Electrochemical cell
US-2024332559-A1 · Oct 3, 2024 · US
US10069148B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10069148-B2 |
| Application number | US-201514697770-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 28, 2015 |
| Priority date | May 10, 2014 |
| Publication date | Sep 4, 2018 |
| Grant date | Sep 4, 2018 |
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Use of a selectively conducting anode component in solid polymer electrolyte fuel cells can reduce the degradation associated with repeated startup and shutdown, but can also adversely affect a cell's tolerance to voltage reversal along with its performance. It was shown that these adverse affects can be mitigated against in certain ways. However, improved results can be obtained by employing a selectively conducting component which comprises a mixed layer of a selectively conducting material and carbon. The mixed layer contacts the side of the anode opposite the solid polymer electrolyte.
Opening claim text (preview).
What is claimed is: 1. A solid polymer electrolyte fuel cell comprising a solid polymer electrolyte, a cathode, and anode components connected in series electrically wherein: i) the anode components comprise an anode, an anode gas diffusion layer, and a selectively conducting component, wherein the gas diffusion layer is separated from the anode electrode by the selectively conducting component; ii) the selectively conducting component comprises a mixed layer in direct contact with the side of the anode opposite the solid polymer electrolyte wherein the mixed layer comprises a mixture of a selectively conducting material and from about 6% to about 14% carbon by weight; and iii) the electrical resistance of the selectively conducting component in the presence of hydrogen is more than 100 times lower than the electrical resistance in the presence of air. 2. The fuel cell of claim 1 wherein the electrical resistance of the selectively conducting component in the presence of hydrogen is more than 1000 times lower than the electrical resistance in the presence of air. 3. The fuel cell of claim 1 wherein the selectively conducting material comprises a noble metal deposited on a metal oxide. 4. The fuel cell of claim 3 wherein the selectively conducting material comprises platinum deposited on tin oxide. 5. The fuel cell of claim 4 wherein the selectively conducting material comprises SnO 2 . 6. The fuel cell of claim 1 wherein the carbon is a synthetic graphite. 7. The fuel cell of claim 1 wherein the thickness of the mixed layer is in the range from about 6 to about 12 micrometers. 8. The fuel cell of claim 1 wherein the selectively conducting component comprises a selectively conducting layer in direct contact with the side of the mixed layer opposite the solid polymer electrolyte wherein the selectively conducting layer consists essentially of the selectively conducting material and binder. 9. The fuel cell of claim 8 wherein the thickness of the mixed layer is in the range from about 2 to about 4 micrometers. 10. The fuel cell of claim 8 wherein the thickness of the selectively conducting layer is in the range from about 2 to about 8 micrometers. 11. The fuel cell of claim 1 wherein the selectively conducting material, carbon, and mixed layer characteristics are selected such that the fuel cell voltage is greater than about 0.5 V when operating at 1.5 A/cm 2 . 12. A fuel cell stack comprising the fuel cell of claim 1 . 13. A vehicle comprising a traction power supply comprising the fuel cell stack of claim 12 . 14. A solid polymer electrolyte fuel cell comprising a solid polymer electrolyte, a cathode, and anode components connected in series electrically wherein: i) the anode components comprise an anode, an anode gas diffusion layer, and a mixed layer, wherein the gas diffusion layer is separated from the anode electrode by the mixed layer; ii) the mixed layer is in direct contact with the side of the anode opposite the solid polymer electrolyte and comprises a mixture of a selectively conducting material and from about 6% to about 14% carbon by weight; and iii) the electrical resistance of the mixed layer in the presence of hydrogen is more than 100 times lower than the electrical resistance in the presence of air. 15. A method for increasing the tolerance of a solid polymer electrolyte fuel cell to voltage reversal, the method comprising: adding a reversal tolerance imparting effective amount of carbon to a selectively conducting material to form a mixed layer forming material, and forming the solid polymer electrolyte fuel cell comprising a cathode flow field plate, a cathode gas diffusion layer, a cathode electrode, a solid polymer electrolyte, an anode electrode, a selectively conducting component having an electrical resistance more than 100 times lower in the presence of hydrogen than in the presence of air and comprising a mixed layer formed from said mixed layer forming material, an anode gas diffusion layer, and an anode flow field plate, wherein the mixed layer is in direct contact with the side of the anode electrode opposite the solid polymer electrolyte and separates the anode gas diffusion layer from the anode electrode, and wherein the reversal tolerance imparting effective amount of carbon is from about 6% to about 14% carbon by weight based on the weight of the mixed layer. 16. The method of claim 15 comprising incorporating a selectively conducting layer in direct contact with the side of the mixed layer opposite the solid polymer electrolyte wherein the selectively conducting layer consists essentially of the selectively conducting material and binder.
Polymeric electrolyte materials · CPC title
Carbonaceous material · CPC title
with both reactants being gaseous or vaporised (H01M8/12 takes precedence) · CPC title
in the form of mixtures · CPC title
Negative electrodes · CPC title
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