Fuel cell and method for reducing electrode degradation during startup and shutdown cycles

Patent metadata

Field	Value
Publication number	US-9401523-B2
Application number	US-62131807-A
Country	US
Kind code	B2
Filing date	Jan 9, 2007
Priority date	Jan 9, 2007
Publication date	Jul 26, 2016
Grant date	Jul 26, 2016

Abstract

One embodiment of the invention includes a product comprising: a membrane electrolyte having a first face and a second face; and an anode over the first face and a cathode over the second face, and wherein the anode has a catalyst loading that is less than 50% of the catalyst loading of the cathode.

First claim

What is claimed is:

1. A method of starting up a fuel cell comprising:
providing a fuel cell comprising a membrane electrolyte having a first side, a second side, and a thickness; an anode over the first side of said membrane, a cathode over the second side of said membrane, an anode gas flow field and a cathode gas flow field, an oxidant gas residing in the flow fields of both the anode and the cathode, said anode having a thickness of less than about 10 μm and said cathode being at least twice as thick as said anode, said anode comprising a metal catalyst in an amount of about 0.02 to about 0.07 mg/cm 2 of the anode surface;
connecting said fuel cell anode to a fuel gas supply;
flowing a fuel gas through the flow field of said anode, the flow field of said anode having a ratio of anode flow field volume to anode electrode area that ranges from about 0.01 cm to 0.06 cm so that flowing the fuel gas through the flow field substantially replaces said oxidant gas, wherein i) the ratio of anode flow field volume to anode electrode area, ii) the thickness of said anode and said cathode, or iii) the amount of said metal catalyst of said anode or any combination of i, ii, and iii, provide a potential increase on the cathode during such gas change that is no more than about 0.1V in order to reduce electrode degradation;
connecting said fuel cell cathode to an oxidant gas supply; and
connecting said fuel cell to an external load.

2. A method of starting up a fuel cell as set forth in claim 1 , wherein said fuel gas is hydrogen and said oxidant gas is air.

3. A method of starting up a fuel cell as set forth in claim 2 , wherein said anode comprises a catalyst support having a BET surface area of about 200 m 2 /g or less.

4. A method of shutting down a fuel cell comprising:
providing a fuel cell comprising a membrane electrolyte, having a first side, a second side, and a thickness; an anode attached to the first side of said membrane, a cathode attached to the second side of said membrane, an oxidant gas flowing over the surfaces of said cathode through a defined cathode flow field and a fuel gas flowing over the surface of said anode in a defined anode flow field, said anode having a thickness of less than about 10 μm and said cathode being at least twice as thick as said anode, said anode comprising a metal catalyst in an amount of about 0.02 to about 0.07 mg/cm 2 of the anode surface;
disconnecting a fuel gas supply from said fuel cell; and
flowing said oxidant gas to the flow field of said anode, the flow field of said anode having a ratio of anode flow field volume to anode electrode area that ranges from about 0.01 cm to 0.06 cm so that flowing said oxidant gas through the flow field substantially replaces said fuel gas, wherein i) the ratio of anode flow field volume to anode electrode area, ii) the thickness of said anode and said cathode, or iii) the amount of said metal catalyst of said anode or any combination of i, ii, and iii, provide a potential increase on the cathode during such gas change that is no more than about 0.26V in order to reduce electrode degradation.

5. A method of shutting down a fuel cell as set forth in claim 4 , wherein said fuel gas is hydrogen and said oxidant gas is air.

6. A method of shutting down a fuel cell as set forth in claim 4 , wherein said anode comprises a catalyst support having a BET surface area of about 200 m 2 /g or less.

7. A method of shutting down a fuel cell comprising:
providing a fuel cell comprising a membrane electrolyte, having a first side, a second side, and a thickness; an anode attached to the first side of said membrane, a cathode attached to the second side of said membrane, an oxidant gas flowing over the surfaces of said cathode through a defined cathode flow field and a fuel gas flowing over the surface of said anode in a defined anode flow field, said anode having a thickness of less than about 10 μm and said cathode being at least twice as thick as said anode, said anode comprising a metal catalyst in an amount of about 0.02 to about 0.07 mg/cm 2 of the anode surface;
disconnecting a fuel gas supply from said fuel cell; and
flowing said oxidant gas to the flow field of said anode, the flow field of said anode having a ratio of anode flow field volume to anode electrode area that ranges from about 0.01 cm to 0.06 cm so that flowing said oxidant gas through the flow field substantially replaces said fuel gas, wherein the ratio of anode flow field volume to anode electrode area provides a potential increase on the cathode during such gas change that is no more than about 0.1V in order to reduce electrode degradation.

8. A method of shutting down a fuel cell comprising:
providing a fuel cell comprising a membrane electrolyte, having a first side, a second side, and a thickness; an anode attached to the first side of said membrane, a cathode attached to the second side of said membrane, an oxidant gas flowing over the surfaces of said cathode through a defined cathode flow field and a fuel gas flowing over the surface of said anode in a defined anode flow field, said anode having a thickness of less than about 10 μm and said cathode being at least twice as thick as said anode, said anode comprising a metal catalyst in an amount of about 0.02 to about 0.07 mg/cm 2 of the anode surface;
disconnecting a fuel gas supply from said fuel cell; and
flowing said oxidant gas to the flow field of said anode, the flow field of said anode having a ratio of anode flow field volume to anode electrode area that ranges from about 0.01 cm to 0.06 cm so that flowing said oxidant gas through the flow field substantially replaces said fuel gas, wherein the thickness of said anode and said cathode provides a potential increase on the cathode during such gas change that is no more than about 0.1V in order to reduce electrode degradation.

9. A method of shutting down a fuel cell comprising:
providing a fuel cell comprising a membrane electrolyte, having a first side, a second side, and a thickness; an anode attached to the first side of said membrane, a cathode attached to the second side of said membrane, an oxidant gas flowing over the surfaces of said cathode through a defined cathode flow field and a fuel gas flowing over the surface of said anode in a defined anode flow field, said anode having a thickness of less than about 10 μm and said cathode being at least twice as thick as said anode, said anode comprising a metal catalyst in an amount of about 0.02 to about 0.07 mg/cm 2 of the anode surface;
disconnecting a fuel gas supply from said fuel cell; and
flowing said oxidant gas to the flow field of said anode, the flow field of said anode having a ratio of anode flow field volume to anode electrode area that ranges from about 0.01 cm to 0.06 cm so that flowing said oxidant gas through the flow field substantially replaces said fuel gas, wherein the amount of said metal catalyst of said anode provides a potential increase on the cathode during such gas change that is no more than about 0.1V in order to reduce electrode degradation.

10. A method of shutting down a fuel cell comprising:
providing a fuel cell comprising a membrane electrolyte, having a first side, a second side, and a thickness; an anode attached to the first side of said membrane, a cathode attached to the second side of said membrane, an oxidant gas flowing over the surfaces of said cathode through a defined cathode flow field and a fuel gas flowing over the surface of said anode in a defined anode flow field, said anode having a thickness of less than about 10 μm and said cathode being at least twice as thick as said anode, said anode comprising a metal catalyst in an amount of about 0.02 to about 0.07 mg/

Assignees

• Swathirajan Swathy
• Merzougui Belabbes
• Yu Paul Taichiang
• Gm Global Tech Operations Llc

Inventors

• Swathirajan Swathy
• Merzougui Belabbes
• Yu Paul Taichiang

Classifications

• H01M4/92

  Metals of platinum group (H01M4/94 {, H01M4/9058} take precedence) · CPC title

• H01M4/8605

  Porous electrodes · CPC title

• H01M8/1004 Primary

  characterised by membrane-electrode assemblies [MEA] (H01M8/12 takes precedence) · CPC title

• H01M8/04223

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

• H01M4/926

  on carbon or graphite · CPC title