Electrodes for fuel cell and processes for producing the same

• US 20020015878A1
• Filed: 07/19/2001
• Published: 02/07/2002
• Est. Priority Date: 07/21/2000
• Status: Active Grant

• Current Assignee: GS Yuasa International Ltd. (GS Yuasa Corporation)
• Original Assignee: Japan Storage Battery Company Limited (GS Yuasa Corporation)
• Inventors: Tsumura, Naohiro, Hitomi, Shuji, Yasuda, Hideo
• Granted Patent: US 6,866,960 B2
• Time in Patent Office: Days
• US Class Current: 429/42
• CPC Class Codes: H01M 4/885 followed by reduction of the catalyst salt precursor
• CPC Class Codes: H01M 4/90 Selection of catalytic material
• CPC Class Codes: H01M 4/921 Alloys or mixtures with metallic elements
• CPC Class Codes: H01M 8/1004 characterised by membrane-electrode assemblies [MEA] H01M8/12 takes precedence
• CPC Class Codes: Y02E 60/50 Fuel cells

Abstract

An electrode for a fuel cell of the invention comprises a cation-exchange resin, carbon particles and a catalyst metal which is amorphous. The electrode has high activity, a high catalyst utilization and high CO tolerance and is highly active in the electrochemical oxidation reaction of methanol. Furthermore these qualities of the electrode were extremely improved when the catalyst metal was loaded mainly on sites where the surface of the carbon particles contacts proton-conductive passages in the cation-exchange resin. Consequently, a fuel cell with the electrode of the invention has a high output current and a long life, and can be produced at low cost.

Claims

1. An electrode for fuel cells, which comprises the following elements:

a cation-exchange resin,

carbon particles, and

a catalyst metal,

the catalyst metal being amorphous.

2. The electrode of claim 1, wherein the catalyst metal has a mean particle diameter of 1.5 nm or lower.

3. The electrode of claim 1, wherein the amount of the catalyst metal loaded on sites where the surface of the carbon particles contacts proton-conductive passages in the cation-exchange resin is higher than 80% by weight of the total amount of all the catalyst metal loaded.

4. The electrode of claim 1, wherein the catalyst metal comprises a metal element belonging to the platinum group.

5. The electrode of claim 1, wherein the catalyst metal comprises platinum element and ruthenium element.

6. The electrode of claim 1, wherein the catalyst metal comprises at least one element selected from the group consisting of magnesium, aluminum, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, silver, and tungsten.

7. The electrode of claim 1, wherein the amount of the catalyst metal contained in the electrode is 0.1 mg or lower per cm² of the electrode.

8. The electrode of claim 4, wherein the amount of the platinum-group metal element contained in the electrode is 0.05 mg or lower per cm² of the electrode.

9. The electrode of claim 2, wherein the catalyst metal comprises a metal element belonging to the platinum group.

10. The electrode of claim 2, wherein the catalyst metal comprises platinum element and ruthenium element.

11. The electrode of claim 2, wherein the catalyst metal comprises at least one element selected from the group consisting of magnesium, aluminum, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, silver, and tungsten.

12. The electrode of claim 2, wherein the amount of the catalyst metal contained in the electrode is 0.1 mg or lower per cm² of the electrode.

13. The electrode of claim 9, wherein the amount of the platinum-group metal element in contained the electrode is 0.05 mg or lower per cm² of the electrode.

14. The electrode of claim 3, wherein the catalyst metal comprises a metal element belonging to the platinum group.

15. The electrode of claim 3, wherein the catalyst metal comprises platinum element and ruthenium element.

16. The electrode of claim 3, wherein the catalyst metal comprises at least one element selected from the group consisting of magnesium, aluminum, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, silver, and tungsten.

17. The electrode of claim 3, wherein the amount of the catalyst metal contained in the electrode is 0.1 mg or lower per cm² of the electrode.

18. The electrode of claim 14, wherein the amount of the platinum-group metal element contained in the electrode is 0.05 mg or lower per cm² of the electrode.

19. The electrode of claim 2, wherein the amount of the catalyst metal loaded on sites where the surface of the carbon particles contacts proton-conductive passages in the cation-exchange resin is higher than 80% by weight of the total amount of all the catalyst metal loaded.

20. The electrode of claim 19, wherein the catalyst metal comprises a metal element belonging to the platinum group.

21. The electrode of claim 19, wherein the catalyst metal comprises platinum element and ruthenium element.

22. The electrode of claim 19, wherein the catalyst metal comprises at least one element selected from the group consisting of magnesium, aluminum, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, silver, and tungsten.

23. The electrode of claim 19, wherein the amount of the catalyst metal contained in the electrode is 0.1 mg or lower per cm² of the electrode.

24. The electrode of claim 20, wherein the amount of the platinum-group metal element contained in the electrode is 0.05 mg or lower per cm² of the electrode.

26. The electrode of claim 25, wherein the amount of the catalyst metal loaded on sites where the surface of the carbon particles contacts proton-conductive passages in the cation-exchange resin is higher than 80% by weight of the total amount of all the catalyst metal loaded.

27. The electrode of claim 25, wherein the catalyst metal comprises a metal element belonging to the platinum group.

28. The electrode of claim 25, wherein the catalyst metal comprises platinum element and ruthenium element.

29. The electrode of claim 25, wherein the catalyst metal comprises at least one element selected from the group consisting of magnesium, aluminum, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, silver, and tungsten.

30. The electrode of claim 25, wherein the amount of the catalyst metal contained in the electrode is 0.1 mg or lower per cm² of the electrode.

31. The electrode of claim 27, wherein the amount of the platinum-group metal element contained in the electrode is 0.05 mg or lower per cm² of the electrode.

32. The electrode of claim 26, wherein the catalyst metal comprises a metal element belonging to the platinum group.

33. The electrode of claim 26, wherein the catalyst metal comprises platinum element and ruthenium element.

34. The electrode of claim 26, wherein the catalyst metal comprises at least one element selected from the group consisting of magnesium, aluminum, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, silver, and tungsten.

35. The electrode of claim 26, wherein the amount of the catalyst metal contained in the electrode is 0.1 mg or lower per cm² of the electrode.

36. The electrode of claim 32, wherein the amount of the platinum-group metal element contained in the electrode for fuel cells is 0.05 mg or lower per cm² of the electrode.

38. The process of claim 37, wherein the reduction step is conducted at a temperature of 200°

C. or lower.

39. The process of claim 37, wherein the cation-exchange resin has an ion-exchange capacity of 2.5 meq/g or lower.

40. The process of claim 37, which further comprises a step in which the cations unreduced are eluted with an inorganic acid after the reduction step.

46. A polymer electrolyte fuel cell comprising the following elements:

(1) an anode,

(2) a cathode, and

(3) a solid polymer electrolyte film,

wherein at least one of the anode and the cathode is the electrode for fuel cells of any one of claims 1 to 36 or the electrode for fuel cells produced by the process of any one of claims 37 to 45.

25. An electrode for fuel cells, which comprises the following elements:

a cation-exchange resin,

carbon particles, and

a catalyst metal,

the catalyst metal having a mean particle diameter of 1.5 nm or lower.

37. A process for producing an electrode for fuel cells which comprises the following steps:

(1) a formation step in which a no-catalyzed electrode comprising a mixture of a cation-exchange resin and carbon particles is formed;

(2) an adsorption step in which the no-catalyzed electrode is immersed in a solution comprising cations containing a catalyst metal element, thereby the cations are absorbed into the cation-exchange resin based on the ion-exchange reaction of the cations with counter ions of the cation-exchange resin; and

(3) a reduction step in which the cations adsorbed into the cation-exchange resin are reduced for 10 hours or longer in a gaseous atmosphere comprising hydrogen gas resulting in formation of the catalyst metal.

41. A process for producing an electrode for fuel cells which comprises the following steps:

(1) a formation step in which a no-catalyzed electrode comprising a mixture of a cation-exchange resin and carbon particles is formed;

(2) an adsorption step in which the no-catalyzed electrode is immersed in a solution comprising cations containing a catalyst metal element, thereby the cations are absorbed into the cation-exchange resin based on the ion-exchange reaction of the cations with counter ions of the cation-exchange resin;

(3) a reduction step in which the cations adsorbed into the cation-exchange resin are reduced in a gaseous atmosphere comprising hydrogen gas resulting formation of the catalyst metal; and

(4) an ageing step in which the catalyst metal is aged in an acid solution or alkaline solution or a gaseous atmosphere comprising an inert gas as the main component.

42. The process of claim 41, wherein at least one of the reduction step and the ageing step is conducted at a temperature of 200°

C. or lower.

43. The process of claim 41, wherein the ageing step is conducted for 10 hours or longer.

44. The process of claim 41, wherein the cation-exchange resin has an ion-exchange capacity of 2.5 meq/g or lower.

45. The process of claim 41, which further comprises a step in which the cations unreduced are eluted with an inorganic acid after the reduction step.