Hydrogen passivation shut down system for a fuel cell power plant
View Patent ↗The invention is a hydrogen passivation shut down system for a fuel cell power plant ( 10, 200 ). During shut down of the plant ( 10, 200 ), hydrogen fuel is permitted to transfer between an anode flow path ( 24, 24 ′) and a cathode flow path ( 38, 38 ′). A passive hydrogen bleed line ( 202 ) permits passage of a smallest amount of hydrogen into the fuel cell ( 12′ ) necessary to maintain the fuel cell ( 12′ ) in a passive state. A diffusion media ( 204 ) may be secured in fluid communication with the bleed line ( 202 ) to maintain a constant, slow rate of diffusion of the hydrogen into the fuel cell ( 12′ ) despite varying pressure differentials between the shutdown fuel cell ( 12′ ) and ambient atmosphere adjacent the cell ( 12′ ).
1. A passive hydrogen bleed hydrogen passivation shut-down system for a fuel cell power plant ( 200 ), the system comprising:
a. at least one fuel cell ( 12 ′) for generating electrical current from hydrogen containing reducing fluid fuel and oxygen containing oxidant reactant streams, the fuel cell ( 12 ′) including an anode catalyst ( 14 ′) and a cathode catalyst ( 16 ′) on opposed sides of an electrolyte ( 18 ′), an anode flow path ( 24 ′) in fluid communication with the anode catalyst ( 14 ′) for directing the hydrogen fuel to flow through the fuel cell ( 12 ′) and adjacent the anode catalyst ( 14 ′), and a cathode flow path ( 38 ′) in fluid communication with the cathode catalyst ( 16 ′) for directing the oxidant stream to flow through the fuel cell ( 12 ′) and adjacent the cathode catalyst ( 14 ′);
b. a hydrogen inlet valve ( 52 ′) secured in fluid communication with a hydrogen feed line ( 55 ′) that is secured between a fuel source ( 54 ′) and the anode catalyst ( 14 ′) for selectively directing flow of the hydrogen fuel from the fuel source ( 54 ′) through the feed line ( 55 ′) and hydrogen inlet valve ( 52 ′) to the anode catalyst ( 14 ′);
c. an oxidant inlet valve ( 56 ′) secured in fluid communication with an oxidant feed line ( 62 ′) extending between an oxidant supply source ( 58 ′) and the cathode flow field ( 42 ′);
d. hydrogen transfer means secured in communication between the anode flow path ( 24 ′) and the cathode flow path ( 38 ′) for selectively permitting transfer of the hydrogen fuel between the anode flow path ( 24 ′) and the cathode flow path ( 38 ′); and,
e. a passive hydrogen bleed line ( 202 ) secured to the hydrogen fuel source ( 54 ′) and extending from the hydrogen fuel source ( 54 ′) to be secured to the anode flow path ( 24 ′) at a location on the anode flow path ( 24 ′) that is between the hydrogen inlet valve ( 52 ′) and the anode catalyst ( 14 ′), the passive hydrogen bleed line ( 202 ) consisting of a diffusion media ( 204 ) secured within a chamber ( 206 ) and a through flow defined by the passive hydrogen bleed line ( 202 ) for permitting consistent flow of the hydrogen from the hydrogen fuel source ( 54 ′) through the diffusion media ( 204 ) to the anode flow path ( 24 ′), wherein the passive hydrogen bleed line ( 202 ) is configured to permit passage through the bleed line ( 202 ) of hydrogen from the hydrogen fuel source ( 54 ′) to the anode flow path ( 24 ′) when the hydrogen inlet valve ( 52 ′) is in either of a closed position and an open position, and the passive hydrogen bleed line ( 202 ) is also configured to permit passage of hydrogen from the hydrogen fuel source ( 54 ′) to the anode flow path ( 24 ′) through the bleed line ( 202 ) of a lowest flow rate of hydrogen necessary to maintain the fuel cell ( 12 ′) in a passive state.
2. The system of claim 1 , wherein the diffusion media ( 204 ) is selected from the group consisting of a palladium membrane, a polymer membrane and a glass membrane, the membranes being of sufficient thickness to withstand a pressure differential between the fuel storage source ( 54 ′) and the anode flow path ( 24 ′).
3. A method of shutting down the fuel cell power plant ( 200 ) of claim 1 , the power plant ( 200 ) including at least one fuel cell ( 12 ′) for generating electrical current from hydrogen containing reducing fluid fuel and oxygen containing oxidant reactant streams, the fuel cell ( 12 ′) including the anode catalyst ( 14 ′) and the cathode catalyst ( 16 ′) on opposed sides of the electrolyte ( 18 ′), the anode flow path ( 24 ′) in fluid communication with the anode catalyst ( 14 ′) for directing the hydrogen fuel to flow through the fuel cell ( 12 ′) and adjacent the anode catalyst ( 14 ′), and the cathode flow path ( 38 ′) in fluid communication with the cathode catalyst ( 16 ′) for directing the oxidant stream to flow through the fuel cell ( 12 ′) and adjacent the cathode catalyst ( 14 ′), the method comprising:
a. disconnecting a primary load ( 90 ′) from the fuel cell ( 12 ′);
b. terminating flow of the oxidant into the cathode flow path ( 24 ′) from an oxidant source ( 58 ′);
c. connecting an auxiliary load ( 94 ′) to the fuel cell ( 12 ′);
d. permitting transfer of the hydrogen fuel from the anode flow path ( 24 ′) into the cathode flow path ( 38 ′);
e. closing a hydrogen inlet valve ( 52 ′) to terminate flow of the hydrogen fuel into the anode flow path ( 24 ′) from a hydrogen fuel source ( 54 ′) through a hydrogen feed line ( 55 ′) whenever the anode flow path ( 24 ′) and cathode flow path ( 38 ′) are filled above an acceptable limit of hydrogen to maintain the fuel cell ( 12 ′) in a passive state; and,
f. directing a consistent flow of hydrogen from the hydrogen fuel source ( 54 ′) through the passive hydrogen bleed line ( 202 ) and through the diffusion media ( 204 ) of the passive hydrogen bleed line ( 202 ) into the anode flow path ( 24 ′) at a location on the anode flow path ( 24 ′) that is between the hydrogen inlet valve ( 52 ′) and the anode catalyst ( 14 ′) and at a lowest flow rate of hydrogen necessary to maintain the fuel cell ( 12 ′) in a passive state.
4. The method of claim 3 , further comprising directing flow of the hydrogen through a diffusion media ( 204 ) secured in fluid communication with the passive hydrogen bleed line ( 202 ) so that hydrogen passing through passive hydrogen bleed line ( 202 ) must pass through the diffusion media ( 204 ) prior to passing into the anode flow path ( 24 ′).
5. The method of claim 4 , further comprising securing the diffusion media ( 204 ) within the fuel storage source ( 54 ′) adjacent the passive hydrogen bleed line ( 202 ).
6. The method of claim 4 , further comprising securing the diffusion media ( 204 ) within a diffusion chamber ( 206 ) secured in fluid communication with the passive hydrogen bleed line ( 202 ).
7. A passive hydrogen bleed hydrogen passivation shut-down system for a fuel cell power plant ( 200 ), the system comprising:
a. at least one fuel cell ( 12 ′) for generating electrical current from hydrogen containing reducing fluid fuel and oxygen containing oxidant reactant streams, the fuel cell ( 12 ′) including an anode catalyst ( 14 ′) and to cathode catalyst ( 16 ′) on opposed sides of an electrolyte ( 18 ′), an anode flow path ( 24 ′) in fluid communication with the anode catalyst ( 14 ′) for directing the hydrogen fuel to flow through the fuel cell ( 12 ′) and adjacent the anode catalyst ( 14 ′), and a cathode flow path ( 38 ′) in fluid communication with the cathode catalyst ( 16 ′) for directing the oxidant stream to flow through the fuel cell ( 12 ′) and adjacent the cathode catalyst ( 14 ′);
b. a hydrogen inlet valve ( 52 ′) secured in fluid communication with a hydrogen feed line ( 55 ′) that is secured between a fuel source ( 54 ′) and the anode catalyst ( 14 ′) for selectively directing flow of the hydrogen fuel from the fuel source ( 54 ′) through the feed line ( 55 ′) and hydrogen inlet valve ( 52 ′) to the anode catalyst ( 14 ′);
c. an oxidant inlet valve ( 56 ′) secured in fluid communication with on oxidant feed line ( 62 ′) extending between an oxidant supply source ( 58 ′) and the cathode flow field ( 42 ′);
d. hydrogen transfer means secured in communication between the anode flow path ( 24 ′) and the cathode flow path ( 38 ′) for selectively permitting transfer of the hydrogen fuel between the anode flow path ( 24 ′) and the cathode flow path ( 38 ′); and,
e. a passive hydrogen bleed line ( 202 ) secured to the hydrogen fuel source ( 54 ′) and extending from the hydrogen fuel source ( 54 ′) to be secured to the anode flow path ( 24 ′) at a location on the anode flow path ( 24 ′) that is between the hydrogen inlet valve ( 52 ′) and the anode catalyst ( 14 ′), the passive hydrogen bleed line ( 202 ) consisting of a through flow defined by the passive bleed line ( 202 ) for permitting consistent flow of the hydrogen from the hydrogen fuel source ( 54 ′) to the anode flow path ( 24 ′), wherein the passive hydrogen bleed line ( 202 ) is configured to permit passage through the bleed line ( 202 ) of hydrogen from the hydrogen fuel source ( 54 ′) to the anode flow path ( 24 ′) when the hydrogen inlet valve ( 52 ′) is in either of a closed position and an open position, and the passive hydrogen bleed line ( 202 ) is also configured to permit passage of hydrogen from the hydrogen fuel source ( 54 ′) to the anode flow path ( 24 ′) through the bleed line ( 202 ) of a lowest flow rate of hydrogen necessary to maintain the fuel cell ( 12 ′) in a passive state.