Method of making membrane-electrode assemblies for electrochemical cells and assemblies made thereby

• US 5,316,871 A
• Filed: 08/05/1993
• Issued: 05/31/1994
• Est. Priority Date: 04/03/1992
• Status: Expired due to Term

• Current Assignee: GM Global Technology Operations LLC (General Motors Company)
• Original Assignee: General Motors Corporation (General Motors Company)
• Inventors: Swathirajan, Sundararajan, Mikhail, Youssef M.
• Primary Examiner(s): Maples, John S.
• Application Number:
  US08/102,189
• Time in Patent Office: 299 Days
• Field of Search: 429/42, 429/43, 429/30, 429/33, 429/192, 429/44
• US Class Current: 429/535
• CPC Class Codes: C25B 9/23 comprising ion-exchange membranes in or on which electrode material is embedded
• CPC Class Codes: H01M 4/96 Carbon-based electrodes
• CPC Class Codes: H01M 8/04291 Arrangements for managing water in solid electrolyte fuel cell systems H01M8/04119 takes precedence
• CPC Class Codes: H01M 8/1004 characterised by membrane-electrode assemblies [MEA] H01M8/12 takes precedence
• CPC Class Codes: Y02E 60/50 Fuel cells
• CPC Class Codes: Y02P 70/50 Manufacturing or production processes characterised by the final manufactured product

Abstract

A method of making a combination, unitary, membrane and electrode assembly having a solid polymer electrolyte membrane, and first and second electrodes at least partially embedded in opposed surfaces of the membrane. The electrodes each comprise a respective group of finely divided carbon particles, very finely divided catalytic particles supported on internal and external surfaces of the carbon particles and a proton conductive material intermingled with the catalytic and carbon particles. A first group of finely divided carbon particles forming the first electrode has greater water attraction and retention properties, and is more hydrophilic than a second group of carbon particles forming the second electrode. In a preferred method, the membrane electrode assembly of the invention is prepared by forming a slurry of proton conductive material and at least one group of the carbon and catalyst particles. The slurry is applied to the opposed surfaces of the membrane and heated while being pressed to the membrane for a time and at a temperature and compressive load sufficient to embed at least a portion of the particles into the membrane.

Claims

1. A method of making a combination electrolyte and electrode structure for an electrochemical cell having an electrolyte membrane of solid polymer proton conductive material with first and second spaced apart opposed surfaces and first and second electrodes at the respective first and second surface, comprising:

a) forming a slurry of proton conductive material and at least one group of finely divided carbon particles and very finely divided catalytic particles supported on and in the carbon particles;

b) applying the slurry onto a first surface of the membrane;

c) applying the slurry onto a second surface of the membrane; and

d) heating while pressing the applied slurry for a time and at a temperature and compressive load sufficient to embed at least a portion of the particles in, respectively, the surfaces of the membrane to thereby form the first and second electrodes.

2. A method according to claim 1, wherein the compressive load is in the range of about 1,000 to about 2,000 pounds per square inch.

3. A method according to claim 1, wherein the time is in the range of about 1 minute to about 5 minutes.

4. A method according to claim 1, wherein the temperature is in the range of about 120°

C. to about 150°

C.

5. A method according to claim 1, wherein before the step of heating while pressing, the applied slurry is dried by heating for a time and at a temperature sufficient to vaporize any volatile liquid components of the slurry.

6. A method of making a combination electrolyte and electrode structure for an electrochemical cell having an electrolyte membrane of solid polymer proton conductive material with first and second spaced apart opposed surfaces and first and second electrodes at the respective first and second surfaces, comprising:

a) forming a first slurry of proton conductive material and a first group of finely divided carbon particles and very finely divided catalytic particles supported on and in the carbon particles;

b) forming a second slurry of proton conductive material and a second group of finely divided carbon particles and very finely divided catalytic particles supported on and in the carbon particles, the second group being less acidic than the first group;

c) applying the first slurry onto a first surface of the membrane;

d) applying the second slurry onto a second surface of the membrane; and

e) heating while pressing the applied slurry for a time and at a temperature and compressive load sufficient to embed at least a portion of the particles in, respectively, the surfaces of the membrane to thereby form the first and second electrodes.

7. A method according to claim 6, wherein step (c) is conducted by coating the first slurry onto a surface of a first sheet of polytetrafluoroethylene impregnated graphite paper and then placing the coated surface in contact with the first surface of the membrane;

and wherein step (d) is conducted by coating the second slurry onto a surface of a second sheet of polytetrafluoroethylene impregnated graphite paper and then placing the coated surface of the second sheet in contact with the second surface of the membrane.

8. A method according to claim 6, wherein the first group of the finely divided carbon particles has an average pore size in the range of about 90 to about 110 angstroms, and wherein the average pore size of the second group is in the range of about 60 to about 80 angstroms.

9. A method according to claim 6, wherein each one of the first and second groups of the finely divided carbon particles is characterized by a pH, and wherein the first group has a pH in the range of about 6 to about 7 and the second group has a pH in the range of about 8 to about 10.

10. A method according to claim 6, wherein the catalytic particles of the first and second slurries are each of platinum, and wherein the second slurry has a concentration of platinum sufficient to provide a platinum loading less than about 0.07 milligrams per cm² of electrode surface area, and wherein the platinum concentration of the first slurry is less than that of the second slurry.

11. A method according to claim 6, wherein the very finely divided catalytic particles are of platinum supported on the carbon particles, and in a proportion, based on 100 parts by weight, the platinum particles constitute up to about 15 parts and the finely divided carbon particles the balance.

12. A method according to claim 6, wherein the electrolyte membrane and the proton conductive material each comprise perfluorocarbon sulfonic acid polymer.

13. A method according to claim 6 wherein each one of the slurries consists essentially of the proton conductive material and the catalytic and carbon particles in a proportion, based on 100 pairs, of about 30 to about 50 parts proton conductive material and the balance the catalytic and carbon particles.

14. A method according to claim 6, wherein the temperature is in the range of about 120°

C. to about 150°

C.

15. A method according to claim 6, wherein the compressive load is in the range of about 1,000 to about 2,000 pounds per square inch.

16. A method according to claim 6, wherein before the step of heating while pressing, the applied slurry is dried by heating for a time and at a temperature sufficient to vaporize any volatile liquid components of the slurry.

17. A method according to claim 6 and including before step (a), ball-milling the first group of carbon particles for a time sufficient to provide an average pore size in the range of about 90 to about 110 angstroms with at least about 50% of the pores having a size greater than about 20 angstroms.