IP Library Granted Patent US 6,924,053
Granted Patent B2
US 6,924,053 · App. 10/394,203 · Granted Aug 2, 2005

Solid oxide regenerative fuel cell with selective anode tail gas circulation

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Quick Facts
Patent No.
US 6,924,053
App. No.
10/394,203
Granted
Aug 2, 2005
Kind
B2
Abstract

A solid oxide fuel cell system includes a solid oxide fuel cell stack and a hydrogen recovery unit connected to a fuel supply inlet conduit and to a fuel exhaust outlet conduit. The hydrogen recovery unit is adapted to selectively transfer at least a portion of hydrogen from the fuel exhaust stream to the hydrocarbon fuel inlet stream.

Claims (49)

1. A solid oxide fuel cell system, comprising:

a solid oxide fuel cell stack;

a fuel supply inlet conduit adapted to provide a hydrocarbon fuel inlet stream toward the solid oxide fuel cell stack;

a fuel exhaust outlet conduit adapted to remove a fuel exhaust stream from the solid oxide fuel cell stack;

a water vapor and enthalpy recovery unit either directly connected or indirectly connected via a water supply conduit to the fuel supply inlet conduit and to the fuel exhaust outlet conduit, wherein the water vapor and enthalpy recovery unit is adapted to selectively transfer at least a portion of water vapor and heat from the fuel exhaust stream to the hydrocarbon fuel inlet stream; and

a hydrogen recovery unit connected to the fuel supply inlet conduit and to the fuel exhaust outlet conduit, wherein the hydrogen recovery unit is adapted to selectively transfer at least a portion of hydrogen from the fuel exhaust stream to the hydrocarbon fuel inlet stream.

2. The system of claim 1 , wherein the water vapor and enthalpy recovery unit comprises an enthalpy wheel.

3. The system of claim 1 , wherein the hydrogen recovery unit comprises an adsorption hydrogen recovery device or an electrochemical pump, which are adapted to selectively recover hydrogen but not carbon dioxide from the fuel exhaust stream.

4. The system of claim 1 , wherein:

the hydrogen recovery unit is located separately from the water vapor and enthalpy recovery unit; and

the hydrogen recovery unit is located further downstream from the water vapor and enthalpy recovery unit relative to the solid oxide fuel cell stack.

5. The system of claim 1 , further comprising:

a heat exchanger connected to the fuel supply inlet conduit and to the fuel exhaust outlet conduit, wherein the heat exchanger is adapted to transfer heat from the fuel exhaust stream to the hydrocarbon fuel inlet stream.

6. The system of claim 1 , wherein the water vapor and enthalpy recovery unit is directly connected to the fuel supply inlet conduit and to the fuel exhaust outlet conduit.

7. The system of claim 1 , wherein the water vapor enthalpy recovery unit is indirectly connected via water supply conduits to the fuel supply inlet conduit and to the fuel exhaust outlet conduit.

8. The system of claim 1 , wherein the hydrogen recovery unit is directly connected to the fuel supply inlet conduit and to the fuel exhaust outlet conduit.

9. The system of claim 1 , wherein the hydrogen recovery unit is indirectly connected via hydrogen supply conduits to the fuel supply inlet conduit and to the fuel exhaust outlet conduit.

10. A solid oxide fuel cell system, comprising:

a solid oxide fuel cell stack;

a fuel supply inlet conduit adapted to provide a hydrocarbon fuel inlet stream toward the solid oxide fuel cell stack;

a fuel exhaust outlet conduit adapted to remove a fuel exhaust stream from the solid oxide fuel cell stack;

a water vapor unit either directly connected or indirectly connected via a water supply conduit to the fuel supply inlet conduit, wherein the water vapor unit is adapted to selectively provide water vapor to the hydrocarbon fuel inlet stream; and

a hydrogen recovery unit connected to the fuel exhaust outlet conduit, wherein the hydrogen recovery unit is adapted to recover hydrogen from the fuel exhaust stream.

11. The system of claim 10 , wherein the hydrogen recovery unit comprises an adsorption hydrogen recovery device.

12. The system of claim 10 , wherein the water vapor unit comprises a water vapor and enthalpy recovery unit which is adapted to provide enthalpy from the fuel exhaust stream to the hydrocarbon fuel inlet stream.

13. The system of claim 10 , comprising a heat exchanger connected to the fuel supply inlet conduit and to the fuel exhaust outlet conduit, wherein the heat exchanger is adapted to transfer heat from the fuel exhaust stream to the hydrocarbon fuel inlet stream.

14. The system of claim 10 , wherein the hydrogen recovery unit is adapted to selectively transfer at least a portion of hydrogen from the fuel exhaust stream to the hydrocarbon fuel inlet stream.

15. The system of claim 10 , wherein the hydrogen recovery unit comprises an electrochemical pump hydrogen recovery device.

16. The system of claim 10 , wherein:

the hydrogen recovery unit is located separately from the water vapor unit; and

the hydrogen recovery unit is located further downstream from the water vapor unit relative to the solid oxide fuel cell stack.

17. The system of claim 10 , wherein the water vapor unit is directly connected to the fuel supply inlet conduit.

18. The system of claim 10 , wherein the water vapor unit is indirectly connected via a water supply conduit to the fuel supply inlet conduit.

19. The system of claim 10 , wherein the hydrogen recovery unit is directly connected to the fuel exhaust outlet conduit.

20. The system of claim 10 , wherein the hydrogen recovery unit is indirectly connected via a hydrogen supply conduit to the fuel exhaust outlet conduit.

21. A solid oxide fuel cell system, comprising:

a solid oxide fuel cell stack;

a first means for providing a hydrocarbon fuel inlet stream toward the solid oxide fuel cell stack;

a second means for removing a fuel exhaust stream from the solid oxide fuel cell stack;

a third means for selectively providing water vapor to the hydrocarbon fuel inlet stream; and

a fourth means for recovering hydrogen from the fuel exhaust stream.

22. The system of claim 21 , wherein the fourth means comprises an adsorption hydrogen recovery device.

23. The system of claim 21 , wherein the third means is a means for providing enthalpy from the fuel exhaust stream to the hydrocarbon fuel inlet stream.

24. The system of claim 21 , wherein:

the fourth means is located separately from the third means; and

the fourth means is located further downstream from the third means relative to the solid oxide fuel cell stack.

25. The system of claim 21 , further comprising a heat exchanger connected to the first and the second means, wherein the heat exchanger is adapted to transfer heat from the fuel exhaust stream to the hydrocarbon fuel inlet stream.

26. The system of claim 21 , wherein the fourth means is a means for selectively transferring at least a portion of hydrogen from the fuel exhaust stream to the hydrocarbon fuel inlet stream.

27. The system of claim 21 , wherein the fourth means comprises an electrochemical pump hydrogen recovery device.

Assignments (4)
RELEASE OF SECURITY INTEREST Recorded Nov 29, 2018
From: U.S. BANK NATIONAL ASSOCIATION, AS COLLATERAL AGENT
To: BLOOM ENERGY CORPORATION
Reel/Frame 047686/0121 →
SECURITY INTEREST Recorded Dec 15, 2015
From: BLOOM ENERGY CORPORATION
To: U.S. BANK NATIONAL ASSOCIATION, AS COLLATERAL AGENT
Reel/Frame 037301/0093 →
CHANGE OF NAME Recorded Oct 4, 2006
From: ION AMERICA CORPORATION
To: BLOOM ENERGY CORPORATION
Reel/Frame 018345/0543 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 24, 2003
From: MCELROY, JAMES FREDERICK
To: ION AMERICA
Reel/Frame 013905/0533 →