Controls giving −25° C. freeze start capability to a fuel cell system

Patent metadata

Field	Value
Publication number	US-9379396-B2
Application number	US-76474910-A
Country	US
Kind code	B2
Filing date	Apr 21, 2010
Priority date	Apr 21, 2010
Publication date	Jun 28, 2016
Grant date	Jun 28, 2016

Abstract

A method for shutting down a fuel cell system including operating a fuel cell stack. the method includes providing an increased cathode air flow so as to dry fuel cell membranes in the stack until a first desired level of high frequency resistance is achieved, rehydrating the cell membranes of the stack until a second desired level of high frequency resistance is achieved, and operating the stack with a decreased cathode input relative humidity until a third desired level of high frequency resistance is achieved.

First claim

What is claimed is:

1. A method for shutting down a fuel cell system, said method comprising:
operating a fuel cell stack with an air flow so as to dry a plurality of fuel cell membranes in the stack to a predetermined average HFR within a predetermined window of time such that a first level of average high frequency resistance is achieved;
rehydrating the cell membranes of the stack until a second level of average high frequency resistance is achieved;
operating the stack with a predetermined cathode input relative humidity until a third level of average high frequency resistance is achieved; and
shutting down the fuel cell system.

2. The method according to claim 1 wherein drying the plurality of membranes to a predetermined average HFR within a predetermined window of time is longer in duration than each of rehydrating the cell membranes of the stack and operating the stack with the predetermined cathode input relative humidity.

3. The method according to claim 1 wherein the ratio of the amount of time for drying the plurality of membranes to a predetermined average HFR within a predetermined window of time to the amount of time for rehydrating the cell membranes of the stack is at least 3:1.

4. The method according to claim 1 wherein drying the plurality of membranes to a predetermined average HFR within a predetermined window of time includes adjusting the speed of a compressor to achieve the first level of high frequency resistance in a predetermined window of time.

5. The method according to claim 1 wherein the cathode input relative humidity while operating the stack with the predetermined cathode input relative humidity is approximately 35%.

6. The method according to claim 1 wherein operating the stack with the predetermined cathode input relative humidity includes increasing the cathode air flow.

7. The method according to claim 1 further comprising setting the speed of a compressor to a cathode air flow so as to reduce high frequency resistance signal noise.

8. The method according to claim 1 further comprising a procedure for aborting the shutdown if a restart of the fuel cell system is requested before shutdown completes and the measured high frequency resistance is below a predetermined level.

9. A method for shutting down a fuel cell, said method comprising:
setting the speed of a compressor to a cathode air flow so as to reduce high frequency resistance signal noise;
operating the fuel cell with a cathode air flow so as to dry a membrane in the fuel cell to a predetermined average HFR within a predetermined window of time such that a first level of cell high frequency resistance is achieved, and measuring the cell high frequency resistance while operating the fuel cell with the cathode air flow;
rehydrating the membrane of the fuel cell until a second level of cell high frequency resistance is achieved and measuring the cell high frequency resistance while rehydrating the membrane of the fuel cell;
decreasing the cathode input relative humidity to a predetermined level and operating the fuel cell until a third level of cell high frequency resistance is achieved, and measuring the cell high frequency resistance while decreasing the cathode input relative humidity and operating the fuel cell; and
shutting down the fuel cell.

10. The method according to claim 9 wherein operating the fuel cell with the cathode air flow so as to dry the membrane in the fuel cell is longer in duration than each of rehydrating the membrane of the fuel cell and decreasing the cathode input relative humidity to the predetermined level and operating the fuel cell.

11. The method according to claim 9 wherein the ratio of the amount of time for drying the membrane to the amount of time for rehydrating the cell membrane is at least 3:1.

12. The method according to claim 9 further comprising monitoring the duration of time of operating the fuel cell with the cathode air flow to dry the membrane in the fuel cell and adjusting the speed of a compressor as needed to achieve the first level of high frequency resistance in the predetermined window of time.

13. The method according to claim 9 wherein decreasing the cathode input relative humidity to the predetermined level and operating the fuel cell further includes increasing the cathode air flow above a predetermined level.

14. The method according to claim 9 wherein the cathode input relative humidity while decreasing the cathode input relative humidity to the predetermined level and operating the fuel cell is approximately 35%.

15. The method according to claim 9 further comprising a procedure for aborting the shutdown if a restart of the fuel cell is requested before shutdown completes and the measured high frequency resistance is below a predetermined level.

16. A method for shutting down a fuel cell system, said method comprising:
setting the speed of a compressor to a first cathode air flow so as to reduce high frequency resistance signal noise;
operating a fuel cell stack with an air flow so as to dry a plurality of fuel cell membranes in the stack to a predetermined average HFR within a predetermined window of time such that a first level of average high frequency resistance is achieved;
rehydrating the cell membranes of the stack until a second level of average high frequency resistance is achieved;
operating the stack with a predetermined cathode input relative humidity until a third level of average high frequency resistance is achieved, wherein operating the fuel cell with the cathode air flow so as to dry the plurality of fuel cell membranes is longer in duration than each of rehydrating the cell membranes of the stack and operating the stack with the predetermined cathode input relative humidity; and
shutting down the fuel cell system.

17. The method according to claim 16 wherein the cathode input relative humidity while operating the stack with the predetermined cathode input relative humidity is approximately 35%.

18. The method according to claim 16 wherein the ratio of the amount of time for drying the plurality of membranes to a predetermined average HFR within a predetermined window of time to the amount of time for rehydrating the cell membranes of the stack is at least 3:1.

19. The method according to claim 16 further comprising a procedure for aborting the shutdown if a restart of the fuel cell system is requested before shutdown completes and the measured high frequency resistance is below a predetermined level.

20. The method according to claim 16 wherein the predetermined cathode input relative humidity is achieved by increasing the cathode air flow above a predetermined level.

Assignees

• Clingerman Bruce J
• Rogahn Aaron
• Cai Jun
• Gerzseny Joseph C
• Sinha Manish
• Burch Steven D
• Alp Abdullah B
• Gm Global Tech Operations Inc

Inventors

• Clingerman Bruce J
• Rogahn Aaron
• Cai Jun
• Gerzseny Joseph C
• Sinha Manish
• Burch Steven D
• Alp Abdullah B

Classifications

• H01M8/04753

  of fuel cell reactants · CPC title

• H01M8/04955

  Shut-off or shut-down of fuel cells · CPC title

• H01M8/04529

  of the electrolyte · CPC title

• H01M8/04253

  Means for solving freezing problems · CPC title

• H01M8/04223 Primary

  during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells · CPC title