Mitigating electrode erosion in high temperature PEM fuel cell

Patent metadata

Field	Value
Publication number	US-9917314-B2
Application number	US-200913261129-A
Country	US
Kind code	B2
Filing date	Aug 28, 2009
Priority date	Aug 28, 2009
Publication date	Mar 13, 2018
Grant date	Mar 13, 2018

Abstract

A method of operating a fuel cell power plant ( 10 ) including a stack ( 11 ) of fuel cells having an anode catalyst layer and a cathode electrode ( 15 ) including a catalyst layer disposed on catalyst support material is characterized by, during normal operation of said power plant, adjusting the voltage of the stack to be substantially equal to or less than a predetermined maximum voltage for the temperature of the stack. Further, said step of adjusting comprises adjusting the stack voltage to the lesser of: a) a predetermined voltage above which corrosion of catalyst support material is significant and below which corrosion of catalyst support material is insignificant at the temperature of the stack; and b) a predetermined voltage above which dissolution of catalyst is significant and below which dissolution of the catalyst is insignificant at the temperature of the stack.

First claim

The invention claimed is:

1. A method of operating a fuel cell power plant including a stack of fuel cells having an electric output and coolant passages having inlets and outlets, each fuel cell comprising an electrolyte disposed between an anode catalyst layer and a cathode including a catalyst layer disposed on catalyst support material, an anode fuel flow field plate on the anode side of the electrolyte and a cathode air flow field plate on the cathode side of the electrolyte, the power plant also having:
a stack voltage sensor,
a stack temperature sensor,
a source providing hydrogen-containing fuel to the anode flow field plates,
an oxidant source providing oxidant to the cathode flow field plates,
a power conditioner connected between the electric output and a load,
a power plant controller; and
wherein said method comprises:
during normal operation of said power plant, adjusting the voltage of the stack to the lesser of:
a) a predetermined voltage above which corrosion of catalyst support material is significant at the temperature of the stack and below which corrosion of a catalyst support material is insignificant at the temperature of the stack; and
b) a predetermined voltage above which dissolution of catalyst is significant at the temperature of the stack and below which dissolution of the catalyst is insignificant at the temperature of the stack.

2. The method according to claim 1 wherein adjusting the voltage of the stack comprises adjusting the stack voltage to be substantially equal to or less than a predetermined voltage above which erosion of an electrode is significant at the temperature of the stack and below which erosion of the electrode is insignificant at the temperature of the stack.

3. The method according to claim 1 wherein adjusting the voltage of the stack comprises adjusting the electrical load on the stack.

4. The method according to claim 3 wherein the power plant controller responds to the stack temperature sensor to regulate the load to cause the voltage of the stack indicated by the stack voltage sensor to be substantially equal to or less than the predetermined voltage.

5. The method according to claim 1 wherein adjusting the voltage of the stack comprises adjusting current flow through an auxiliary load.

6. The method according to claim 1 wherein adjusting the voltage of the stack comprises adjusting the current flow through a variable resistance.

7. The method according to claim 1 wherein adjusting the voltage of the stack comprises adjusting current flow into an electric storage device.

8. The method according to claim 1 wherein the oxidant source is controllable; and wherein adjusting the voltage of the stack comprises regulating the oxidant flow to the cathode flow field to control the voltage of the stack.

9. The method according to claim 8 wherein the power plant controller responds to the stack temperature sensor to regulate oxidant flow to cause the voltage of the stack indicated by the stack voltage sensor to be substantially equal to or less than the predetermined voltage.

10. The method according to claim 1 wherein the power conditioner is connected between the electric output and the load; and wherein adjusting the voltage of the stack comprises operating the power conditioner so as to adjust the load on the stack.

11. The method according to claim 2 wherein the predetermined voltage above which erosion of an electrode is significant at the temperature of the stack and below which erosion of the electrode is insignificant at the temperature of the stack is less than or equal to 0.85 volts with respect to a hydrogen reference electrode when the temperature of the stack is 100 degrees Celsius.

12. The method according to claim 11 wherein the electrode includes a noble metal catalyst and a carbon support.

13. The method according to claim 2 wherein the predetermined voltage above which erosion of an electrode is significant at the temperature of the stack and below which erosion of the electrode is insignificant at the temperature of the stack is greater than or equal to 0.85 volts with respect to a hydrogen reference electrode when the temperature of the stack is 65 degrees Celsius.

14. The method according to claim 13 wherein the electrode includes a noble metal catalyst and a carbon support.

Assignees

• Darling Robert M
• Badrinarayanan Paravastu
• Reiser Carl A
• Audi Ag

Inventors

• Darling Robert M
• Badrinarayanan Paravastu
• Reiser Carl A

Classifications

• H01M8/04559

  of fuel cell stacks · CPC title

• H01M8/0488

  of fuel cell stacks · CPC title

• H01M8/0491

  of fuel cell stacks · CPC title

• H01M2008/1095

  Fuel cells with polymeric electrolytes · CPC title

• H01M8/04753

  of fuel cell reactants · CPC title