Method for operating a fuel cell system, and fuel cell system
The invention relates to a method for operating a fuel cell system, in particular a PEM fuel cell system, in which an anode gas is supplied to an anode ( 1 ) of a fuel cell via a supply path ( 2 ), and is fed back via a recirculation path ( 3 ) connected to the anode ( 1 ), wherein hydrogen is used as the anode gas. According to the invention, during the start up of the fuel cell system, the anode gas is supplied to a drying device ( 4 ), in particular an adsorber, via at least one normally open valve ( 8, 9, 10 ), and water is extracted from the anode gas using the drying device ( 4 ). The invention also relates to a fuel cell system, in particular a PEM fuel cell system, which is suitable for carrying out the method.
1. A method for operating a fuel cell system in which an anode gas is supplied to an anode ( 1 ) of a fuel cell via a supply path ( 2 ), and the anode gas from the anode ( 1 ) is recirculated via a recirculation path ( 3 ) connected to the anode ( 1 ), wherein hydrogen is used as the anode gas, wherein, during a starting of the fuel cell system, the anode gas is supplied from the supply path ( 2 ) to a drying device ( 4 ) via at least one normally open valve ( 8 , 9 , 10 ), and water is extracted from the anode gas using the drying device ( 4 ), wherein an inlet of the recirculation path ( 3 ) and an outlet of the recirculation path ( 3 ) each extend from the supply path ( 2 ) such that the recirculation path ( 3 ) is upstream of the anode ( 1 ).
2. The method as claimed in claim 1 , wherein, during an operating shutdown of the fuel cell system, the anode gas is supplied to the drying device ( 4 ) via at least one normally open valve ( 8 , 9 , 10 ), and water is extracted from the anode gas using the drying device ( 4 ), wherein an operation of a blower ( 5 ) arranged in the recirculation path ( 3 ) is maintained.
3. The method as claimed in claim 1 , wherein water is removed from the drying device ( 4 ) by desorption during the operation of the fuel cell system.
4. The method as claimed in claim 3 , wherein, to promote desorption during the operation of the fuel cell system, fresh anode gas is supplied to the drying device ( 4 ) from a tank ( 6 ) and/or the drying device ( 4 ) is heated by a heating device ( 7 ).
5. A fuel cell system comprising at least one fuel cell having an anode, which is connected on an inlet side to a supply path ( 2 ) for supplying an anode gas and on an outlet side to a recirculation path ( 3 ) for recirculating the anode gas, wherein a drying device ( 4 ) is connected to the supply path ( 2 ) via at least one normally open valve ( 8 , 9 , 10 ), wherein the drying device is arranged in parallel with the anode ( 1 ) in a path that extends from the supply path ( 2 ) to the recirculation path ( 3 ), bypassing the anode ( 1 ).
6. The fuel cell system as claimed in claim 5 , wherein the drying device ( 4 ) is connected to the supply path ( 2 ) via at least one normally open valve ( 8 , 9 ) and can be connected to the recirculation path ( 3 ) via a check valve ( 11 ) opening in a direction of the recirculation path ( 3 ).
7. The fuel cell system as claimed in claim 5 , wherein an ejector pump ( 12 ) is arranged in the supply path ( 2 ) and/or a blower ( 5 ) is arranged in the recirculation path ( 3 ) to promote the recirculation of the anode gas.
8. The fuel cell system as claimed in claim 5 , wherein the drying device ( 4 ) has a heating device ( 7 ).
9. The fuel cell system as claimed in claim 5 , wherein the drying device ( 4 ) comprises a container which is filled with zeolite and is designed to be permeable to the anode gas at least in some region or regions.
10. The method as claimed in claim 1 , wherein the fuel cell system is a PEM fuel cell system.
11. The method as claimed in claim 1 , wherein the drying device ( 4 ) is an adsorber.
12. The fuel cell system as claimed in claim 5 , wherein the fuel cell system is a PEM fuel cell system.
13. The fuel cell system as claimed in claim 5 , wherein the drying device ( 4 ) is an adsorber.
14. The fuel cell system as claimed in claim 9 , wherein the zeolite in the container is configured as a bed.
15. The method as claimed in claim 1 , wherein the anode gas is supplied to the supply path ( 2 ) via a tank ( 6 ) and is supplied from the supply path ( 2 ) to the drying device ( 4 ) at a location between the tank ( 6 ) and the anode ( 1 ).
16. The method as claimed in claim 15 , wherein the recirculation path ( 3 ) terminates at the supply path ( 2 ) at a location between the tank ( 6 ) and the anode ( 1 ).
17. The fuel cell system as claimed in claim 5 , wherein the anode gas is supplied to the supply path ( 2 ) via a tank ( 6 ) and is supplied from the supply path ( 2 ) to the drying device ( 4 ) at a location between the tank ( 6 ) and the anode ( 1 ).
18. The fuel cell system as claimed in claim 17 , wherein the recirculation path ( 3 ) terminates at the supply path ( 2 ) at a location between the tank ( 6 ) and the anode ( 1 ).