Operation of fuel cell systems with reduced carbon formation and anode leading edge damage

• US 9,287,571 B2
• Filed: 07/22/2009
• Issued: 03/15/2016
• Est. Priority Date: 07/23/2008
• Status: Active Grant

• Current Assignee: Bloom Energy Corporation
• Original Assignee: Bloom Energy Corporation
• Inventors: McElroy, James F., Weingaertner, David, Venkataraman, Swaminathan, Couse, Stephen
• Primary Examiner(s): Ruddock, Ula C
• Assistant Examiner(s): PARSONS, THOMAS H
• Application Number:
  US12/507,670
• Publication Number:
  US 20100047637A1
• Time in Patent Office: 2,428 Days
• Field of Search: 429/415, 429/420, 429/423, 429/514, 429/457, 429/458, 429/459, 429/465, 429/460, 429/469, 429/483
• US Class Current: 1/1
• CPC Class Codes: H01M 2008/1293 Fuel cells with solid oxide electrolytes
• CPC Class Codes: H01M 8/0618 Reforming processes, e.g. autothermal, partial oxidation or steam reforming
• CPC Class Codes: H01M 8/0637 Direct internal reforming at the anode of the fuel cell
• CPC Class Codes: Y02E 60/50 Fuel cells

Abstract

A method of operating a fuel cell system includes introducing a fuel mixture comprising hydrogen, fuel, and steam at a fuel inlet of the fuel cell system, and operating the fuel cell system to generate electricity. A ratio of hydrogen to carbon from fuel (H₂:C_fuel) in the fuel mixture is within a range of 0.25:1 to 3:1, inclusive; and a ratio of steam to carbon (S:C) in the fuel mixture is less than 2:1.

Claims

1. A method of operating a fuel cell system, comprising:

introducing a fuel mixture comprising molecular hydrogen, a fuel comprising carbon and hydrogen, and steam at a fuel inlet of a fuel cell of the fuel cell system, said fuel mixture comprising an output of an external reformer that reforms a hydrocarbon fuel to form molecular hydrogen, and the external reformer is coupled to the fuel inlet of the fuel cell of the fuel cell system; and

operating the fuel cell system to generate electricity,

wherein a ratio of molecular hydrogen not contained in fuel to carbon contained in the fuel (H2;

C_fuel) in said fuel mixture introduced at the fuel inlet of the fuel cell is within a range of 0.25;

1 to 3;

1, inclusive; and

a ratio of steam to carbon (S;

C) in said fuel mixture introduced at the fuel inlet of the fuel cell is less than 2;

1.

2. The method of claim 1, wherein said fuel is selected from the group consisting of methane, natural gas, propane, alcohol, or syngas derived from coal or natural gas reformation.

3. The method of claim 1, wherein said fuel cell system is a solid oxide fuel cell system.

4. The method of claim 3, wherein said fuel cell system comprises a solid oxide fuel cell system with an internal reformer.

5. The method of claim 1, wherein said S:

C ratio is less than or equal to 1.2;

1.

6. The method of claim 1, wherein said H₂:

C_fuel ratio is within the range of 0.5;

1 to 1.5;

1.

7. The method of claim 6, wherein the recycled anode exhaust gas is up to 70% of the total anode exhaust gas.

8. The method of claim 7, wherein the recycled anode exhaust gas is 50% to 70% of the total anode exhaust gas.

9. The method of claim 6, further comprising converting steam to hydrogen in all or a portion of anode exhaust gas using a water-gas shift reactor prior to reintroduction of all or a portion of the reformed anode exhaust gas into the fuel cell system.

10. The method of claim 1, wherein a source of said molecular hydrogen is recycled anode exhaust gas.

11. A method of operating a fuel cell system, comprising:

partially reforming a hydrocarbon fuel in an external reformer that is coupled to a fuel inlet of a fuel cell of the fuel cell system;

introducing a fuel mixture comprising the partially reformed hydrocarbon fuel from the external reformer and recycled anode exhaust gas and including steam at the fuel inlet of the fuel cell of the fuel cell system, wherein a portion of the hydrocarbon fuel reformed in the external reformer prior to introduction at the fuel inlet is 5% to 15%; and

operating the fuel cell system to generate electricity;

wherein the steam to carbon ratio (S;

C) in said fuel mixture introduced at the fuel inlet of the fuel cell is 1;

1 or greater and less than 2;

1.

12. The method of claim 11, wherein said reforming a portion of said fuel is conducted with a catalytic reactor.

13. The method of claim 11, wherein the recycled anode exhaust gas is up to 70% of the total anode exhaust gas.

14. The method of claim 11, wherein an average cell voltage of the fuel cell system is increased as compared to operation of the fuel cell system operating at S:

C greater than or equal to 2;

1.

15. The method of claim 11, further comprising converting steam to hydrogen in anode exhaust gas using a water-gas shift reactor prior to reintroduction of the anode exhaust gas into the fuel cell system.

16. The method of claim 11, wherein the mixture comprises carbon monoxide, carbon dioxide, water vapor, hydrogen and fuel, and a percentage of said fuel in the mixture is less than or equal to 20%.

17. The method of claim 11, wherein the fuel comprises methane or natural gas and the percentage of said fuel in said mixture is within a range of about 13% to about 19%.

18. A solid oxide fuel cell stack, comprising:

a plurality of electrolyte-supported solid oxide fuel cells and a plurality of interconnects, each of the plurality of fuel cells comprising;

a solid oxide electrolyte having a first surface and a second surface and a fuel riser inlet opening extending through the solid oxide electrolyte;

an anode electrode on the first surface of the electrolyte and adapted for internal fuel reformation; and

a cathode electrode on the second surface of the electrolyte, wherein the cathode electrode includes an outer edge that includes a concave-shaped offset region adjacent to at least a first side of the fuel inlet riser opening, and the concave-shaped offset region is offset from the fuel inlet riser opening by a first distance sufficient to accommodate a seal that surrounds the fuel inlet riser opening on the second surface of the electrolyte but not on the first surface of the electrolyte;

wherein the anode electrode and the cathode electrode are symmetrical in a region where fuel enters the fuel cell such that an outer edge of the anode electrode is exactly or substantially aligned with the outer edge of the cathode electrode on an opposite side of the electrolyte in the same fuel cell in the region where fuel enters the fuel cell, and the outer edge of the anode electrode includes a concave-shaped offset region adjacent to at least the first side of the fuel inlet riser opening, and the concave-shaped offset region of the outer edge of the anode electrode is offset from the fuel inlet riser opening by the first distance and wherein the solid oxide fuel cell stack is internally manifolded for fuel.

19. The stack of claim 18, wherein the anode and cathode are symmetrical around their entire area.

20. The stack of claim 18, wherein:

the region where fuel enters the fuel cell comprises a region near the fuel inlet riser opening in the electrolyte and the anode electrode is offset from the fuel inlet riser opening by at least 4 mm; and

the fuel inlet riser opening is located adjacent to a first edge of the solid oxide electrolyte, and the outer edge of the anode electrode extends from the concave-shaped offset region in a straight line parallel to the first edge of the solid oxide electrolyte.

21. The stack of claim 20, wherein the anode electrode is located over a fuel distribution plenum in an adjacent interconnect.

22. The stack of claim 20, wherein the anode electrode is not located over a fuel distribution plenum in an adjacent interconnect.