초록 ▼

The membrane electrode assembly (MEA) of a PEM fuel cell can be recycled by contacting the MEA with a lower alkyl alcohol solvent which separates the membrane from the anode and cathode layers of the assembly. The resulting solution containing both the polymer membrane and supported noble metal cata

The membrane electrode assembly (MEA) of a PEM fuel cell can be recycled by contacting the MEA with a lower alkyl alcohol solvent which separates the membrane from the anode and cathode layers of the assembly. The resulting solution containing both the polymer membrane and supported noble metal catalysts can be heated under mild conditions to disperse the polymer membrane as particles and the supported noble metal catalysts and polymer membrane particles separated by known filtration means.

대표청구항 ▼

1. A process for recycling a membrane electrode assembly from a PEM fuel cell, said membrane electrode assembly comprising a fluorocarbon-containing ionomer film and supported noble metal catalysts coated on at least one side of said film, wherein said process comprising the steps: (a) contacting sa

1. A process for recycling a membrane electrode assembly from a PEM fuel cell, said membrane electrode assembly comprising a fluorocarbon-containing ionomer film and supported noble metal catalysts coated on at least one side of said film, wherein said process comprising the steps: (a) contacting said membrane electrode assembly with a solvent containing at least one C1 to C8 alkyl alcohol for a time sufficient to separate said ionomer film from said supported noble metal catalysts;(b) heating said solvent to a temperature sufficient for dispersing said ionomer film into polymer particles in said solvent; and(c) separating said dispersed polymer particles from said supported noble metal catalysts. 2. The process of claim 1, wherein said membrane electrode assembly is contacted with said solvent in a bath containing said solvent. 3. The process of claim 2, wherein said solvent is heated by a heater separated from said bath comprising said membrane electrode assembly. 4. The process of claim 3, wherein said solvent flows through said heater with a residence time of from about 1 minute to about 30 minutes. 5. The process of claim 1, wherein said solvent is directed to a first system for separation of said supported noble metal catalysts from said solution creating a permeate containing said dispersed polymer particles. 6. The process of claim 5, wherein said first system is a filter press. 7. The process of claim 1, wherein said noble metal catalyst is recovered from said support by combustion of said support in open air, or acid treatment of said support. 8. The process of claim 5, wherein said permeate is directed to a second system for separation of said dispersed polymer particles from said solvent. 9. The process of claim 8, wherein said dispersed polymer particles contain a radius of greater than 100 nm and wherein at least 90% of the particles contain a radius of less than 500 nm. 10. The process of claim 8, wherein said second system is an ultra-filtration system. 11. The process of claim 8, wherein said solvent is recycled for use in step (a). 12. The process of claim 1, wherein said solvent comprises at least one C3-C6 alkyl alcohol. 13. The process of claim 1, wherein said solvent comprises a mixture of said alcohol and water. 14. The process of claim 1, wherein said solvent comprises a mixture of two alcohols and water. 15. The process of claim 14, wherein said alcohols are isopropanol and butanol. 16. The process of claim 1, wherein said process is a continuous process. 17. The process of claim 1, wherein said membrane electrode assembly further comprises gas diffusion layers placed against each coating of said supported noble catalysts. 18. The process of claim 17, wherein said membrane electrode assembly further comprises outer gasket layers placed against each coating of said gas diffusion layers. 19. The process of claim 1, wherein said temperature in step (b) is from about 50° C. to about 180° C. 20. The process of claim 1, wherein said temperature in step (b) is from about 70° C. to about 100° C.