Fuel cell system and method for operating fuel cell system

Patent metadata

Field	Value
Publication number	US-11367887-B2
Application number	US-201916976205-A
Country	US
Kind code	B2
Filing date	Mar 6, 2019
Priority date	Mar 7, 2018
Publication date	Jun 21, 2022
Grant date	Jun 21, 2022

Abstract

Provided is a fuel cell system capable of further increasing electric power generation efficiency, compared to the current circumstances, with respect to a fuel cell SOFC that generates electric power by supplying a reformed gas obtained by steam reforming to a fuel electrode. A steam reformer that reforms a hydrocarbon fuel by a steam reforming reaction; a fuel cell that operates by introducing a reformed gas to a fuel electrode; and an anode off-gas circulation path that removes condensed water while cooling an anode off-gas, and introduces the anode off-gas to the steam reformer are provided. A condensation temperature in a condensing device is controlled by a control unit that controls a steam partial pressure of the anode off-gas circulated to the steam reformer, and S/C adjustment is adapted to high-efficiency electric power generation.

First claim

The invention claimed is:

1. A fuel cell system comprising:
a steam reformer that reforms a hydrocarbon fuel by a steam reforming reaction;
a fuel cell that operates by introducing a reformed gas obtained by the steam reformer to a fuel electrode;
an anode off-gas circulation path that removes condensed water while cooling an anode off-gas exhausted from the fuel electrode, and introduces the anode off-gas to the steam reformer; and
a control unit configured to:
adjust an amount of the condensed water removed from the anode off-gas circulation path, and control a steam partial pressure of the anode off-gas circulated to the steam reformer;
adjust an S/C ratio of an appropriate S/C ratio, wherein in an external power supply state where generated electric power is supplied to an outside by following an electric power load, with a configuration in which only the steam circulated through the anode off-gas circulation path is allowed to flow in as steam required for the steam reformer, with respect to the electric power load, the appropriate S/C ratio is preset for the S/C ratio which is a ratio of an amount of the steam circulated to the steam reformer to an amount of carbon input to the steam reformer, and a minimum fuel gas concentration is set for a fuel gas concentration at the outlet of the fuel electrode; and
control the steam partial pressure of the anode off-gas circulated to the steam reformer to a steam partial pressure that allows the hydrocarbon fuel, in an amount sufficient to maintain the fuel gas concentration at the outlet of the fuel electrode at the minimum fuel gas concentration or higher, to be input to the steam reformer.

2. The fuel cell system according to claim 1 , further comprising:
a condensing means configured to remove condensed water, provided on one or both of a discharge side and a suction side of a circulating means which circulates the anode off-gas to the steam reformer,
wherein the control unit adjusts a circulation amount by the circulating means and a condensation temperature in the condensing means to adjust an amount of steam circulated to the steam reformer.

3. The fuel cell system according to claim 2 ,
wherein in the anode off-gas circulation path,
a cooling means that cools the anode off-gas flowing in the anode off-gas circulation path is provided between the condensing means and the fuel cell, and
a temperature raising means that raises a temperature of the anode off-gas flowing in the anode off-gas circulation path is provided between the condensing means and the steam reformer.

4. The fuel cell system according to claim 3 ,
wherein heat recovered by the cooling means is used in the temperature raising means.

5. The fuel cell system according to claim 1 ,
wherein in the anode off-gas circulation path, the anode off-gas is cooled to a temperature of higher than 50° C. and lower than 250° C.

6. The fuel cell system according to claim 2 ,
wherein
the condensing means and the control unit cooperate to operate as a S/C ratio adjusting means that adjusts the S/C ratio.

7. The fuel cell system according to claim 1 , further comprising:
a desulfurization reactor that removes a sulfur component supplied together with the hydrocarbon fuel; and
a path that supplies at least a part of the anode off-gas whose steam partial pressure is reduced to the desulfurization reactor.

8. The fuel cell system according to claim 1 , further comprising:
a desulfurization reactor that removes a sulfur component supplied together with the hydrocarbon fuel,
wherein the hydrocarbon fuel desulfurized so as to have a sulfur content of 1 vol. ppb or less in the desulfurization reactor is supplied to the steam reformer.

9. The fuel cell system according to claim 1 ,
wherein regarding the anode off-gas exhausted from the fuel electrode, the anode off-gas is configured to be distributively supplied as a steam reforming gas in the steam reformer and as a combustion gas used for heating in steam reforming.

10. The fuel cell system according to claim 1 ,
wherein the fuel cell is a solid oxide fuel cell.

11. A method for operating a fuel cell system, the fuel system comprising:
a steam reformer that reforms a hydrocarbon fuel by a steam reforming reaction; a fuel cell that operates by introducing a reformed gas obtained by the steam reformer to a fuel electrode; and
an anode off-gas circulation path that removes condensed water while cooling an anode off-gas exhausted from the fuel electrode, and introduces the anode off-gas to the steam reformer,
the method comprising:
adjusting an amount of condensed water removed from the anode off-gas circulation path to adjust a steam partial pressure of the anode off-gas circulated to the steam reformer;
adjusting an S/C ratio to an appropriate S/C ratio, wherein in an external power supply state where generated electric power is supplied to an outside by following an electric power load, with a configuration in which only the steam circulated through the anode off-gas circulation path is allowed to flow in as steam required for the steam reformer, with respect to the electric power load, the appropriate S/C ratio is preset for the S/C ratio which is a ratio of an amount of the steam circulated to the steam reformer to an amount of carbon input to the steam reformer, and a minimum fuel gas concentration is set for a fuel gas concentration at the outlet of the fuel electrode; and
controlling the steam partial pressure of the anode off-gas circulated to the steam reformer to a steam partial pressure that allows the hydrocarbon fuel, in an amount sufficient to maintain the fuel gas concentration at the outlet of the fuel electrode at the minimum fuel gas concentration or higher, to be input to the steam reformer.

12. The method for operating a fuel cell system according to claim 11 ,
wherein a condensing means capable of removing condensed water is provided on one or both of a discharge side and a suction side of a circulating means which circulates the anode off-gas to the steam reformer, and
the circulation amount by the circulating means and the condensation temperature in the condensing means are adjusted to adjust an amount of the steam circulated to the steam reformer.

13. The method for operating a fuel cell system according to claim 12 ,
wherein in an external power supply state where generated electric power is supplied to an outside by following an electric power load, with a configuration in which only the steam circulated through the anode off-gas circulation path is allowed to flow in as steam required for the steam reformer,
the condensing means is operated as a S/C ratio adjusting means that adjusts a S/C ratio, which is a ratio of the amount of the steam circulated to the steam reformer to an amount of carbon input to the steam reformer.

14. The method for operating a fuel cell system according to claim 11 ,
wherein a desulfurization reactor that removes a sulfur component supplied together with the hydrocarbon fuel is provided, and
the method further comprises supplying at least a part of the anode off-gas whose steam partial pressure is reduced to the desulfurization reactor.

15. The method for operating a fuel cell system according to claim 11 ,
wherein a desulfurization reactor that removes a sulfur component supplied together with the hydrocarbon fuel is provided, and
the method further comprises desulfurizing a sulfur content to 1 vol. ppb or less in the desulfurization reactor and supplying the hydrocarbon fuel to the steam reformer.

16. A fuel cell system comprising:
a steam re

Assignees

• Osaka Gas Co Ltd

Inventors

• SHINKE Noritoshi
• Echigo Mitsuaki

Classifications

• C01B2203/0827

  at least part of the fuel being a recycle stream · CPC title

• H01M8/04761

  of fuel cell exhausts · CPC title

• H01M8/04843

  of fuel cell exhausts · CPC title

• H01M8/0675

  Removal of sulfur · CPC title

• C01B2203/0233

  the reforming step being a steam reforming step · CPC title