of the electrolyte membrane, a cathode on a second primary surface of the electrolyte membrane, and an anode separator on the anode. The anode includes an anode catalyst layer on the first primary surface of the electrolyte membrane and an anode gas diffusion layer on the anode catalyst layer. The anode gas diffusion layer includes a porous carbon sheet that is a powder molded body.
Opening claim text (preview).
What is claimed is: 1 . An electrochemical hydrogen pump comprising: an electrolyte membrane; an anode on a first primary surface of the electrolyte membrane; a cathode on a second primary surface of the electrolyte membrane; and an anode separator on the anode, wherein the anode includes an anode catalyst layer on the first primary surface of the electrolyte membrane and an anode gas diffusion layer on the anode catalyst layer, and the anode gas diffusion layer includes a porous carbon sheet that is a powder molded body. 2 . An electrochemical hydrogen pump comprising: an electrolyte membrane; an anode on a first primary surface of the electrolyte membrane; a cathode on a second primary surface of the electrolyte membrane; and an anode separator on the anode, wherein the anode includes an anode catalyst layer on the first primary surface of the electrolyte membrane and an anode gas diffusion layer on the anode catalyst layer, the anode gas diffusion layer includes a porous carbon sheet whose first surface layer, which is closer to the anode separator, contains amorphous carbon, and wherein the porous carbon sheet is analyzed by Raman spectroscopy, D/G>1.0. 3 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet has a Young's modulus in a direction of thickness higher than or equal to 2.5 GPa at least in a first surface layer, which is closer to the anode separator, thereof. 4 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet has a Young's modulus in a direction of thickness higher than or equal to 7.8 GPa at least in a first surface layer, which is closer to the anode separator, thereof. 5 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet has a flexural strength higher than or equal to 10 MPa at least in a first surface layer, which is closer to the anode separator, thereof. 6 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet has a flexural strength higher than or equal to 20 MPa at least in a first surface layer, which is closer to the anode separator, thereof. 7 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet has a porosity lower than or equal to 45% at least in a first surface layer, which is closer to the anode separator, thereof. 8 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet has a porosity lower than or equal to 39% at least in a first surface layer, which is closer to the anode separator, thereof. 9 . The electrochemical hydrogen pump according to claim 7 , wherein the porous carbon sheet has a porosity lower than or equal to 45% in a second surface layer, which is closer to the anode catalyst layer, thereof. 10 . The electrochemical hydrogen pump according to claim 8 , wherein the porous carbon sheet has a porosity lower than or equal to 39% in a second surface layer, which is closer to the anode catalyst layer, thereof. 11 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet has higher rigidity in a first surface layer, which is closer to the anode separator, thereof than in a layer lying under the first surface layer. 12 . The electrochemical hydrogen pump according to claim 11 , wherein the porous carbon sheet has higher rigidity in a second surface layer, which is closer to the anode catalyst layer, thereof than in a layer lying under the second surface layer. 13 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet has a lower porosity in a first surface layer, which is closer to the anode separator, thereof than in a layer lying under the first surface layer. 14 . The electrochemical hydrogen pump according to claim 13 , wherein the porous carbon sheet has a lower porosity in a second surface layer, which is closer to the anode catalyst layer, thereof than in a layer lying under the second surface layer. 15 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet has a peak pore diameter smaller than a thickness of the electrolyte membrane. 16 . The electrochemical hydrogen pump according to claim 1 , wherein the porous carbon sheet has an overall porosity higher than or equal to 20%. 17 . The electrochemical hydrogen pump according to claim 1 , wherein a second surface layer, which is closer to the anode catalyst layer, of the anode gas diffusion layer is water-repellent. 18 . The electrochemical hydrogen pump according to claim 1 , wherein a first surface layer, which is closer to the anode separator, of the anode gas diffusion layer is hydrophilic.
characterised by shape or form · CPC title
Carbon · CPC title
Electrodes comprising one or more electrocatalytic coatings on a substrate · CPC title
Gas diffusion electrodes · CPC title
having diaphragms · CPC title
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