초록 ▼

For various reasons, it can be desirable to subject fuel cells to drying procedures. In solid polymer electrolyte fuel cells for instance, drying may be carried out prior to storing at below freezing temperatures, or to recover cell performance lost following freeze/thaw events. An improved drying m

For various reasons, it can be desirable to subject fuel cells to drying procedures. In solid polymer electrolyte fuel cells for instance, drying may be carried out prior to storing at below freezing temperatures, or to recover cell performance lost following freeze/thaw events. An improved drying method involves drying the cell uniformly throughout. That is, the drying power over the length of the fuel cell is adjusted to be essentially uniform. This can be accomplished by using an appropriate set of operating conditions. The improved drying method can improve the lifetime of the fuel cell.

대표청구항 ▼

What is claimed is: 1. A method of drying a fuel cell following a normal operating period, the fuel cell comprising a reactant flow field channel having an inlet and an outlet and a fuel cell length defined by the span from the channel inlet to the channel outlet, the method comprising: operating t

What is claimed is: 1. A method of drying a fuel cell following a normal operating period, the fuel cell comprising a reactant flow field channel having an inlet and an outlet and a fuel cell length defined by the span from the channel inlet to the channel outlet, the method comprising: operating the fuel cell for a normal operating period; subsequently varying at least one operating parameter to make total drying power over the fuel cell length vary by less than about 0.05 (Mol/sec)/(A/cm2) said total drying power being a combination of anode and cathode drying power, said at least one operating parameter being selected from the group consisting of: reactant operating pressure, pressure drop, flow rate, humidification level, stoichiometry and stack operating load; and operating the fuel cell for a drying period during which the total drying power over the fuel cell length varies by less than about 0.05 (Mol/sec)/(A/cm2). 2. The method of claim 1 wherein the variation in total drying power over the fuel cell length is less than about 0.005 (Mol/sec)/(A/cm2). 3. The method of claim 2 wherein the variation in drying power over the fuel cell length is less than about 0.0005 (Mol/sec)/(A/cm2). 4. The method of claim 1 wherein the total drying power over the fuel cell length is more than about 10−4 Mol/sec. 5. The method of claim 1 wherein the fuel cell is a solid polymer electrolyte fuel cell. 6. The method of claim 5 wherein the solid polymer electrolyte is a perfluorosulfonic acid polymer. 7. The method of claim 5 wherein the fuel cell comprises flow field channels for fuel and oxidant reactants and for a coolant and wherein the directions of flow for the oxidant reactant and coolant are opposite to that of the fuel reactant. 8. A method for recovering performance in a fuel cell following a freeze/thaw event comprising drying the fuel cell according to the method of claim 1. 9. The method of claim 8 comprising measuring the relative humidity in the oxidant exhaust and stopping the drying when the relative humidity reaches 80%. 10. A fuel cell system comprising a fuel cell and a control system, the fuel cell comprising a reactant flow field channel having an inlet and an outlet, a coolant channel having a direction of flow opposite to that of the reactant, and a fuel cell length defined by the span from the channel inlet to the channel outlet, wherein the reactant flow field channel and the coolant channel are linear and run parallel to the fuel cell length and the control system is configured to operate the fuel cell normally and subsequently dry the fuel cell by operating the fuel cell such that total drying power over the fuel cell length varies by less than about 0.05 (Mol/sec)/(A/cm2), wherein said total drying power is a combination of anode and cathode drying power, is achieved by varying at least one operating parameter to make the total drying power over the fuel cell length vary by less than about 0.05 (Mol/sec)/(A/cm2), said at least one operating parameter being selected from the group consisting of: reactant operating pressure, pressure drop, flow rate, humidification level, stoichiometry and stack operating load.