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A method and apparatus increase the temperature of a fuel cell via reactant starvation at one or both electrodes. Reactant starvation at an electrode results in increased internal heat generation under load. Starvation conditions can be prolonged or intermittent and can be obtained, for example, by

A method and apparatus increase the temperature of a fuel cell via reactant starvation at one or both electrodes. Reactant starvation at an electrode results in increased internal heat generation under load. Starvation conditions can be prolonged or intermittent and can be obtained, for example, by suitably reducing the supply rate of a reactant or by operating the fuel cell at sufficiently high current density so as to consume reactant faster than it is supplied. The method can allow for some generation of useful power by the fuel cell during start-up. The method is particularly suitable for starting up a solid polymer electrolyte fuel cell from temperatures below 0° C.

대표청구항 ▼

1. A method of operating a solid polymer electrolyte fuel cell comprising:supplying an oxidant reactant stream to the cathode electrode of said fuel cell;supplying a fuel reactant stream to the anode electrode of said fuel cell;monitoring a temperature parameter indicative of the operating temperatu

1. A method of operating a solid polymer electrolyte fuel cell comprising:supplying an oxidant reactant stream to the cathode electrode of said fuel cell;supplying a fuel reactant stream to the anode electrode of said fuel cell;monitoring a temperature parameter indicative of the operating temperature of said fuel cell; andwhen said temperature parameter is below a predetermined threshold value, reactant starving at least a portion of one of said electrodes. 2. The method of claim 1 wherein said reactant starving is intermittent. 3. The method of claim 1 wherein said reactant starving comprises interrupting the supply of one of said reactant streams to said respective fuel cell electrodes. 4. The method of claim 3 wherein said method comprises intermittently interrupting the supply of one of said reactant streams to said fuel cell electrodes. 5. The method of claim 3 wherein said one of said reactant streams is said fuel reactant stream. 6. The method of claim 3 wherein said one of said reactant streams is said oxidant reactant stream. 7. The method of claim 3 wherein said fuel cell is one of a plurality of fuel cells arranged in a fuel cell stack. 8. The method of claim 7 wherein said supply of one of said reactant streams to each of said plurality of fuel cells is not simultaneously interrupted. 9. The method of claim 1 wherein said method comprises connecting a transient electrical load to draw electrical power from said fuel cell. 10. The method of claim 9 wherein said method comprises intermittently connecting a transient electrical load to draw electrical power from said fuel cell. 11. The method of claim 9 wherein the rates of supply of said reactants to said fuel cell electrodes are not increased in response to the connection of said transient load. 12. The method of claim 9 wherein said fuel cell is one of a plurality of fuel cells arranged in a fuel cell stack, and the connection of said transient load to draw power from each one of said plurality of fuel cells is not simultaneous. 13. The method of claim 1 wherein said reactant streams are essentially free of electrocatalyst poisons. 14. The method of claim 13 wherein said fuel reactant stream is substantially pure hydrogen. 15. The method of claim 2 wherein said fuel cell is one of a plurality of fuel cells arranged in a fuel cell stack and said reactant starving causes a voltage reversal to occur in at least one of said plurality of fuel cells. 16. The method of claim 9 wherein said fuel cell is one of a plurality of fuel cells arranged in a fuel cell stack and said reactant starving causes a voltage reversal to occur in at least one of said plurality of fuel cells.