Membrane electrode assembly for proton exchange membrane water electrolyzer and method of preparing membrane electrode assembly for proton exchange membrane water electrolyzer
US-2019071786-A1 · Mar 7, 2019 · US
US10975476B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10975476-B2 |
| Application number | US-201816198286-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 21, 2018 |
| Priority date | Nov 29, 2017 |
| Publication date | Apr 13, 2021 |
| Grant date | Apr 13, 2021 |
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The present disclosure relates to an IrO2 electrodeposited porous titanium composite layer of a polymer electrolyte membrane water electrolysis apparatus serving as both a diffusion layer and an oxygen electrode, the apparatus including: a porous titanium (Ti) layer; and an electrodeposited iridium oxide (IrO2) layer on the porous Ti layer. The IrO2 layer may be uniformly deposited on a porous Ti layer through an electrolysis process, and the electrodeposited IrO2 layer may play multiple roles as not only a catalyst layer toward oxygen evolution reaction (OER) on the surface of the Ti layer, but also a corrosion-protection layer which prevents an inner Ti layer from corrosion.
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What is claimed is: 1. An IrO 2 electrodeposited porous titanium composite layer of a polymer electrolyte membrane water electrolysis apparatus serving as both a diffusion layer and an oxygen electrode, the apparatus comprising: a porous titanium (Ti) layer; and an electrodeposited iridium oxide (IrO 2 ) layer on the porous Ti layer; wherein the porous Ti layer is in a form of titanium mesh having a porosity of 60% to 70%; wherein the electrodeposited IrO 2 layer comprises amorphous iridium oxide having a density of 7 to 9 g/cm 3 ; and wherein the electrodeposited IrO 2 layer has a thickness of 10 to 210 nm. 2. The composite layer of the polymer electrolyte membrane water electrolysis apparatus according to claim 1 , wherein the IrO 2 layer comprises iridium oxide loaded at 0.01 to 1.05 mg/cm 2 onto the porous Ti layer. 3. The composite layer of the polymer electrolyte membrane water electrolysis apparatus according to claim 1 , wherein the IrO 2 layer comprises iridium oxide loaded at 0.1 to 0.5 mg/cm 2 onto the porous Ti layer. 4. The composite layer of the polymer electrolyte membrane water electrolysis apparatus according to claim 1 , wherein the IrO 2 layer is uniformly deposited on the porous Ti layer, and thus physically blocks the porous Ti layer from the external oxidative environment. 5. A polymer electrolyte membrane water electrolysis apparatus comprising the composite layer of the polymer electrolyte membrane water electrolysis apparatus according to claim 1 . 6. The polymer electrolyte membrane water electrolysis apparatus according to claim 5 , wherein the polymer electrolyte membrane water electrolysis apparatus exhibits a current density of 0.07 to 0.96 A/cm 2 at 1.6 V and 120° C. 7. The polymer electrolyte membrane water electrolysis apparatus according to claim 5 , wherein the polymer electrolyte membrane water electrolysis apparatus exhibits a current density of 0.16 to 0.96 A/cm 2 . 8. The polymer electrolyte membrane water electrolysis apparatus according to claim 5 , wherein the polymer electrolyte membrane water electrolysis apparatus is a high-temperature polymer electrolyte membrane water electrolysis apparatus which is operated at 200° C. or less. 9. The polymer electrolyte membrane water electrolysis apparatus according to claim 8 , wherein the polymer electrolyte membrane water electrolysis apparatus is a high-temperature polymer electrolyte membrane water electrolysis apparatus which is operated at 60° C. or more. 10. A method for preparing an IrO 2 electrodeposited porous titanium composite layer of a polymer electrolyte membrane water electrolysis apparatus serving as both a diffusion layer and an oxygen electrode according to claim 1 , the method comprising: electrodepositing an iridium oxide (IrO 2 ) layer on a porous titanium (Ti) layer. 11. The method according to claim 10 , wherein the porous Ti layer comprises one or more selected from a group consisting of Ti layers in a form of titanium paper and mesh. 12. The method according to claim 10 , wherein the electrodeposition is performed at a deposition potential of 0.5 to 0.9 V SCE . 13. The method according to claim 10 , wherein the electrodeposition is performed for 1 min or more and less than 10 min. 14. The method according to claim 10 , wherein the electrodeposition is performed for 3 min or more and 8 min or less.
by anodic processes · CPC title
Electrodes comprising one or more electrocatalytic coatings on a substrate · CPC title
Valve metal, e.g. titanium · CPC title
by electrolysis of water · CPC title
comprising ion-exchange membranes in or on which electrode material is embedded · CPC title
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