Method of operating hydrogen generator and method of operating fuel cell system

Patent metadata

Field	Value
Publication number	US-9685670-B2
Application number	US-201314125283-A
Country	US
Kind code	B2
Filing date	Mar 1, 2013
Priority date	Apr 10, 2012
Publication date	Jun 20, 2017
Grant date	Jun 20, 2017

Abstract

A method of operating a hydrogen generator includes: a step (a) of generating a hydrogen-containing gas by a hydrogen generation unit by using a raw material in the hydrogen generation unit; a step (b) of removing a sulfur compound from the raw material by a hydrodesulfurizer which is heated by heat transferred from the hydrogen generation unit; and a step (c) of performing an operation of supplying the raw material to the hydrogen generation unit after stopping the generating of the hydrogen-containing gas by the hydrogen generation unit. The step (c) is not performed unless, at least, a temperature of the hydrodesulfurizer is such a temperature at which carbon deposition from the raw material is suppressed.

First claim

The invention claimed is:

1. A method of operating a hydrogen generator, comprising:
removing a sulfur compound from a raw material by a hydrodesulfurizer which is heated by heat transferred from a hydrogen generation unit;
generating a hydrogen-containing gas by the hydrogen generation unit by using the raw material including at least hydrogen and carbon;
stopping the generating of the hydrogen-containing gas by stopping supplying the raw material to the hydrogen generation unit;
detecting a temperature of the hydrodesulfurizer with a first detector; and thereafter,
enabling an operation of re-supplying the raw material to the hydrogen generation unit via the hydrodesulfurizer if the temperature of the hydrodesulfurizer detected by the first detector is equal to or less than a first predetermined temperature, the first predetermined temperature corresponding to such a temperature of the hydrodesulfurizer at which carbon deposition from the raw material onto a hydrodesulfurization catalyst is suppressed.

2. The method of operating a hydrogen generator according to claim 1 , further comprising detecting a temperature of the hydrogen generation unit with a second detector,
wherein the operation of re-supplying includes supplying the raw material to the hydrogen generation unit via the hydrodesulfurizer in order to compensate for an internal pressure drop or gas contraction, if the temperature of the hydrogen generation unit detected by the second detector is equal to or less than a second predetermined temperature.

3. The method of operating a hydrogen generator according to claim 1 , wherein:
the stopping the generating of the hydrogen-containing gas is performed during a stop operation of the hydrogen generator, and
the operation of re-supplying is performed during a re-starting operation after the hydrogen generator is stopped.

4. The method of operating a hydrogen generator according to claim 1 , further comprising performing a cooling process of reducing the temperature of the hydrodesulfurizer after stopping the generating of the hydrogen-containing gas.

5. The method of operating a hydrogen generator according to claim 4 , wherein:
the hydrogen generator includes a combustor which is configured to heat at least part of the hydrogen generation unit, and
the cooling process, performed after stopping the generating of the hydrogen-containing gas, includes a process of supplying air to the combustor.

6. The method of operating a hydrogen generator according to claim 4 , wherein:
the hydrogen generator includes a recycle gas passage, by which the hydrogen-containing gas generated by the hydrogen generation unit is supplied to the hydrodesulfurizer, and
the cooling process includes a process of causing a gas in the hydrogen generation unit to circulate through the recycle gas passage, while stopping the supplying of the raw material to the hydrogen generation unit.

7. The method of operating a hydrogen generator according to claim 1 , wherein the operation of re-supplying the raw material to the hydrogen generation unit is refrained from being performed until the temperature of the hydrodesulfurizer detected by the first detector is equal to or less than the predetermined temperature.

8. The method of operating a hydrogen generator according to claim 1 , wherein:
the stopping the generating of the hydrogen-containing gas is performed during a stop operation of the hydrogen generator, and
a re-starting operation is prohibited until the temperature of the hydrodesulfurizer is equal to or less than the first predetermined temperature.

9. The method of operating a hydrogen generator according to claim 1 ,
wherein, in a special operation mode, the operation of re-supplying is performed for a limited number of times when the temperature of the hydrodesulfurizer is a temperature at which carbon deposition from the raw material onto a hydrodesulfurization catalyst in the hydrodesulfurizer is not suppressed.

10. The method of operating a hydrogen generator according to claim 1 , wherein:
the hydrodesulfurization catalyst includes Co and Mo, and
the operation of re-supplying is performed only when the temperature of the hydrodesulfurizer is lower than or equal to 400° C.

11. The method of operating a hydrogen generator according to claim 1 , wherein:
the hydrodesulfurization catalyst includes Cu and Zn, and
the operation of re-supplying is performed only when the temperature of the hydrodesulfurizer is lower than or equal to 300° C.

12. A method of operating a fuel cell system, comprising:
removing a sulfur compound from a raw material by a hydrodesulfurizer which is heated by heat transferred from a hydrogen generation unit;
generating a hydrogen-containing gas by the hydrogen generation unit by using the raw material including at least hydrogen and carbon;
generating electric power by a fuel cell by using the hydrogen-containing gas;
stopping the generating of the hydrogen-containing gas by stopping supplying the raw material to the hydrogen generation unit;
detecting a temperature of the hydrodesulfurizer with a detector; and thereafter,
enabling an operation of re-supplying the raw material to the hydrogen generation unit via the hydrodesulfurizer if the temperature of the hydrodesulfurizer detected by the detector is equal to or less than a predetermined temperature, the predetermined temperature corresponding to such a temperature of the hydrodesulfurizer at which carbon deposition from the raw material onto a hydrodesulfurization catalyst is suppressed.

13. The method of operating a fuel cell system according to claim 12 , wherein:
the generating the hydrogen-containing gas by the hydrogen generation unit is performed for a power generation operation time period,
the operation of re-supplying includes supplying the raw material to the hydrogen generation unit at a re-starting operation after the fuel cell system is stopped,
the method further comprises:
prohibiting the re-starting operation for a first period when the power generation operation time period is relatively long; and
prohibiting the re-starting operation for a second period when the power generation operation time period is relatively short,

the first period is a period for recovering the fuel cell system, and
the second period is set based on a period required for the temperature of the hydrodesulfurizer to become such a temperature at which carbon deposition from the raw material does not occur.

Assignees

• Panasonic Corp
• Panasonic Ip Man Co Ltd

Inventors

• Harada Chie
• Wakita Hidenobu
• Fujihara Seiji
• Nakajima Tomoyuki
• Kusuyama Takahiro
• Taguchi Kiyoshi

Classifications

• C01B2203/1604

  Starting up the process · CPC title

• H01M8/04776

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

• C01B3/34

  by reaction of hydrocarbons with gasifying agents · CPC title

• C01B2203/066

  with fuel cells · CPC title

• C01B2203/025

  containing a partial oxidation step · CPC title