Divided Electrochemical Cell and Low Cost High Purity Hydride Gas Production Process
US-2015345037-A1 · Dec 3, 2015 · US
US2023122705A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2023122705-A1 |
| Application number | US-202218065654-A |
| Country | US |
| Kind code | A1 |
| Filing date | Dec 14, 2022 |
| Priority date | Jul 14, 2020 |
| Publication date | Apr 20, 2023 |
| Grant date | — |
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A hydrogen system includes: a compressor including at least one cell that includes an electrolyte membrane, an anode catalyst layer provided on one principal surface of the electrolyte membrane, a cathode catalyst layer provided on another principal surface of the electrolyte membrane, an anode gas diffusion layer provided on the anode catalyst layer and including a porous sheet containing a metal, and a cathode gas diffusion layer provided on the cathode catalyst layer, and a voltage applicator that apples a voltage between the anode catalyst layer and the cathode catalyst layer, wherein the compressor that generates compressed hydrogen by causing the voltage applicator to apply the voltage to move hydrogen in hydrogen-containing gas supplied to an anode to the cathode via the electrolyte membrane; and a controller that causes the voltage applicator to apply the voltage after shutdown or at startup.
Opening claim text (preview).
What is claimed is: 1 . A hydrogen system comprising: a compressor including at least one cell that includes an electrolyte membrane, an anode catalyst layer provided on one principal surface of the electrolyte membrane, a cathode catalyst layer provided on another principal surface of the electrolyte membrane, an anode gas diffusion layer provided on the anode catalyst layer and including a porous sheet containing a metal, and a cathode gas diffusion layer provided on the cathode catalyst layer, and a voltage applicator that apples a voltage between the anode catalyst layer and the cathode catalyst layer, wherein the compressor that generates compressed hydrogen by causing the voltage applicator to apply the voltage to move hydrogen in hydrogen-containing gas supplied to an anode to the cathode via the electrolyte membrane; and a controller that causes the voltage applicator to apply the voltage after shutdown or at startup. 2 . The hydrogen system according to claim 1 , wherein the controller causes the voltage applicator to apply the voltage after supply of the hydrogen-containing gas to the anode is stopped. 3 . The hydrogen system according to claim 1 , wherein the controller causes the voltage applicator to apply the voltage after a cathode off gas is discharged from the cathode to a discharge destination different from a hydrogen demanding unit. 4 . The hydrogen system according to claim 1 , wherein the metal includes titanium. 5 . The hydrogen system according to claim 1 , wherein after the shutdown, the controller causes the voltage applicator to apply the voltage smaller than a maximum voltage to be applied during operation. 6 . The hydrogen system according to claim 1 , wherein after the shutdown, the controller causes the voltage applicator to apply the voltage smaller than a voltage applied when a cathode pressure reaches a supply pressure of compressed hydrogen to a hydrogen demanding unit. 7 . The hydrogen system according to claim 1 , further comprising: a flow regulator that regulates a flow rate of the hydrogen-containing gas supplied to the anode, wherein when the controller causes the voltage applicator to apply the voltage after the shutdown, the controller controls the flow regulator such that the hydrogen-containing gas is supplied to the anode at a flow rate smaller than a flow rate of the hydrogen-containing gas supplied to the anode during operation. 8 . The hydrogen system according to claim 1 , comprising: a flow regulator that regulates a flow rate of the hydrogen-containing gas supplied to the anode, wherein when the controller causes the voltage applicator to apply the voltage after the shutdown, the controller controls the flow regulator and does not supply the hydrogen-containing gas to the anode. 9 . The hydrogen system according to claim 1 , wherein after the shutdown, the controller causes the voltage applicator to apply the voltage necessary for moving, from the anode to the cathode, hydrogen of an amount which corresponds to an amount of hydrogen returning from the cathode to the anode via the electrolyte membrane. 10 . The hydrogen system according to claim 1 , further comprising a first flow channel for supplying to the anode a cathode off gas discharged from the cathode of the compressor, a first on-off valve provided in the first flow channel, a second flow channel through which an anode off gas discharged from the anode of the compressor flows, and a second on-off valve provided in the second flow channel, wherein before or while the controller causes the voltage applicator to apply a voltage after the shutdown, the controller opens the first on-off valve and closes the second on-off valve. 11 . The hydrogen system according to claim 1 , wherein after the shutdown, the controller causes the voltage applicator to apply the voltage smaller than or equal to ⅒ of a maximum voltage to be applied during operation. 12 . The hydrogen system according to claim 1 , wherein after the shutdown, the controller causes the voltage applicator to apply the voltage lower than or equal to 0.1 V per the one cell. 13 . The hydrogen system according to claim 1 , wherein a voltage applied by the voltage applicator after the shutdown is a voltage necessary for increasing to 0 V or higher an anode potential of the compressor that is assumed when no voltage is applied by the voltage applicator after the shutdown. 14 . The hydrogen system according to claim 1 , wherein the controller causes the voltage applicator to apply the voltage when no hydrogen-containing gas is supplied to the anode at the startup. 15 . The hydrogen system according to claim 1 , wherein when the hydrogen-containing gas is supplied to the anode at the startup, the controller causes the voltage applicator to apply the voltage when a potential of the anode is greater than a predetermined potential at which metal ions contained in the anode gas diffusion layer elute, or the controller causes the voltage applicator to apply the voltage within a predetermined period of time after the potential of the anode falls below the predetermined potential. 16 . The hydrogen system according to claim 1 , wherein the metal includes titanium. 17 . The hydrogen system according to claim 1 , wherein the cathode is filled with nitrogen or air before the voltage is applied by the voltage applicator. 18 . The hydrogen system according to claim 15 , wherein when a humidified hydrogen-containing gas is supplied to the anode at the startup, the controller controls the voltage applicator such that a density of current flowing through the cell is maintained at or below a first threshold which is smaller than an intended current density during a compressing operation, and such that a pressure of the cathode is maintained at or below a second threshold which is smaller than an intended pressure during the compressing operation. 19 . The hydrogen system according to claim 18 , wherein when a voltage applied by the voltage applicator to maintain the density of the current flowing through the cell at or below the first threshold and the pressure of the cathode at or below the second threshold decreases, the controller increases the voltage applied by the voltage applicator such that at least one of the density of the current flowing through the cell or the pressure of the cathode increases. 20 . A method of operating a hydrogen system comprising: generating compressed hydrogen by applying a voltage between an anode and a cathode to move hydrogen in hydrogen-containing gas supplied to the anode to the cathode, which includes an anode gas diffusion layer including a porous sheet containing a metal, and the cathode, the anode and the cathode being provided with an electrolyte membrane interposed therebetween; and applying a voltage between the anode and the cathode after shutdown or at startup. 21 . The method of operating a hydrogen system according to claim 20 , wherein the voltage is applied between the anode and the cathode after supply of the hydrogen-containing gas to the anode is stopped. 22 . The method of operating a hydrogen system according to claim 20 , wherein the voltage is applied between the anode and the cathode after a cathode off gas is discharged from the cathode to a discharge destination which is different from a hydrogen demanding unit. 23 . The method of operating a hydrogen system according to claim 20 , wherein the voltage is ap
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