IP Library Granted Patent US 9,276,273
Granted Patent B2
US 9,276,273 · App. 13/642,309 · Granted Mar 1, 2016

Fuel cell water management via reduced anode reactant pressure

Inventors: Andrew J. L. Steinbach (St. Anthony Village, MN); Mark K. Debe (Stillwater, MN); Andrew T. Haug (St. Paul, MN)
Assignee: 3M Innovative Properties Company
H01M8/0247H01M4/926H01M4/928H01M8/04104H01M8/04156H01M8/04223H01M8/04753H01M8/04783H01M4/921H01M2008/1095Y02E60/50
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Quick Facts
Patent No.
US 9,276,273
App. No.
13/642,309
Granted
Mar 1, 2016
Kind
B2
Abstract

A method is provided for operation of a fuel cell with improved water management by maintaining reduced anode pressure relative to cathode pressure, relative to atmospheric pressure, or both. Typically, the fuel cell comprises a membrane electrode assembly comprising nanostructured thin film cathode catalyst.

Claims (16)

1. A method of operating a fuel cell comprising a membrane electrode assembly having an anode supplied with a gaseous anode reactant at an anode pressure and a cathode supplied with a gaseous cathode reactant at a cathode pressure, wherein the anode pressure is below atmospheric pressure.

2. The method according to claim 1 wherein the anode pressure is less than the cathode pressure by at least 50 kPa.

3. The method according to claim 1 wherein the anode pressure is less than the cathode pressure by at least 150 kPa.

4. The method according to claim 1 wherein the anode pressure is less than the cathode pressure by at least 200 kPa.

5. The method according to claim 1 wherein the difference between anode pressure and cathode pressure is maintained for at least 10 minutes of continuous service.

6. The method according to claim 1 wherein the anode pressure is lower than a maximum pressure which is 90 kPa or less.

7. The method according to claim 6 wherein the anode pressure is at least 10 kPa.

8. The method according to claim 6 wherein the anode pressure is maintained below the maximum pressure for at least 10 minutes of continuous service.

9. The method according to claim 6 wherein the anode pressure is maintained below the maximum pressure for <1 minute of continuous service.

10. The method according to claim 6 wherein the fuel cell comprises an anode flow field with a reactant pressure drop of <90 kPa wherein the anode pressure is maintained below the maximum pressure.

11. The method according to claim 6 wherein the fuel cell comprises an anode flow field with a reactant pressure drop of <50 kPa wherein the anode pressure is maintained below the maximum pressure.

12. The method according to claim 6 wherein the fuel cell comprises an anode flow field with a reactant pressure drop of <25 kPa wherein the anode pressure is maintained below the maximum pressure.

13. The method according to claim 6 wherein the fuel cell comprises an anode flow field with a reactant pressure drop of <10 kPa wherein the anode pressure is maintained below the maximum pressure.

14. The method according to claim 1 wherein the fuel cell comprises a membrane electrode assembly comprising nanostructured film cathode catalyst.

15. The method according to claim 1 wherein the fuel cell comprises a membrane electrode assembly comprising an anode gas diffusion layer and a cathode gas diffusion layer where a microporous layer of the anode GDL is thinner than a microporous layer of the cathode GDL.

16. The method according to claim 1 wherein the fuel cell system comprises a anode reactant recirculation system capable of maintaining anode reactant pressure less than atmospheric pressure.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 19, 2012
From: STEINBACH, ANDREW J. L.; DEBE, MARK K.; HAUG, ANDREW T.
To: 3M INNOVATIVE PROPERTIES COMPANY
Reel/Frame 029159/0825 →
Continuity (2)
Provisional Application 61328058 · Apr 26, 2010
Related Publication 20130040214A1 · Feb 14, 2013