Fuel cell system and control method for fuel cell system
US-2018375129-A1 · Dec 27, 2018 · US
US2019288316A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2019288316-A1 |
| Application number | US-201916280041-A |
| Country | US |
| Kind code | A1 |
| Filing date | Feb 20, 2019 |
| Priority date | Mar 15, 2018 |
| Publication date | Sep 19, 2019 |
| Grant date | — |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
A SOFC system includes: a fuel cell stack; a reformer; an air supplier: a combustor; and a controller. In a stop control of the above system, the controller calculates an average of ratios of the air to the raw material supplied to the reformer as a first average, in a case in which a molar fraction of a hydrogen component in the anode off-gas is higher than a molar fraction of a raw material component in the anode off-gas, and calculates the average of the ratios of the air to the raw material supplied to the reformer as a second average, in a case in which the molar fraction of the hydrogen component in the anode off-gas is lower than the molar fraction of the raw material component in the anode off-gas. The controller controls the air supplier so that the first average is higher than the second average.
Opening claim text (preview).
What is claimed is: 1 . A solid oxide fuel cell system comprising: a fuel cell stack generating a power using a fuel gas and air; a reformer generating the fuel gas by reforming a raw material; an air supplier supplying the air to the fuel cell stack: a combustor combusting an anode off-gas and a cathode off-gas each discharged from the fuel cell stack; and a controller, wherein in a stop control of the solid oxide fuel cell system in which the fuel gas and the air are continuously supplied to the fuel cell stack after power generation is stopped, the controller calculates an average value of ratios of the air to the raw material supplied to the reformer as a first average value, in a case in which a molar fraction of a hydrogen component in the anode off-gas is higher than a molar fraction of a raw material component in the anode off-gas, the controller calculates the average value of the ratios of the air to the raw material supplied to the reformer as a second average value, in a case in which the molar fraction of the hydrogen component in the anode off-gas is lower than the molar fraction of the raw material component in the anode off-gas, and the controller controls the air supplier so that the first average value is higher than the second average value. 2 . The solid oxide fuel cell system according to claim 1 , further comprising a temperature detector detecting a temperature of the reformer, wherein in the stop control, the controller controls the air supplier based on the temperature detected by the temperature detector. 3 . The solid oxide fuel cell system according to claim 2 , wherein in the stop control, the controller controls the air supplier so that the air ratio is decreased as the temperature detected by the temperature detector is decreased. 4 . The solid oxide fuel cell system according to claim 2 , wherein the temperature detector is provided for the reformer. 5 . The solid oxide fuel cell system according to claim 2 , wherein the temperature detector is provided for the fuel cell stack or a periphery thereof. 6 . The solid oxide fuel cell system according to claim 1 , further comprising a raw material supplier supplying the raw material to the reformer, wherein in the stop control, the controller controls the raw material supplier so as to set a supply amount of the raw material supplied to the reformer to a flow rate corresponding to a calorific value of 300 W or more. 7 . The solid oxide fuel cell system according to claim 1 , further comprising a water supplier supplying water to the reformer, wherein in the stop control, the controller controls the water supplier so as to set S/C in the reformer to 2.0 or more. 8 . The solid oxide fuel cell system according to claim 2 , further comprising an ignition device igniting the combustor, wherein in the stop control, the controller controls the ignition device to ignite the combustor when the temperature detected by the temperature detector is decreased by a predetermined value or more in a predetermined time or at predetermined time intervals. 9 . The solid oxide fuel cell system according to claim 1 , wherein the combustor is a diffusion combustor.
Fuel cells with solid oxide electrolytes · CPC title
with one of the reactants being liquid, solid or liquid-charged · CPC title
Reforming processes, e.g. autothermal, partial oxidation or steam reforming · CPC title
Shut-off or shut-down of fuel cells · CPC title
of fuel cell reactants · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.