Fuel cell reactant control
View Patent ↗The invention generally relates to controlling the temperature and relative humidity of an incoming fuel cell reactant stream. In one aspect, a fuel cell system is provided that includes a fuel cell having an anode inlet adapted to receive a flow of anode gas from an anode inlet conduit, and a cathode inlet adapted to receive a flow of cathode gas from a cathode inlet conduit. A first heat exchange surface is adapted to contact the flow of anode gas within the anode inlet conduit, and a second heat exchange surface adapted to contact the flow of cathode gas within the cathode inlet conduit. A coolant system is adapted to circulate a coolant through a coolant conduit. The coolant system is adapted to transfer heat from each of the first and second heat exchange surfaces to the coolant.
1. A fuel cell system, comprising:
a fuel cell comprising a polymer electrolyte membrane, the fuel cell having an anode inlet adapted to receive a flow of anode gas from an anode inlet conduit, and a cathode inlet adapted to receive a flow of cathode gas from a cathode inlet conduit;
a first heat exchange surface adapted to contact the flow of anode gas within the anode inlet conduit;
a second heat exchange surface adapted to contact the flow of cathode gas within the cathode inlet conduit; and
a coolant system adapted to circulate a coolant through a coolant conduit, wherein the coolant system is adapted to transfer heat from each of the first and second heat exchange surfaces to the coolant.
2. The system of claim 1 , wherein the coolant system further comprises a radiator adapted to remove heat from the coolant.
3. The system of claim 1 , wherein the fuel cell comprises a fuel cell stack.
4. The system of claim 1 , wherein the fuel cell has an operating temperature greater than a first temperature of the flow of anode gas at a location in the anode inlet conduit between the first heat exchange surface and the anode inlet of the fuel cell, and wherein the fuel cell operating temperature is greater than a second temperature of the flow of cathode gas at a location in the cathode inlet conduit between the second heat exchange surface and the cathode inlet of the fuel cell.
5. The system of claim 1 , wherein the fuel cell has an operating temperature less than a first temperature of the flow of anode gas at a location in the anode inlet conduit between the first heat exchange surface and the anode inlet of the fuel cell, and wherein the fuel cell operating temperature is less than a second temperature of the flow of cathode gas at a location in the cathode inlet conduit between the second heat exchange surface and the cathode inlet of the fuel cell.
6. The system of claim 4 , wherein the flow of anode gas at the fuel cell anode inlet has a relative humidity greater than 95%, and wherein the flow of cathode gas at the fuel cell cathode inlet has a relative humidity greater than 95%.
7. The system of claim 5 , wherein the flow of anode gas at the fuel cell anode inlet has a relative humidity greater than 95%, and wherein the flow of cathode gas at the fuel cell cathode inlet has a relative humidity greater than 95%.
8. The system of claim 5 , wherein the flow of anode gas at the fuel cell anode inlet has a relative humidity greater than 98%, and wherein the flow of cathode gas at the fuel cell cathode inlet has a relative humidity greater than 98%.
9. The system of claim 1 , wherein a first temperature of the flow of anode gas at a location in the anode inlet conduit between the first heat exchange surface and the anode inlet of the fuel cell is within 5.0° C. of a second temperature of the flow of cathode gas at a location in the cathode inlet conduit between the second heat exchange surface and the cathode inlet of the fuel cell.
10. The system of claim 1 , wherein the first heat exchange surface comprises a first heat exchanger adapted to transfer heat from the flow of anode gas to the coolant, and wherein the second heat exchange surface is a second heat exchanger adapted to transfer heat from the flow of cathode gas to the coolant.
11. The system of claim 10 , further comprising:
a first condensate drain adapted to remove condensate from the anode inlet conduit at a location between the first heat exchanger and the fuel cell anode inlet; and
a second condensate drain adapted to remove condensate from the cathode inlet conduit at a location between the second heat exchanger and the fuel cell cathode inlet.
12. The system of claim 1 , wherein the flow of anode gas comprises reformate.
13. The system of claim 1 , wherein the flow of cathode gas comprises air, and wherein the cathode inlet conduit is connected to an outlet of an enthalpy wheel.
14. The system of claim 1 , wherein the flow of cathode gas comprises air, and wherein the cathode inlet conduit is connected to an outlet of a cathode gas humidifier.
15. The system of claim 1 , wherein the flow of anode gas at a location in the anode inlet conduit between the first heat exchange surface and the anode inlet of the fuel cell has a first dew point temperature;
wherein the flow of cathode gas at a location in the cathode inlet conduit between the second heat exchange surface and the cathode inlet of the fuel cell has a second dew point temperature; and
wherein the fuel cell has an operating temperature within 5.0° C. of each of the first and second dew point temperatures.