IP Library Granted Patent US 11,784,331
Granted Patent B2
US 11,784,331 · App. 17/166,476 · Granted Oct 10, 2023

SOFC-conduction

Inventors: Nathan Palumbo (West Boylston, MA); Paul Osenar (Boxborough, MA); Joshua Persky (Berlin, MA)
Assignee: UPSTART POWER, INC.
H01M8/04067H01M8/2475H01M8/2484H01M2008/1293
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Quick Facts
Patent No.
US 11,784,331
App. No.
17/166,476
Granted
Oct 10, 2023
Kind
B2
Abstract

A solid oxide fuel cell (SOFC) system included high thermal conductivity materials such as copper 10 increase thermal energy transfer by thermal conduction. The copper is protected from oxidation by nickel electroplating and protected from thermal damage by providing Hastelloy liners inside combustion chambers. Monel elements are used in the incoming air conduits to prevent cathode poisoning.

Claims (71)

1. A Solid Oxide Fuel Cell (SOFC) system comprising:

hot zone enclosure walls enclosing a hot zone cavity;

a top tube support wall attached to a surface of the hot zone enclosure walls;

a bottom tube support wall attached to a surface of the hot zone enclosure walls;

a SOFC stack comprising a plurality of fuel cells supported between the top tube support wall and the bottom tube support wall;

a cathode chamber formed between the top tube support wall and the bottom tube support wall;

wherein the bottom tube support wall comprises a first thermal mass formed from one or more thermally conductive materials having a coefficient of thermal conductivity of 100 W/mK at temperatures above 350° C.

2. The SOFC system of claim 1 wherein the hot zone cavity includes a combustion region bounded by a portion of the hot zone enclosure walls, the bottom tube support wall, and a combustor end wall disposed opposed to the bottom support wall.

3. The SOFC system of claim 2 wherein the hot zone enclosure cavity includes a recuperator chamber bounded by a portion of the hot zone enclosure walls, the combustor end wall and a hot zone enclosure bottom wall disposed opposed to the combustor end wall.

4. The SOFC system of claim 2 wherein:

the combustion region confines combustion of a mixture of spent fuel and oxygen depleted cathode air therein;

the combustion of the mixture generates thermal energy that is transferred, from the combustion inside the combustion region, to the first thermal mass, by thermal convection or by thermal radiation;

the thermal energy, received by the first thermal mass, from the combustion inside the combustion region, is transferred, from the first thermal mass, to cathode air contained within the cathode chamber by thermal convection or by thermal radiation.

5. The SOFC system of claim 3 wherein:

the combustion region confines combustion of a mixture of spent fuel and oxygen depleted cathode air therein;

the combustion of the mixture generates thermal energy that is transferred, from the combustion inside the combustion region, to the second thermal mass, by thermal convection or by thermal radiation;

the thermal energy, received by the second thermal mass, from the combustion inside the combustion region, is transferred from the second thermal mass to cathode air contained within the recuperator chamber by thermal convection or by thermal radiation.

6. The SOFC system of claim 1 wherein, the hot zone enclosure walls are formed to provide one or more thermally conductive pathways extending between different regions of the hot zone enclosure walls; are formed from one or more thermally conductive materials having a coefficient of thermal conductivity of 100 W/mK or greater; wherein the first thermal mass is thermally conductively coupled to at least one of the hot zone enclosure walls; wherein thermal energy received by the first thermal mass is transferred, from the first thermal mass, to the hot zone enclosure walls by thermal conduction, and transferred, from the hot zone enclosure walls, to cathode air contained within the cathode chamber, by thermal convection or by thermal radiation.

7. The SOFC system of claim 3 wherein the hot zone enclosure walls are formed to provide one or more thermally conductive pathways extending between different regions of the hot zone enclosure walls; are formed from one or more thermally conductive materials having a coefficient of thermal conductivity of 100 W/mK or greater; wherein the second thermal mass is thermally conductively coupled to at least one of the hot zone enclosure walls; wherein thermal energy received by the second thermal mass is transferred from, the second thermal mass, to the hot zone enclosure walls by thermal conduction, and transferred, from the hot zone enclosure walls to cathode air contained within the recuperator chamber, by thermal convection or by thermal radiation.

8. The SOFC system of claim 1 further comprising a first top protective surface layer ( 5040 ) covering a top surface of the first thermal mass, wherein the first top protective surface layer is thermally conductively coupled to the top surface of the first thermal mass.

9. The SOFC system of claim 8 wherein the first top protective surface layer comprises a chromium free metal.

10. The SOFC system of claim 1 further comprising a first bottom protective surface layer covering a bottom surface of the first thermal mass, wherein the first bottom protective surface layer is thermally conductively coupled to the bottom surface of the first thermal mass.

11. The SOFC system of claim 10 wherein the first bottom protective surface layer ( 5050 ) comprises a metal.

12. The SOFC system of claim 1 further comprising a second top protective surface layer covering a top surface of the second thermal mass, wherein the second top protective surface layer is thermally conductively coupled to the top surface of the second thermal mass.

13. The SOFC system of claim 2 wherein the second top protective surface layer comprises a metal.

14. The SOFC system of claim 1 further comprising a second bottom protective surface layer covering a bottom surface of the second thermal mass, wherein the second bottom protective surface layer is thermally conductively coupled to the bottom surface of the second thermal mass.

15. The SOFC system of claim 14 wherein the second bottom protective surface layer comprises a chromium free metal.

16. A method for thermal energy distribution for a Solid Oxide Fuel Cell (SOFC) system comprising the steps of:

forming a plurality of hot zone enclosure walls to enclose a hot zone cavity;

attaching a top tube support wall to a surface of the hot zone enclosure walls inside the hot zone cavity;

attaching a bottom tube support wall to a surface of the hot zone enclosure walls inside the hot zone cavity;

supporting, a SOFC stack comprising a plurality of fuel cells, inside the hot zone cavity, between the top tube support wall and the bottom tube support wall;

forming, between the top tube support wall and the bottom tub support wall, inside the hot zone cavity, a cathode chamber, for receiving cathode air therein;

forming, the bottom tube support wall to include a first thermal mass formed from one or more thermally conductive materials having a coefficient of thermal conductivity of 100 W/m K at temperatures above 350° C.

17. The method of claim 14 further comprising forming, inside the hot zone cavity, a combustion region bounded by each of, a portion of the hot zone enclosure walls, the bottom tube support wall, and a combustor end wall disposed opposed to the bottom support wall.

18. The method of claim 17 further comprising forming, inside the hot zone cavity, a recuperator chamber bounded by, each of, a portion of the hot zone enclosure walls, the combustor end wall and a hot zone enclosure bottom wall disposed opposed to the combustor end wall.

19. The SOFC system of claim 17 further comprising the steps of:

combusting, inside the combustion region, a mixture of spent fuel, received into the combustion region from the SOFC stack, and oxygen depleted cathode air, received into the cathode chamber from the cathode chamber;

transferring thermal energy generated inside the combustion region to the first thermal mass by thermal convection or by thermal radiation;

transferring the thermal energy, received by the first thermal mass from inside the combustion region, to cathode air contained inside the cathode chamber by thermal convection or by thermal radiation.

20. The method of claim 18 further comprising the steps of:

combusting, inside the combustion region, a mixture of, spent fuel, received into the combustion region from the SOFC stack, and oxygen depleted cathode air, received into the combustion region from the cathode chamber;

transferring thermal energy generated inside the combustion region to the second thermal mass by thermal convection or by thermal radiation;

transferring the thermal energy, received by the second thermal mass from inside the combustion region, to cathode air contained within the recuperator chamber by thermal convection or by thermal radiation.

21. The method of claim 16 further comprising the steps of:

forming the hot zone enclosure walls to provide one or more thermally conductive pathways extending between different regions of the hot zone enclosure walls;

forming the one or more thermally conductive pathways to include one or more thermally conductive materials having a coefficient of thermal conductivity of 100 W/mK or greater;

thermally conductively coupling the first thermal mass to an inside surface of at least one of the hot zone enclosure walls;

transferring thermal energy, between the first thermal mass and the hot zone enclosure walls by thermal conduction;

transferred thermal energy, from the hot zone enclosure walls, to cathode air inside the cathode chamber and to surfaces of the SOFC stack by thermal convection or by thermal radiation.

22. The method of claim 18 further comprising the steps of:

forming the hot zone enclosure walls to provide one or more thermally conductive pathways extending between different regions of the hot zone enclosure walls;

forming the one or more thermally conductive pathways to include one or more thermally conductive materials having a coefficient of thermal conductivity of 100 W/mK or greater;

thermally conductively coupling the second thermal mass an inside surface of at least one of the hot zone enclosure walls;

transferring thermal energy, between the second thermal mass and the hot zone enclosure walls by thermal conduction;

transferring thermal energy, from the hot zone enclosure walls, to cathode air inside the recuperator chamber by thermal convection or by thermal radiation.

23. The method of claim 16 further comprising the steps of: covering a top surface of the first thermal mass with a first top protective surface layer ( 5040 ), wherein the first top protective surface layer is thermally conductively coupled to the top surface of the first thermal mass.

24. The method of claim 23 wherein the first top protective surface layer comprises a chromium free metal.

25. The method of claim 16 further comprising the steps of:

covering a bottom surface of the first thermal mass with a first bottom protective surface layer, wherein the first bottom protective surface layer is thermally conductively coupled to the bottom surface of the first thermal mass.

26. The method of claim 25 wherein the first bottom protective surface layer comprises a metal.

27. The method of claim 16 further comprising the step of covering a top surface of the second thermal mass with a second top protective surface layer, wherein the second top protective surface layer is thermally conductively coupled to the top surface of the second thermal mass.

28. The method of claim 27 wherein the second top protective surface layer comprises a metal.

29. The method of claim 16 further comprising the step of covering a bottom surface of the second thermal mass with a second bottom protective surface layer, wherein the second bottom protective surface layer is thermally conductively coupled to the bottom surface of the second thermal mass.

30. The method of claim 29 wherein the second bottom protective surface layer comprises a chromium free metal.

31. A Solid Oxide Fuel Cell (SOFC) system comprising:

hot zone enclosure walls enclosing a hot zone cavity, wherein the hot zone enclosure walls are formed to include one or more thermally conductive pathways extending between different regions of the hot zone enclosure walls and wherein the one or more thermally conductive pathways are formed to include one or more thermally conductive materials having a coefficient of thermal conductivity of 100 W/mK or greater at temperatures above 350° C.;

a bottom tube support wall attached to a surface of the hot zone enclosure walls;

a SOFC stack comprising a plurality of fuel cells supported to extend from the bottom tube support wall;

wherein the bottom tube support wall comprises a first thermal mass formed from one or more thermally conductive materials having a coefficient of thermal conductivity of 100 W/mK at temperatures above 350° C. and wherein the first thermal mass is thermally conductively coupled to at least one of the one or more thermally conductive pathways;

wherein thermal energy is transferred by thermal conduction, between the first thermal mass, and at least one of the one or more thermally conductive pathways extending between different regions of the hot zone enclosure walls.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 24, 2023
From: PALUMBO, NATHAN; OSENAR, PAUL; PERSKY, JOSHUA
To: PROTONEX TECHNOLOGY CORPORATION
Reel/Frame 064690/0131 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 24, 2023
From: PROTONEX TECHNOLOGY CORPORATION
To: UPSTART POWER, INC.
Reel/Frame 064690/0278 →
Continuity (3)
Continuation 16553868 · Aug 28, 2019
Continuation 14399795
Related Publication 20210167406A1 · Jun 3, 2021