Granted Patent B2

US 7,887,963 · App. 11/113,462 · Granted Feb 15, 2011

Abstract

Claims (52)

1. A method of operating an electrochemical conversion assembly comprising a membrane electrode assembly, an anode flow field, and a cathode flow field, wherein:

said membrane electrode assembly comprises a proton exchange membrane separating an anode and cathode of said assembly;

said membrane electrode assembly comprises a catalyst supported by a relatively high surface area support material;

said proton exchange membrane comprises a material characterized by enhanced proton conductivity under wet conditions; and

said method comprises

initiating a start up sequence,

operating said electrochemical conversion assembly under wet conditions by driving a hydrogenous gas through said anode flow field and an oxygen-containing gas through said cathode flow field, and

initiating a shut down sequence comprising driving a substantially dry oxygen-containing reactant gas through said cathode flow field for an amount of time sufficient to reduce the water content of said proton exchange membrane to a level sufficient to suppress catalyst dissolution and corrosion in said membrane electrode assembly, wherein said substantially dry oxygen-containing reactant gas is initially introduced at a first temperature characterized by a relatively high vapor capacity and is subsequently introduced at a second, cooler temperature sufficient to reduce the temperature of said membrane electrode assembly; interrupting a flow of said substantially dry oxygen-containing reactant gas when the water content of said proton exchange membrane is reduced; supplying said hydrogenous gas through said anode flow field after interrupting said flow of said substantially dry oxygen-containing reactant gas for a time sufficient to dilute an oxygen content of said cathode flow field; and introducing a substantially dry air purge into said anode flow field following dilution of said oxygen content.

2. A method as claimed in claim 1 wherein said substantially dry oxygen-containing reactant gas is driven through said cathode flow field during said shut down sequence for an amount of time sufficient to reduce the water content λ of said proton exchange membrane to below about 5, where λ corresponds to the molar ratio H 2 O/SO 3 H in said membrane.

3. A method as claimed in claim 1 wherein said substantially dry oxygen-containing reactant gas is driven through said cathode flow field during said shut down sequence for an amount of time sufficient to reduce the water content λ of said proton exchange membrane to below about 50% equivalent RH.

4. A method as claimed in claim 1 wherein electrical resistivity of said proton exchange membrane is monitored during said shut down sequence and supply of said substantially dry oxygen-containing reactant gas is interrupted when said resistivity reaches a predetermined value.

5. A method as claimed in claim 1 wherein the relative humidity of a cathode outlet gas is monitored during said shut down sequence and supply of said substantially dry oxygen-containing reactant gas is interrupted when said relative humidity reaches a predetermined value.

6. A method as claimed in claim 1 wherein said substantially dry oxygen-containing reactant gas is driven through said cathode flow field to initiate a transition of said conversion assembly from relatively high load operating conditions.

7. A method as claimed in claim 6 wherein said transition from said relatively high load operating conditions is accompanied by a substantial decrease in the supply of said hydrogenous gas through said anode flow field.

8. A method as claimed in claim 1 wherein:

said shut down sequence is further characterized by connecting a shorting resistor across said membrane electrode assembly; and.

9. A method as claimed in claim 8 wherein supply of said diluting hydrogenous gas is accompanied by application of an electrical short across said membrane electrode assembly to reduce the voltage of said cathode.

10. A method as claimed in claim 1 wherein:

said shut down sequence is further characterized by connecting a shorting resistor across said membrane electrode assembly introducing a substantially dry air in said cathode flow fields to achieve said reduction in said water content of said proton exchange membrane and simulate an equilibrium storage condition in said electrochemical conversion assembly.

11. A method as claimed in claim 1 wherein said start up sequence is characterized by driving a substantially dry gas through said cathode flow field following said shut down sequence and prior to driving said hydrogenous gas through said anode flow field.

12. A method as claimed in claim 1 wherein said substantially dry oxygen-containing reactant gas is characterized by a relative humidity of less than about 40%.

13. A method as claimed in claim 1 wherein said substantially dry oxygen-containing reactant gas is air or is characterized by a composition substantially equivalent to that of air.

14. A method as claimed in claim 1 wherein said electrochemical conversion assembly is operated at relatively low current density for a sufficient amount of time during said shut down sequence to provide energy sufficient to drive said substantially dry oxygen-containing reactant gas through said cathode flow field.

15. A method as claimed in claim 1 wherein said electrochemical conversion assembly is operated from an external power source to provide energy sufficient to drive said substantially dry oxygen-containing reactant gas through said cathode flow field.

16. A method as claimed in claim 1 wherein said second, cooler temperature comprises a temperature sufficient to suppress said catalyst dissolution and said corrosion in said membrane electrode assembly.

17. A method as claimed in claim 16 wherein said second, cooler temperature is affected through the operation of an assembly coolant pump, the introduction of a relatively cool gas into one or both of said flow fields, or combinations thereof.

18. A method as claimed in claim 16 wherein said cooling is sufficient to reduce the temperature of said membrane electrode assembly to below about 50° C.

19. A method as claimed in claim 16 wherein said cooling is sufficient to reduce the temperature of said membrane electrode assembly to about 25° C.

20. A method as claimed in claim 1 wherein said first temperature is between about 75° C. and about 90° C. and said second temperature is below about 50° C.

21. A method of operating an electrochemical conversion assembly comprising a membrane electrode assembly, an anode flow field, and a cathode flow field, wherein:

said membrane electrode assembly comprises a proton exchange membrane separating an anode and cathode of said assembly;

said proton exchange membrane comprises a material characterized by enhanced proton conductivity under wet conditions; and

said method comprises

initiating a start up sequence where a hydrogenous front is driven through said anode flow field,

operating said electrochemical conversion assembly under wet conditions by driving a hydrogenous gas through said anode flow field and an oxygen-containing gas through said cathode flow field, and

initiating a shut down sequence comprising driving a substantially dry oxygen-containing reactant gas through said cathode flow field for an amount of time sufficient to reduce the water content λ of said proton exchange membrane to below about 5, where λ corresponds to an H 2 O/SO 3 H ratio in said membrane, wherein said substantially dry oxygen-containing reactant gas is initially introduced at a first temperature characterized by a relatively high vapor capacity and is subsequently introduced at a second, cooler temperature sufficient to reduce the temperature of said membrane electrode assembly; interrupting a flow of said substantially dry oxygen-containing reactant gas when the water content of said proton exchange membrane is reduced; supplying said hydrogenous gas through said anode flow field after interrupting said flow of said substantially dry oxygen-containing reactant gas for a time sufficient to dilute an oxygen content of said cathode flow field; and introducing a substantially dry air purge into said anode flow field following dilution of said oxygen content.

22. A method of operating an electrochemical conversion assembly comprising a membrane electrode assembly, an anode flow field, and a cathode flow field, wherein:

said membrane electrode assembly comprises a proton exchange membrane separating an anode and cathode of said assembly;

said membrane electrode assembly comprises a catalyst supported by a relatively high surface area support material;

said proton exchange membrane comprises a material characterized by enhanced proton conductivity under wet conditions; and

said method comprises

initiating a start up sequence,

operating said electrochemical conversion assembly under wet conditions by driving a hydrogenous gas through said anode flow field and an oxygen-containing gas through said cathode flow field, and

initiating a shut down sequence comprising driving a substantially dry oxygen-containing reactant gas through said anode flow field for an amount of time sufficient to reduce the water content of said proton exchange membrane to a level sufficient to suppress catalyst dissolution and corrosion in said membrane electrode assembly, wherein said substantially dry oxygen-containing reactant is initially introduced at a first temperature characterized by a relatively high vapor capacity and is subsequently introduced at a second, cooler temperature sufficient to reduce the temperature of said membrane electrode assembly; interrupting a flow of said substantially dry oxygen-containing reactant gas when the water content of said proton exchange membrane is reduced; supplying said hydrogenous gas through said anode flow field after interrupting said flow of said substantially dry oxygen-containing reactant gas for a time sufficient to dilute an oxygen content of said cathode flow field; and introducing a substantially dry air purge into said anode flow field following dilution of said oxygen content.

23. An electrochemical conversion assembly comprising a membrane electrode assembly, an anode flow field, a cathode flow field, a source of substantially dry gas, and an assembly controller, wherein:

said membrane electrode assembly comprises a proton exchange membrane separating an anode and cathode of said assembly;

said membrane electrode assembly comprises a catalyst supported by a relatively high surface area support material;

said proton exchange membrane comprises a material characterized by enhanced proton conductivity under wet conditions;

said support material and said electrode catalyst are subject to corrosion and catalyst dissolution as a result of relatively high voltages developed on said cathode of said membrane electrode assembly;

said electrochemical conversion assembly is optimized for operation under wet conditions with a hydrogenous gas driven through said anode flow field and an oxygen-containing gas driven through said cathode flow field;

said assembly controller is programmed to initiate a shut down sequence where a substantially dry oxygen-containing reactant gas from said dry gas source is driven through said cathode flow field for an amount of time sufficient to reduce the water content of said proton exchange membrane to a level sufficient to suppress said catalyst dissolution and said corrosion in said membrane electrode assembly, wherein said substantially dry oxygen-containing reactant gas is initially introduced at a first temperature characterized by a relatively high vapor capacity and is subsequently introduced at a second, cooler temperature sufficient to reduce the temperature of said membrane electrode assembly; a flow of said substantially dry oxygen-containing reactant gas is interrupted when the water content of said proton exchange membrane is reduced; said hydrogenous gas is supplied through said anode flow field after said flow of said substantially dry oxygen-containing reactant gas is interrupted for a time sufficient to dilute an oxygen content of said cathode flow field; and introducing a substantially dry air purge into said anode flow field following dilution of said oxygen content.

24. The method of claim 1 wherein said shut down sequence further comprises substantially decreasing a supply of said hydrogenous gas through said anode flow field while said substantially dry oxygen-containing reactant gas is flowing through said cathode flow field.

Assignments (12)