IP Library Granted Patent US 9,947,934
Granted Patent B2
US 9,947,934 · App. 14/786,632 · Granted Apr 17, 2018

Catalyst and electrode catalyst layer, membrane electrode assembly, and fuel cell using the catalyst

Inventors: Ken Akizuki (Nishitokyo, JP); Atsushi Ohma (Yokohama, JP); Tetsuya Mashio (Yokohama, JP); Yoshitaka Ono (Yokohama, JP); Shinichi Takahashi (Miura-gun, JP)
Assignees: NISSAN MOTOR CO., LTD.; NIPPON STEEL & SUMIKIN CHEMICAL CO., LTD.
H01M4/8657B22F9/02C22F1/02C22F1/14H01M4/8663H01M4/8885H01M4/9008H01M4/92H01M4/925H01M4/926H01M8/1004H01M2004/8684H01M2008/1095H01M2250/20Y02T90/32
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Quick Facts
Patent No.
US 9,947,934
App. No.
14/786,632
Granted
Apr 17, 2018
Kind
B2
Abstract

The present invention has an object to provide a catalyst having excellent oxygen reduction reaction activity. The present invention relates to a catalyst comprising a catalyst support and a catalyst metal supported on the catalyst support, wherein a specific surface area of the catalyst per support weight is 715 m 2 /g support or more or a covering ratio of the catalyst metal with an electrolyte is less than 0.5, and an amount of an acidic group of the catalyst per support weight is 0.75 mmol/g support or less.

Claims (30)

1. A cathode catalyst layer for a fuel cell, comprising:

a cathode catalyst comprising a catalyst support and catalyst metal supported on the catalyst support,

wherein catalyst metal is supported inside mesopores having a radius of 1 nm or more of the catalyst support,

wherein a specific surface area of the cathode catalyst per support weight is 1200 m 2 /g support or more, and

wherein an amount of an acidic group of the cathode catalyst per support weight is 0.75 mmol/g support or less, and

an electrolyte,

wherein catalyst metal, which is present inside the mesopores, is not covered with the electrolyte.

2. The cathode catalyst layer according to claim 1 , further comprising:

catalyst metal covered with the electrolyte,

wherein a covering ratio of the catalyst metal covered with the electrolyte is less than 0.5.

3. The cathode catalyst layer according to claim 2 , wherein the covering ratio of the catalyst metal covered with the electrolyte is 0.4 or less.

4. The cathode catalyst layer according to claim 1 , wherein the support includes a metal oxide or carbon.

5. The cathode catalyst layer according to claim 1 , wherein the acidic group is at least one selected from the group consisting of a hydroxyl group, a lactone group, and a carboxyl group.

6. The cathode catalyst layer according to claim 1 , wherein the catalyst metal is platinum or includes platinum and a metal component other than platinum.

7. The cathode catalyst layer according to claim 1 , wherein an amount of the catalyst metal supported on the support is 50 wt % or less.

8. The cathode catalyst layer for the fuel cell set forth in claim 1 , wherein the amount of the acidic group of the cathode catalyst per support weight is 0.1 mmol/g support or more.

9. The cathode catalyst layer for the fuel cell set forth in claim 1 , wherein the specific surface area of the cathode catalyst per support weight is 1700 m 2 /g support or more.

10. A membrane electrode assembly for a fuel cell comprising the cathode catalyst layer for the fuel cell set forth in claim 1 .

11. A fuel cell comprising the membrane electrode assembly for the fuel cell set forth in claim 10 .

12. The fuel cell set forth in claim 11 , wherein the fuel cell is a polymer electrolyte fuel cell.

13. A method of manufacturing the cathode catalyst layer set forth in claim 1 , comprising:

supporting the catalyst metal on the catalyst support to obtain a catalyst powder; and

subjecting the catalyst powder to heat-treatment in a hydrogen atmosphere,

wherein the heat-treatment is carried out at a range of 900° C. to 1400° C. in temperature.

14. A cathode, comprising:

a cathode catalyst comprising a catalyst support and catalyst metal supported on the catalyst support,

wherein catalyst metal is supported inside mesopores having a radius of 1 nm or more of the catalyst support,

wherein a specific surface area of the cathode catalyst per support weight is 1700 m 2 /g support or more,

wherein an amount of an acidic group of the cathode catalyst per support weight is 0.75 mmol/g support or less, and

wherein catalyst metal, which is present inside the mesopores, is not covered with the electrolyte.

Assignments (4)
CHANGE OF ADDRESS Recorded Nov 8, 2019
From: NIPPON STEEL CHEMICAL & MATERIAL CO., LTD.
To: NISSAN STEEL CHEMICAL & MATERIAL CO., LTD.
Reel/Frame 050968/0286 →
CORRECTIVE ASSIGNMENT TO CORRECT THE THE NAME OF THE ASSIGNEE PREVIOUSLY RECORDED ON REEL 048153 FRAME 0246. ASSIGNOR(S) HEREBY CONFIRMS THE NAME CHANGE. Recorded Mar 15, 2019
From: NIPPON STEEL & SUMIKIN CHEMICAL CO., LTD.
To: NIPPON STEEL CHEMICAL & MATERIAL CO., LTD.
Reel/Frame 048610/0244 →
CHANGE OF NAME Recorded Jan 28, 2019
From: NIPPON STEEL & SUMIKIN CHEMICAL CO., LTD.
To: NISSAN STEEL CHEMICAL & MATERIAL CO., LTD.
Reel/Frame 048153/0246 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 26, 2015
From: AKIZUKI, KEN; OHMA, ATSUSHI; MASHIO, TETSUYA; ONO, YOSHITAKA; TAKAHASHI, SHINICHI
To: NISSAN MOTOR CO., LTD.; NIPPON STEEL & SUMIKIN CHEMICAL CO., LTD.
Reel/Frame 036880/0674 →
Priority Claims (1)
JP 2013-092930 · Apr 25, 2013 · national
Continuity (1)
Related Publication 20160072133A1 · Mar 10, 2016