Control system and method for starting a frozen fuel cell
View Patent ↗A method for starting a frozen fuel cell stack includes discontinuing reactant humidification before shutting down the fuel cell stack. The anode and cathode are purged with the dry reactants. The fuel cell stack is soaked at freezing temperatures. During subsequent startup, dry reactants are initially delivered. An outlet temperature of the anode and a current load of the fuel cell stack are measured. The dry reactants are shut off when the temperature of the anode outlet or the current load reach predetermined values. The open circuit voltage potential of the fuel cells is monitored and compared to a first voltage value. When the open circuit voltage exceeds the first value, the fuel cell stack begins supplying current load. The current load of the fuel cell stack is increased or decreased based on a difference between the minimum voltage and a second voltage value.
1. A method for operating a fuel cell stack that is subjected to freezing temperatures, comprising:
prior to a soak at freezing temperatures, terminating normal operation of said fuel cell stack;
discontinuing humidification of reactants supplied to at least one of an anode and a cathode of said fuel cell stack to provide non-humidified reactants; and
purging at least one of said anode and said cathode with said non-humidified reactants to clear inlet areas of said fuel cell stack.
2. The method of claim 1 further comprising draining coolant fluid from said fuel cell stack.
3. The method of claim 1 wherein said non-humidified reactants are delivered at a first flow rate for said first period.
4. The method of claim 3 wherein said first flow rate is between 0.1 and 25 sccm/cell/cm 2 .
5. The method of claim 3 wherein said first period is between 1 and 600 seconds.
6. The method of claim 2 further comprising soaking said fuel cell stack at freezing temperatures for a first period.
7. The method of claim 6 further comprising delivering non-humidified reactants to said fuel cell stack at a second flow rate.
8. The method of claim 7 wherein said second flow rate is between 1 and 100 sccm/cell/cm 2 .
9. The method of claim 7 wherein said second flow rate is sufficient to support a first current load that exceeds a typical current load that is encountered during operation.
10. The method of claim 7 further comprising:
delivering 25% airbleed to said anode; and
correcting hydrogen levels for consumption.
11. The method of claim 7 further comprising:
measuring an outlet temperature of said anode;
measuring a current load that is supplied by said fuel cell stack;
humidifying said reactants when at least one of said temperature of said anode outlet reaches a first predetermined temperature value and said current load reaches a first predetermined current load value.
12. The method of claim 11 further comprising verifying that fuel cells in said fuel cell stack have an open circuit voltage potential that is greater than a first predetermined voltage value.
13. The method of claim 12 further comprising:
applying a load to said fuel cell stack;
measuring a minimum voltage of fuel cells in said fuel cell stack; and
increasing said current load when said minimum voltage value exceeds a first calibration voltage value.
14. The method of claim 13 wherein a magnitude that said current load is increased is based on a difference between said minimum voltage value and said first calibration voltage value.
15. The method of claim 13 wherein said current load is increased in discrete steps.
16. The method of claim 13 further comprising decreasing said current load when said minimum voltage value is less than a second calibration voltage value.
17. The method of claim 16 wherein a magnitude that said current load is decreased is related to a difference between said minimum voltage value and said second calibration voltage value.
18. The method of claim 17 wherein said current load is decreased in discrete steps.
19. The method of claim 13 further comprising reducing said current load to a steady state current load that is encountered during normal driving conditions when said current load reaches a second predetermined current value.
20. A method for operating a fuel cell stack that is subjected to freezing temperatures, comprising:
prior to a soak at freezing temperatures, terminating normal operation of said fuel cell stack;
discontinuing humidification of reactants supplied to at least one of an anode and a cathode of said fuel cell stack to provide non-humidified reactants; and
purging at least one of said anode and said cathode with said non-humidified reactants to clear inlet areas of said fuel cell stack;
draining coolant fluid from said fuel cell stack;
soaking said fuel cell stack at freezing temperatures;
after said soak, delivering non-humidified reactants to said fuel cell stack at a second flow rate;
measuring at least one of an outlet temperature of said anode and a current load that is supplied by said fuel cell stack;
humidifying said reactants when said at least one of said temperature of said anode outlet reaches a first predetermined temperature value and said current load reaches a first predetermined current load value;
verifying that fuel cells in said fuel cell stack have an open circuit voltage potential that is greater than a first predetermined voltage value;
applying a load to said fuel cell stack;
measuring a minimum voltage of fuel cells in said fuel cell stack;
increasing said current load when said minimum voltage value exceeds a first calibration voltage value; and
decreasing said current load when said minimum voltage value is less than a second calibration voltage value.