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A method is provided for reducing degradation in a fuel cell assembly, including at least one fuel cell with a PBI membrane, during standby, operation. The method may include electrochemically consuming an oxidant from a cathode coupled to the PBI membrane in response to a disconnection of an extern

A method is provided for reducing degradation in a fuel cell assembly, including at least one fuel cell with a PBI membrane, during standby, operation. The method may include electrochemically consuming an oxidant from a cathode coupled to the PBI membrane in response to a disconnection of an external load and supplying fuel to remove or electrochemically consume any back-diffused oxidant to the associated fuel cell sufficient to replace or consume the back-diffused oxidant while the external load is removed, and/or also may include controlling a standby temperature of the fuel cell. In this way, it may be possible to avoid increased cell voltage decay associated with degradation of the PBI in a simple and cost effective system.

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1. A method for reducing degradation in a fuel cell assembly including a polybenzimidazole (PBI) membrane doped with phosphoric acid, the method comprising: electrochemically consuming oxidant from a cathode coupled to the PBI membrane in response to a disconnection of an external load; andsupplying

1. A method for reducing degradation in a fuel cell assembly including a polybenzimidazole (PBI) membrane doped with phosphoric acid, the method comprising: electrochemically consuming oxidant from a cathode coupled to the PBI membrane in response to a disconnection of an external load; andsupplying fuel to maintain zero or near zero potential by removing any back-diffused oxidant to the associated anode or cathode electrode of the fuel cell sufficient to consume or replace the back-diffused oxidant while the external load is disconnected. 2. The method of claim 1 where the fuel is supplied without a supply of inert gas to the anode and/or cathode, and where the fuel is supplied at a predetermined rate. 3. The method of claim 2 further comprising reducing the fuel cell temperature to a predetermined temperature while maintaining low cell potential, where the predetermined temperature is lower than an operating temperature of the fuel cell. 4. The method of claim 1 further comprising discontinuing an oxidant supply in response to disconnection of the external load. 5. The method of claim 1 where the electrochemically consumed oxidant includes oxidant supplied during previous operation of the fuel cell in power delivery mode. 6. The method of claim 2 where an internal load is applied to the fuel cell to electrochemically consume the oxidant. 7. The method of claim 6 where the internal load is further applied during the removal of the back-diffused oxidant. 8. The method of claim 1 where the removal of the external load is determined when a detected voltage of the fuel cell is greater than or equal to a threshold value. 9. The method of claim 1 further comprising reducing the fuel cell temperature below a predetermined temperature; and maintaining the fuel cell temperature at the predetermined temperature while the external load is disconnected. 10. A fuel cell system, comprising: at least one fuel cell stack, where a plurality of cells in the stack include a polybenzimidazole (PBI) membrane electrolyte having an anode and a cathode;flow fields configured to supply air to the cathode and hydrogen to the anode of the fuel cell system;an external load;an internal load;a controller configured to detect disconnection of the external load and transition the system from power generation to a stand-by mode, stop a supply of oxidant, connect the internal load in response to the detected external load disconnection, the internal load reducing voltage of the fuel cell to substantially zero, maintain connection of the internal load while supplying hydrogen to the anode of the fuel cell, where the hydrogen is repeatedly supplied commensurate with a reaction of back-diffused oxygen at the cathode, and reducing a temperature of the fuel cell to a predetermined temperature, without supplying inert gasses during said maintenance of zero or near zero potential. 11. The fuel cell system of claim 10 where the system is coupled in a back-up power generation system, where the controller operates the fuel cell to provide back-up power in response to line voltage and/or current of a power system. 12. The fuel cell system of claim 10 where the hydrogen is repeatedly supplied at a predetermined rate. 13. The fuel cell system of claim 10 where the disconnection of the external load is detected when a voltage of the fuel cell is greater than or equal to a threshold value. 14. The method of claim 9, where temperature is reduced by adjusting the cooling fan. 15. The method of claim 6 further comprising detecting disconnection of the external load, and transitioning from power generation to a standby mode, stopping a supply of oxidant, connecting the internal load in response to the detected external load disconnection, maintaining connection of the internal load while repeatedly supplying hydrogen to the anode of the fuel cell, and supplying the hydrogen commensurate with the reaction of back-diffused oxygen at the cathode, without supplying inert gasses during maintenance of zero or near zero potential. 16. The method of claim 15 further comprising detecting the disconnection of the external load when a voltage of the fuel cell is greater than or equal to a threshold value.