Carbon sheet, gas diffusion electrode substrate and fuel cell
US-2017237079-A1 · Aug 17, 2017 · US
US10673075B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10673075-B2 |
| Application number | US-201715592631-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 11, 2017 |
| Priority date | May 13, 2016 |
| Publication date | Jun 2, 2020 |
| Grant date | Jun 2, 2020 |
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A fuel cell includes: an electrolyte membrane; an anode catalyst layer; a cathode catalyst layer; and a cathode gas diffusion layer. The cathode catalyst layer includes an ionomer, the ionomer includes copolymers each of which has a hydrophilic block. The hydrophilic block is positioned at a terminal of a copolymer which includes a hydrophobic portion and a hydrophilic portion having a sulfonic acid group. The hydrophilic block has an aggregated structure of the hydrophilic portion. A gas diffusion resistance coefficient of the cathode gas diffusion layer is 3.2×10 −4 m or lower. The gas diffusion resistance coefficient is expressed by “Gas Diffusion Resistance Coefficient=Thickness of Cathode Gas Diffusion Layer/(Porosity of Cathode Gas Diffusion Layer) 4 ”.
Opening claim text (preview).
What is claimed is: 1. A fuel cell comprising: an electrolyte membrane; an anode catalyst layer that is provided on a first surface of the electrolyte membrane; a cathode catalyst layer that includes an ionomer and is provided on a second surface of the electrolyte membrane, the ionomer including copolymers each of which has a hydrophilic block, the hydrophilic block being positioned at a terminal of the copolymer including a hydrophobic portion and a hydrophilic portion which has a sulfonic acid group, the hydrophilic block having an aggregated structure of the hydrophilic portion; and a cathode gas diffusion layer that is provided outside the cathode catalyst layer, wherein a gas diffusion resistance coefficient of the cathode catalyst layer represented by the following expression is 3.2×10 −4 m or lower, the gas diffusion resistance coefficient=a thickness of the cathode gas diffusion layer/(a porosity of the cathode gas diffusion layer) 4 , wherein the hydrophilic portion has a structure represented by the following Formula A1, and the hydrophobic portion has a structure represented by the following Formula B1, where a represents an integer of 0 or more, and b represents an integer of 2 or more, where Rf 1 and Rf 2 each independently represent fluorine or a perfluoroalkyl group having 1 to 10 carbon atoms. 2. The fuel cell according to claim 1 , wherein the copolymer is a random copolymer having the hydrophilic portion at the terminal. 3. The fuel cell according to claim 1 , wherein the number of repeats of the hydrophilic portion in the hydrophilic block is 11 to 16. 4. The fuel cell according to claim 1 , wherein a lower melting point water content in the ionomer is 28 dry % to 38 dry %. 5. The fuel cell according to claim 1 , wherein an oxygen permeability of the ionomer at a relative humidity of 30% or higher is 20×10 −12 mol/(cm 2 ×s×atm) or higher. 6. The fuel cell according to claim 1 , wherein a portion of the copolymer other than the hydrophilic block includes a non-aggregated portion. 7. A fuel cell comprising: an electrolyte membrane; an anode catalyst layer that is provided on a first surface of the electrolyte membrane; a cathode catalyst layer that includes an ionomer and is provided on a second surface of the electrolyte membrane, the ionomer including copolymers each of which has a hydrophilic block, the hydrophilic block being positioned at a terminal of the copolymer including a hydrophobic portion and a hydrophilic portion which has a sulfonic acid group, the hydrophilic block having an aggregated structure of the hydrophilic portion; and a cathode gas diffusion layer that is provided outside the cathode catalyst layer, wherein a gas diffusion resistance coefficient of the cathode catalyst layer represented by the following expression is 3.2×10 −4 m or lower, the gas diffusion resistance coefficient=a thickness of the cathode gas diffusion layer/(a porosity of the cathode gas diffusion layer) 4 , wherein the hydrophilic portion has a structure represented by the following Formula A1, and the hydrophobic portion has a structure represented by the following Formula B1, where a represents an integer of 0 or more, and b represents an integer of 2 or more, where Rf 1 and Rf 2 each independently represent fluorine or a perfluoroalkyl group having 1 to 10 carbon atoms which has an ether bond in a middle of the perfluoroalkyl group. 8. The fuel cell according to claim 7 , wherein the copolymer is a random copolymer having the hydrophilic portion at the terminal. 9. The fuel cell according to claim 7 , wherein the number of repeats of the hydrophilic portion in the hydrophilic block is 11 to 16. 10. The fuel cell according to claim 7 , wherein a lower melting point water content in the ionomer is 28 dry % to 38 dry %. 11. The fuel cell according to claim 7 , wherein an oxygen permeability of the ionomer at a relative humidity of 30% or higher is 20×10 −12 mol/(cm 2 ×s×atm) or higher. 12. The fuel cell according to claim 7 , wherein a portion of the copolymer other than the hydrophilic block includes a non-aggregated portion.
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