Solid oxide fuel cell system

Patent metadata

Field	Value
Publication number	US-10686204-B2
Application number	US-201515750682-A
Country	US
Kind code	B2
Filing date	Aug 10, 2015
Priority date	Aug 10, 2015
Publication date	Jun 16, 2020
Grant date	Jun 16, 2020

Abstract

A solid oxide fuel cell system includes a primary fuel supply passage for supplying fuel, plural fuel cell stacks each uses a solid oxide fuel cell and that are provided in line on the primary fuel supply passage and includes at least a first fuel cell stack and a second fuel cell stack, a first reformer that is provided on an upstream side from the first fuel cell stack on the primary fuel supply passage and reforms the fuel by utilizing endothermic reforming reactions, a second reformer that is provided between the first fuel cell stack and the second fuel cell stack on the primary fuel supply passage and reforms the fuel by utilizing endothermic reforming reactions and exothermic methanation reactions, and a secondary fuel supply passage connected between the first fuel cell stack and the second reformer.

First claim

The invention claimed is:

1. A solid oxide fuel cell system comprising:
a primary fuel supply passage that supplies fuel;
a plurality of fuel stacks that are provided in line on the primary fuel supply passage and include at least a first fuel cell stack on an upstream side and a second fuel cell stack on a downstream side, and each of which uses a solid oxide fuel cell;
a first reformer that is provided on an upstream side from the first fuel cell stack on the primary fuel supply passage, and includes reforming catalytic agents for endothermic reforming reactions to reform the fuel by utilizing the endothermic reforming reactions;
a second reformer that is provided between the first fuel cell stack and the second fuel cell stack on the primary fuel supply passage, and includes methanation catalytic agents for exothermic methanation reactions in addition to reforming catalytic agents for endothermic reforming reactions to reform the fuel by utilizing the exothermic methanation reactions in addition to the endothermic reforming reactions;
a heating device that is provided at an upstream side from the first reformer and provides heat to the fuel being supplied through the primary fuel supply passage;
a secondary fuel supply passage that diverges from the primary fuel supply passage at an upstream side from the heating device and is connected to the primary fuel supply passage between the first fuel cell stack and the second reformer;
a temperature sensor that detects gas temperature at an inlet port of the second reformer;
a regulator that regulates fuel volume to be supplied to the second fuel cell stack through the secondary fuel supply passage; and
a controller that is configured to control the regulator based on the gas temperature, detected by the temperature sensor, at the inlet port of the second reformer,
wherein the controller is configured to control the fuel volume such that the lower the gas temperature detected by the temperature sensor at the inlet port of the second reformer becomes, the less the fuel volume supplied to the second reformer becomes.

2. The solid oxide fuel cell system according to claim 1 , wherein
a fuel supply pipe extending in a flow direction of the fuel is provided inside the second reformer, and
a plurality of fuel ejection holes are formed on the fuel supply pipe along a longitudinal direction thereof.

3. The solid oxide fuel cell system according to claim 2 , wherein
the plurality of fuel ejection holes are formed along the longitudinal direction such that an ejected amount on an upstream side is larger than an ejected amount on a downstream side.

4. The solid oxide fuel cell system according to claim 1 , wherein,
inside the second reformer, a reforming catalytic layer for the endothermic reforming reactions is provided adjacently to a methanation catalytic layer for the exothermic methanation reactions.

5. The solid oxide fuel cell system according to claim 4 , wherein
the methanation catalytic layer is disposed as a surface layer, and the reforming catalytic layer is disposed on an inner side of the methanation catalytic layer.

6. The solid oxide fuel cell system according to claim 5 , wherein
a second methanation catalytic layer is further disposed on an inner side of the reforming catalytic layer.

7. The solid oxide fuel cell system according to claim 1 , wherein,
inside the second reformer, a methanation catalytic layer for the exothermic methanation reactions is disposed as a surface layer, and a mixed layer of reforming catalytic agents for the endothermic reforming reactions and methanation catalytic agents for the exothermic methanation reactions is disposed on an inner side of the methanation catalytic layer.

8. A solid oxide fuel cell system comprising:
a primary fuel supply passage that supplies fuel;
a plurality of fuel stacks that are provided in line on the primary fuel supply passage and include at least a first fuel cell stack on an upstream side and a second fuel cell stack on a downstream side, and each of which uses a solid oxide fuel cell;
a first reformer that is provided on an upstream side from the first fuel cell stack on the primary fuel supply passage, and includes reforming catalytic agents for endothermic reforming reactions to reform the fuel by utilizing the endothermic reforming reactions;
a second reformer that is provided between the first fuel cell stack and the second fuel cell stack on the primary fuel supply passage, and includes methanation catalytic agents for exothermic methanation reactions in addition to reforming catalytic agents for endothermic reforming reactions to reform the fuel by utilizing the exothermic methanation reactions in addition to the endothermic reforming reactions;
a heating device that is provided at an upstream side from the first reformer and provides heat to the fuel being supplied through the primary fuel supply passage;
a secondary fuel supply passage that diverges from the primary fuel supply passage at an upstream side from the heating device and is connected to the primary fuel supply passage between the first fuel cell stack and the second reformer;
a temperature sensor that detects gas temperature at an inlet port of the second reformer; and
a controller that is configured to control electricity generated by the first fuel cell stack such that the lower the gas temperature detected by the temperature sensor at the inlet port of the second reformer becomes, the more the electricity generated by the first fuel cell stack becomes.

9. The solid oxide fuel cell system according to claim 8 , further comprising
a regulator that regulates fuel volume to be supplied to the second fuel cell stack through the secondary fuel supply passage;
wherein the controller is configured to control the regulator based on the gas temperature, detected by the temperature sensor, at the inlet port of the second reformer.

10. The solid oxide fuel cell system according to claim 9 , wherein
the controller is configured to control the fuel volume such that the lower the gas temperature detected by the temperature sensor at the inlet port of the second reformer becomes, the less the fuel volume supplied to the second reformer becomes.

11. The solid oxide fuel cell system according to claim 8 , wherein:
a fuel supply pipe extending in a flow direction of the fuel is provided inside the second reformer, and
a plurality of fuel ejection holes are formed on the fuel supply pipe along a longitudinal direction thereof.

12. The solid oxide fuel cell system according to claim 11 , wherein the plurality of fuel ejection holes are formed along the longitudinal direction such that an ejected amount on an upstream side is larger than an ejected amount on a downstream side.

13. The solid oxide fuel cell system according to claim 8 , wherein inside the second reformer, a reforming catalytic layer for the endothermic reforming reactions is provided adjacently to a methanation catalytic layer for the exothermic methanation reactions.

14. The solid oxide fuel cell system according to claim 13 , wherein the methanation catalytic layer is disposed as a surface layer, and the reforming catalytic layer is disposed on an inner side of the methanation catalytic layer.

15. The solid oxide fuel cell system according to claim 14 , wherein a second methanation catalytic layer is further disposed on an inner side of the reforming catalytic layer.

16. The solid oxide fuel cell system according to claim 8 , wherein inside the second reformer, a methanation catalytic layer for the exothermic methanation react

Assignees

• Nissan Motor

Inventors

• Hoshino Maki
• Yaguchi Tatsuya

Classifications

• H01M8/04373 Primary

  of auxiliary devices, e.g. reformers, compressors, burners · CPC title

• Y02E60/50

  Fuel cells · CPC title

• H01M8/0618

  Reforming processes, e.g. autothermal, partial oxidation or steam reforming · CPC title

• H01M8/04776

  at auxiliary devices, e.g. reformer, compressor, burner · CPC title

• H01M8/04753

  of fuel cell reactants · CPC title