IP Library Granted Patent US 10,673,075
Granted Patent B2
US 10,673,075 · App. 15/592,631 · Granted Jun 2, 2020

Fuel cell catalyst layer for improving power generation

Inventor: Noriyuki Kitao (Shizuoka-ken, JP)
Assignee: TOYOTA JIDOSHA KABUSHIKI KAISHA
H01M4/8673B01J39/20H01M4/86H01M4/8663H01M8/1004H01M8/1067H01M2004/8689H01M2008/1095H01M2250/20Y02E60/521
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Quick Facts
Patent No.
US 10,673,075
App. No.
15/592,631
Granted
Jun 2, 2020
Kind
B2
Abstract

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 ”.

Claims (40)

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.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 11, 2017
From: KITAO, NORIYUKI
To: TOYOTA JIDOSHA KABUSHIKI KAISHA
Reel/Frame 042446/0133 →
Priority Claims (1)
JP 2016-097280 · May 13, 2016 · national
Continuity (1)
Related Publication 20170331119A1 · Nov 16, 2017