Procedure for starting up a fuel cell system having an anode exhaust recycle loop

• US 20030129462A1
• Filed: 07/03/2002
• Published: 07/10/2003
• Est. Priority Date: 01/04/2002
• Status: Abandoned Application

• Current Assignee: UTC Fuel Cells, LLC
• Original Assignee: UTC Fuel Cells, LLC
• Inventors: Sawyer, Richard D., Yang, Deliang, Steinbugler, Margaret M., Reiser, Carl A., Van Dine, Leslie L.
• Application Number:
  US10/189,696
• Publication Number:
  US 20030129462A1
• Time in Patent Office: Days
• US Class Current: 429/17
• CPC Class Codes: H01M 16/003 of fuel cells with other electrochemical devices, e.g. capacitors, electrolysers
• CPC Class Codes: H01M 8/0258 characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
• CPC Class Codes: H01M 8/04007 related to heat exchange
• CPC Class Codes: H01M 8/04022 Heating by combustion
• CPC Class Codes: H01M 8/04097 with recycling of the reactants H01M8/04119, H01M8/04104 take precedence
• CPC Class Codes: H01M 8/04225 during start-up
• CPC Class Codes: H01M 8/04231 Purging of the reactants
• CPC Class Codes: H01M 8/04238 Depolarisation
• CPC Class Codes: H01M 8/04302 applied during start-up
• CPC Class Codes: H01M 8/241 with solid or matrix-supported electrolytes
• CPC Class Codes: H01M 8/2457 with both reactants being gaseous or vaporised
• CPC Class Codes: Y02E 60/50 Fuel cells

Abstract

A procedure for starting up a fuel cell system that is disconnected from its primary load and that has air in both its cathode and anode flow fields includes a) connecting an auxiliary resistive load across the cell to reduce the cell voltage; b) initiating a recirculation of the anode flow field exhaust through a recycle loop and providing a limited flow of hydrogen fuel into that recirculating exhaust; c) catalytically reacting the added fuel with oxygen present in the recirculating gases until substantially no oxygen remains within the recycle loop; disconnecting the auxiliary load; and then d) providing normal operating flow rates of fuel and air into respective anode and cathode flow fields and connecting the primary load across the cell. The catalytic reaction may take place on the anode or within a catalytic burner disposed within the recycle loop. The procedure allows start-up of the fuel cell system without the use of an inert gas purge while minimizing dissolution of the catalyst and corrosion of the catalyst support during the start-up process.

Claims

1. A procedure for starting-up a fuel cell system that is shut down, the shut down system comprising a source of hydrogen containing fuel, a fuel cell including a cathode flow field adjacent the cathode of the cell on one side of the cell electrolyte and an anode flow field adjacent the anode of the cell on the other side of the cell electrolyte, an anode recycle loop for recirculating at least a portion of the anode flow field exhaust through the anode flow field, wherein both the anode flow field and cathode flow field are filled with air, and the primary electricity using device is disconnected from the fuel cell external circuit, the start-up procedure comprising the steps of:

(A) initiating a recirculation, through the recycle loop, of the anode flow field exhaust, which is initially 100% air, and then providing a limited flow of hydrogen containing fuel into the recirculating anode exhaust to create a mixture of hydrogen and air within the recycle loop;

(B) catalytically reacting hydrogen and oxygen within the mixture on a catalyst within the recycle loop as the hydrogen and oxygen circulates through the recycle loop in contact with a catalyst to form water, and continuing to add hydrogen containing fuel to the recirculating mixture until substantially no oxygen remains in the recycle loop, including regulating the rate at which fuel is added such that the recirculating gases do not contain a flammable ratio of hydrogen and oxygen when they contact the catalyst or when the enter the anode flow field; and

,

(C) after substantially no oxygen remains in the recycle loop, (i) increasing the rate of fuel flow into the anode flow field to a normal operating flow rate, (ii) providing an oxidant into the cathode flow field at a normal operating flow rate, and, (iii) connecting the primary electricity using device to the external circuit.

2. The start-up procedure according to claim 1, wherein, in step (B), catalytically reacting hydrogen and oxygen includes passing the recirculating anode exhaust and hydrogen containing fuel into a burner disposed within the recycle loop, the burner including a catalytic element therein, and catalytically reacting hydrogen and oxygen on the catalytic element.

3. The start-up procedure according to claim 1, wherein, throughout step (B), the hydrogen containing fuel introduced into the recycle loop is mixed with the recirculating anode flow field exhaust, and that mixture is introduced into the anode flow field, whereupon oxygen is catalytically consumed at the cell anode in the presence of the hydrogen.

4. The start-up procedure according to claim 1, wherein prior to said step of providing a flow of hydrogen containing fuel in step (A), connecting an auxiliary resistive load across the cell to lower the cell voltage to a preselected value, and maintaining the cell voltage at or below the preselected value at least until substantially no oxygen remains in the recycle loop.

5. The shut-down procedure according to claim 4, wherein the auxiliary resistive load reduces the cell voltage to 0.2 volts per cell or less, and the cell voltage is maintained at or below 0.2 volts per cell until substantially no oxygen remains in the recycle loop.

6. The start-up procedure according to claim 5, wherein a diode is in series with the auxiliary load and limits the cell voltage to 0.2 volts per cell or less.

7. The start-up procedure according to claim 4, wherein during step (B) no air flow is provided to the cathode flow field while the auxiliary load is connected.

8. The start-up procedure according to claim 5, wherein the voltage is maintained at or below 0.2 volts per cell by a diode in series with the auxiliary load.

9. The start-up procedure according to claim 2, wherein prior to said step of providing a flow of hydrogen containing fuel in step (A), connecting an auxiliary resistive load across the cell to lower the cell voltage to a preselected value, and maintaining the cell voltage at or below the preselected value at least until substantially no oxygen remains in the recycle loop.

10. The start-up procedure according to claim 9, wherein said preselected value is 0.2 volts per cell.

11. The start-up procedure according to claim 9, wherein a diode is in series with the auxiliary load and limits the cell voltage to said preselected value throughout step (B).

12. The start-up procedure according to claim 4, wherein the amount of hydrogen containing fuel added in step (B) is regulated to maintain the amounts of hydrogen and oxygen entering the inlet of the anode flow field below the flammability limit.

13. The start-up procedure according to claim 1, wherein the recycle loop includes a plurality of burners disposed in series, and wherein in step (A), providing a flow of fuel includes providing a separate flow of fuel to each burner, wherein hydrogen and oxygen are catalytically consumed within each of the burners.

14. The start-up procedure according to claim 4, wherein said step (B) of catalytically reacting hydrogen and oxygen includes passing the recirculating anode exhaust through a plurality of burners arranged in series within the recycle loop, each burner including a catalytic element therein, and delivering a separate controlled flow of hydrogen containing fuel into each of the catalytic burners, and catalytically reacting said hydrogen and oxygen on each of the catalytic elements to produce water.

15. The start-up procedure according to claim 14, wherein the amount of reaction air added in step (B) is regulated to maintain the amounts of hydrogen and oxygen mixture below the flammability limit before it comes into contact with the burner catalytic element.

16. The start-up procedure according to claim 14, wherein the cell voltage is limited to 0.2 volts per cell or less throughout step (B).

17. The start-up procedure according to claim 16, wherein a diode is in series with the auxiliary load and limits the cell voltage to 0.2 volts per cell or less throughout step (B).

18. The start-up procedure according to claim 8, wherein in step (B) the controlled amount of hydrogen added into the recirculating anode exhaust is burned, in a difussion burning zone, with oxygen in said exhaust, upstream of said catalytic element, and the exhaust from said zone is directed over said catalytic element, wherein oxygen and hydrogen remaining in said diffusion burning zone exhaust catalytically react to form water.

19. The start-up procedure according to claim 17, wherein the hydrogen to oxygen mixture of said diffusion burning zone exhaust is below the flammability limit.

21. The start-up procedure according to claim 19, wherein the burners each have a catalytic element therein, and hydrogen and oxygen are catalytically converted to water on the elements.

23. The start-up procedure according to claim 21, wherein the rate of fuel flow into the burner is regulated to assure that the unburned gases leaving the diffusion zone of each burner, as well as the recirculating gases entering the anode flow field are always below the flammability limits.

24. The start-up procedure according to claim 12, wherein, in step(B), burning hydrogen and oxygen in a catalytic burner comprises passing the anode exhaust through a plurality of burners arranged in series, each burner including a catalytic element, and said step of providing fuel includes providing a separate flow of fuel for each catalytic burner in the series.

25. The start-up procedure according to claim 18, wherein the auxiliary resistive load reduces the cell voltage to 0.2 volts per cell or less, and the cell voltage is maintained at or below 0.2 volts per cell until substantially no oxygen remains in the recycle loop.

26. The start-up procedure according to claim 25, wherein a diode is in series with the auxiliary load and limits the cell voltage to 0.2 volts per cell or less.

20. A procedure for starting-up a fuel cell system that is shut down, the shut down system comprising a hydrogen containing fuel source, a fuel cell including a cathode flow field filled with air adjacent the cathode of the cell on one side of the cell electrolyte and an anode flow field filled with air adjacent the anode of the cell on the other side of the cell electrolyte, and an anode recycle loop for recirculating anode flow field exhaust through the anode flow field, the recycle loop including one or more burners, wherein during shut-down the primary electricity using device is disconnected from the fuel cell external circuit, the start-up procedure comprising the steps of:

(A) connecting an auxiliary resistive load across the cell;

(B) initiating a recirculation of anode flow field exhaust through the recycle loop, including through the burners;

(C) providing a controlled flow of hydrogen containing fuel into the burners and consuming, in each burner, (i) at least some of the oxygen in the anode exhaust and (ii) at least some of the fuel provided to the burners; and

(D) continuing the controlled flow of fuel into the burners and the recirculation of the anode flow field exhaust through the burners at least until there is substantially no oxygen remaining in the anode exhaust, and, thereafter, (i) providing a fuel flow to the anode flow field and air flow to the cathode flow field at normal operating flow rates, and (ii) connecting the primary electricity using device to the external circuit,

wherein the auxiliary load remains connected at least until there is substantially no oxygen remaining in the anode exhaust to limit the cell voltage during the start-up process.

22. The start-up procedure according to claim 20, wherein there is a diffusion burning zone within each burner upstream of the catalytic element of each burner, and the fuel added to each burner in step (C) is added to the diffusion zone where it is ignited and diffusion burns with oxygen in the recirculating anode exhaust gases passing through the burner.