Dynamic cathode gas control for a fuel cell system
View Patent ↗A fuel cell system utilizes at least one flow restricting device to vary the stoichiometric quantity of cathode reactant flowing to two discrete cathode sides of the fuel cell system. The varying of the stoichiometric quantity of cathode reactant can be between two predetermined values. The varying of the stoichiometric quantity can be during a steady state power demand placed on the system and/or during transients in a power demand placed on the system. The airmover that supplies the cathode reactant stream can be operated in a substantially continuous manner during a continuous power demand placed on the fuel cell system.
1. A method of operating a fuel cell system having at least one fuel cell stack and at least two discrete cathode sides, the method comprising:
(a) determining a first power demand on the at least one fuel cell stack;
(b) determining first and second stoichiometric quantities of cathode reactant to supply to at least one of the at least two cathode sides based on the first power demand;
(c) supplying a cathode reactant stream;
(d) routing a first portion of said cathode reactant stream to a first one of the cathode sides via a first cathode reactant flow path;
(e) routing a second portion of said cathode reactant stream to a second one of the cathode sides via a second cathode reactant flow path; and
(f) varying a quantity of cathode reactant in at least one of said first and second portions of said cathode reactant stream between the determined first and second stoichiometric quantities, which remain unchanged as a power demand on the fuel cell stack remains constant at the first power demand, such that at least one of the first and second cathode sides receives cathode reactant at a quantity that varies back and forth between the first and second stoichiometric quantities over time while the power demand on the fuel stack remains constant at the first power demand.
2. The method of claim 1 , wherein (f) includes changing a flow resistance in said flow paths.
3. The method of claim 2 , wherein changing a flow resistance in said flow paths includes changing a flow resistance in said flow paths downstream of the cathode sides.
4. The method of claim 2 , wherein changing a flow resistance in said flow paths includes changing a flow resistance in said flow paths upstream of the cathode sides.
5. The method of claim 2 , wherein changing a flow resistance in said flow paths includes changing a flow resistance in said flow paths both upstream and downstream of the cathode sides.
6. The method of claim 2 , wherein the fuel cell system includes at least two valves communicating with the cathode flow paths and changing a flow resistance in said flow paths includes operating said at least two valves to change said flow resistance.
7. The method of claim 1 , wherein (f) includes maintaining a minimum stoichiometric flow rate of cathode reactant into each of the cathode sides.
8. The method of claim 1 , wherein (f) is performed during substantially steady state power demand placed on the fuel cell system.
9. The method of claim 1 , wherein (f) is performed during transients in a power demand placed on the fuel cell system.
10. The method of claim 1 , wherein (f) includes varying said quantity of cathode reactant at a predetermined frequency.
11. The method of claim 1 , wherein (f) includes varying said quantity of cathode reactant in each of said first and second portions between the determined first and second stoichiometric quantities such that both of the first and second cathode sides receive cathode reactant at a quantity that varies back and forth between the first and second stoichiometric quantities over time while a power demand on the fuel stack remains at the first power demand.
12. The method of claim 1 , wherein said at least one fuel cell stack is at least two fuel cell stacks and the first and second cathode sides are associated with a respective first and second one of the fuel cell stacks, (d) includes routing a first portion of said cathode reactant stream to the cathode side of the first one of the fuel cell stacks via said first cathode reactant flow path, and (e) includes routing a second portion of said cathode reactant stream to the cathode side of the second one of the fuel cell stacks via said second cathode reactant flow path.
13. The method of claim 12 , further comprising:
routing a portion of a cathode effluent exiting said first fuel cell stack to the cathode side of said second fuel cell stack;
routing a portion of a cathode effluent exiting said second fuel cell stack to the cathode side of said first fuel cell stack; and
varying said routing of said cathode effluent to the cathode sides of said first and second fuel cell stacks.
14. The method of claim 1 , wherein (e) includes routing a remaining portion of said cathode reactant stream to the second cathode side.
15. A method of operating a fuel cell system having at least one fuel cell stack and at least two discrete cathode sides, the method comprising:
(a) supplying a cathode reactant stream of a constant value;
(b) routing a first portion of said cathode reactant stream to a first one of the cathode sides via a first cathode reactant flow path;
(c) routing a second portion of said cathode reactant stream to a second one of the cathode sides via a second cathode reactant flow path; and
(d) varying a stoichiometric quantity of cathode reactant in at least one of said first and second portions of said cathode reactant stream between two predetermined stoichiometric magnitudes which remain unchanged while a power demand on the at least one fuel cell stack remains at a constant level,
wherein the fuel cell system includes an airmover and (a) includes supplying said cathode reactant stream with said airmover and operating said airmover at a substantially constant rate while the power demand remains at the constant level and the stoichiometric quantity is varied.
16. A fuel cell system comprising:
at least one fuel cell stack;
at least two cathode sides;
first and second cathode reactant flow paths communicating with a respective first and second of said cathode sides;
an airmover operable to supply a cathode reactant stream to said cathode sides to meet a power demand;
a first portion of said cathode reactant stream flowing through said first flow path and said first cathode side;
a second portion of said cathode reactant stream flowing through said second flow path and said second cathode side; and
at least two flow restricting devices communicating with said flow paths, said flow restricting devices selectively varying a quantity of cathode reactant in at least one of said first and second portions of said cathode reactant stream between first and second stoichiometric values which remain unchanged while a power demand on the at least one fuel cell stack remains at a constant level such that the quantity of cathode reactant in at least one of the first and second portions varies back and forth between the first and second stoichiometric values.
17. The fuel cell system of claim 16 , wherein said at least two flow restricting devices vary said stoichiometric quantity by varying a flow resistance in said flow paths.
18. The fuel cell system of claim 17 , wherein said at least two flow restricting devices vary a flow resistance in said flow paths downstream of said cathode sides.
19. The fuel cell system of claim 17 , wherein said at least two flow restricting devices vary a flow resistance in said flow paths both upstream and downstream of said cathode sides.
20. The fuel cell system of claim 17 , wherein said at least two flow restricting devices vary a flow resistance in said flow paths upstream of said cathode sides.
21. The fuel cell system of claim 16 , wherein said at least two flow restricting devices vary said quantity of cathode reactant in said first and second flow paths at a predetermined frequency.
22. The fuel cell system of claim 21 , wherein said predetermined frequency and said first and second stoichiometric values are based on a look-up table.
23. The fuel cell system of claim 16 , wherein said at least one fuel cell stack is at least two fuel cell stacks each having a cathode side and an anode side, and said first and second cathode sides are associated with a respective first and second of said fuel cell stacks.
24. The fuel cell system of claim 23 , further comprising:
a first cathode effluent recycle flow path extending between said first cathode reactant flow path downstream of said first fuel cell stack and said second cathode reactant flow path upstream of said second fuel cell stack;
a second cathode effluent recycle flow path extending between said second cathode reactant flow path downstream of said second fuel cell stack and said first cathode reactant flow path upstream of said first fuel cell stack; and
first and second recycle flow restricting devices operable to selectively restrict flow through said respective first and second cathode effluent recycle flow paths to control a quantity of cathode effluent flowing from one of said fuel cell stacks to another of said fuel cell stacks.
25. The fuel cell system of claim 16 , wherein said airmover operates at a substantially constant speed during a substantially steady state power demand on the at least one fuel cell stack and while the quantity of cathode reactant in at least one of the first and second portions is varied.
26. The fuel cell system of claim 16 , wherein said at least two flow restricting devices maintain a pressure differential between an anode side and a cathode side of said fuel cell stack below a predetermined magnitude.
27. The fuel cell system of claim 16 , wherein said first and second stoichiometric values of cathode reactant are the same for both of said first and second portions.
28. The fuel cell system of claim 16 , wherein said at least two flow restricting devices vary said quantity of cathode reactant in said first and second portions of said cathode reactant stream during a substantially steady state power demand placed on the fuel cell system.
29. The fuel cell system of claim 16 , wherein said at least two flow restricting devices vary said quantity of cathode reactant in said first and second portions of said cathode reactant stream during a transient in a power demand placed on the fuel cell system.