JPS62140376A - Starting method for power generating system with molten type fuel cell - Google Patents
Starting method for power generating system with molten type fuel cellInfo
- Publication number
- JPS62140376A JPS62140376A JP60280439A JP28043985A JPS62140376A JP S62140376 A JPS62140376 A JP S62140376A JP 60280439 A JP60280439 A JP 60280439A JP 28043985 A JP28043985 A JP 28043985A JP S62140376 A JPS62140376 A JP S62140376A
- Authority
- JP
- Japan
- Prior art keywords
- fuel cell
- gas
- cell stack
- lamination
- temperature
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
- H01M8/04014—Heat exchange using gaseous fluids; Heat exchange by combustion of reactants
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04223—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04223—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells
- H01M8/04225—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells during start-up
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
- H01M8/043—Processes for controlling fuel cells or fuel cell systems applied during specific periods
- H01M8/04302—Processes for controlling fuel cells or fuel cell systems applied during specific periods applied during start-up
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/241—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
- H01M8/244—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes with matrix-supported molten electrolyte
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/249—Grouping of fuel cells, e.g. stacking of fuel cells comprising two or more groupings of fuel cells, e.g. modular assemblies
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Fuel Cell (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の技術分野〕
本発明は、溶融炭酸１塩型燃料電池積層体を均一にかつ
少ないエネルギーで昇温させるようにした溶融炭酸塩型
燃料電池発電システムの起動方法に関する。[Detailed Description of the Invention] [Technical Field of the Invention] The present invention provides a method for starting a molten carbonate fuel cell power generation system, which raises the temperature of a molten monosalt carbonate fuel cell stack uniformly and with little energy. Regarding.
溶融炭酸塩型燃料電池では、電池の運転に先立ち、燃料
電池積層体を反応）品度近くまで予熱する必要がある。In molten carbonate fuel cells, the fuel cell stack must be preheated to near-reaction grade prior to operation of the cell.
従来、この予熱手段として積層体の内部に設【プた電気
ヒーターを用いていたが、積層数が多くなると、電気ヒ
ータでは積層方向に均一に昇温させるのが困難になると
いう問題があった。Conventionally, electric heaters installed inside the laminate have been used as a means of preheating, but as the number of layers increases, it becomes difficult for the electric heater to raise the temperature uniformly in the direction of the laminate. .
また、多数の燃料電池積層体を備えた大規模な発電シス
テムを構成しようとすると、これに伴って多数の電気ヒ
ータを備えなくてはならず、メインテナンスの困難性が
増大するというおそれもあった。Additionally, if a large-scale power generation system with a large number of fuel cell stacks was constructed, it would be necessary to install a large number of electric heaters, which could increase the difficulty of maintenance. .
さらには、腐蝕性が強く、しかも高温度で運転される溶
融炭酸塩型燃料電池の内部に電気ヒータを内蔵するとい
うことは、長期間の運転に伴う電気ヒータの劣化を免れ
得ない。Furthermore, since an electric heater is built into a molten carbonate fuel cell which is highly corrosive and operates at high temperatures, it is inevitable that the electric heater will deteriorate over long periods of operation.
本発明は、このような問題に基づきなされたもので、燃
料電池の積層数が増えても均一な昇温か可能であるうえ
、メインテナンスが容易で、しかも経時的な劣化を伴わ
ない溶融炭酸塩型燃料電池発電システムの起動方法を提
供することを目的とする。The present invention was made based on these problems, and is a molten carbonate type fuel cell that can be heated uniformly even when the number of stacked fuel cells increases, is easy to maintain, and does not deteriorate over time. The purpose is to provide a method for starting a fuel cell power generation system.
本発明は、複数の溶融炭酸ＪｉｌＡ型燃料電池積層体を
備えた溶融炭酸塩型燃料電池発電システムを起動するに
際し、まず所定の溶融炭酸塩型燃料電池積層体にガス予
熱器からの加熱ガスを供給して該燃料電池積層体をＵｔ
した後、起動させ、次に該燃料電池積層体からのｌｉｔ
ガスで他の前記溶融炭酸塩型燃料電池積層体を昇温ざＵ
るようにしたことを特徴としている。In the present invention, when starting up a molten carbonate fuel cell power generation system equipped with a plurality of molten carbonate JILA fuel cell stacks, heating gas from a gas preheater is first applied to a predetermined molten carbonate fuel cell stack. The fuel cell stack is supplied to Ut.
After that, it is started up, and then the lit from the fuel cell stack is
The temperature of the other molten carbonate fuel cell stack is raised with gas.
The feature is that it is made to look like this.
本発明によれば、先ず所定の溶融炭酸塩型燃料電池積層
体をガス予熱器で胃温さけ、その後、運転状態となった
上記燃料電池積層体の１１ガスを利用して他の溶融炭酸
塩型燃料電池積層体の昇温を行なうようにしているので
、昇温手段はすべてガスである。ガスは各中位電池に均
一に供給されるので、積層体の積層数が増えた場合でも
均一な昇）届が可能である。According to the present invention, a predetermined molten carbonate fuel cell stack is first warmed with a gas preheater, and then other molten carbonate is heated using the 11 gases of the fuel cell stack that is in operation. Since the temperature of the type fuel cell stack is raised, all temperature raising means are gas. Since gas is uniformly supplied to each intermediate battery, uniform heating is possible even when the number of layers in the stack increases.
しかも、この発明によれば、昇温手段どして電気ヒータ
を必要どじないので、積層体の構造ら簡単になり、メイ
ンテナンスが容易になる。Moreover, according to the present invention, since an electric heater is not required as a temperature raising means, the structure of the laminated body is simplified and maintenance is facilitated.
また、この発明では運転状態の燃料電池ｖ４層体で発生
ずるジュール熱を利用して、他の積層体を臂瀉するよう
にしているので、エネルギー効率の向上化を図ることが
でき、省エネルギーに寄与するところ大である。In addition, in this invention, the Joule heat generated in the V4 fuel cell stack in operation is used to evacuate the other stacks, making it possible to improve energy efficiency and save energy. This is a great contribution.
以下、本発明の詳細を図示の実施例に基づき説明する。 Hereinafter, details of the present invention will be explained based on illustrated embodiments.
第１図は本実施例に係る溶融炭酸塩型燃料電池発電シス
テムの構成を示す図である。予熱のために供給されるガ
スＲ（例えば空気）は、ガス予熱器１，２に供給されて
、ここで加熱される。予熱器１の排出側は、バルブ３を
介して燃料電池積層体４のアノード側の供給マニホール
ドに接続されるとともに、バルブ５を介して燃料電池積
層体６のアノード側の供給マニホールドに接続され、必
要に応じてさらに図示しない他の燃料電池積層体にバル
ブを介して接続される。一方、予熱器２の排出側は、バ
ルブ７を介して燃料電池積層体４のカソード側の供給マ
ニホールドに接続されるとともに、バルブ８を介して燃
料電池積層体６のカソード側の供給マニホールドに接続
され、必要に応じてさらに図示しない伯の燃料転地積層
体にバルブを介して接続される。燃料電池積層体４のア
ノード側の排出マニホールドは、バルブ９を介してさら
に次の燃おｌ電池積層体１０のアノード側の供給マニホ
ールドに接続されるとともに、バルブ１１を介して排出
系統に接続されている。また、燃料電池積層体４のカソ
ード側の排出マニホールドは、バルブ１２を介して燃料
転地積層体１０のカソード側の供給マニホールドに接続
されるとともに、バルブ１３を介してＪ、Ｉｌ出糸系統
接続されている。一方、燃料電池積層体６のアノード側
の排出マニホールドは、バルブ１４を介してさらに次の
燃料電池積層体１５のアノード側の供給マニホールドに
接続されるとともに、バルブ１６を介して排出系統に接
続されている。また、燃利電池積５一
層体６のカソード側の排出マニホールドは、バルブ１７
を介して燃料電池積層体１５のカソード側の供給マニホ
ールドに接続されるとともに、バルブ１８を介して排出
系統に接続されている。これら燃料電池積層体４，６．
１０．１５の各排出系は必要に応じてさらに次段の図示
しない燃料電池積層体に接続することもできる。FIG. 1 is a diagram showing the configuration of a molten carbonate fuel cell power generation system according to this embodiment. Gas R (for example, air) supplied for preheating is supplied to gas preheaters 1 and 2 and heated there. The discharge side of the preheater 1 is connected to a supply manifold on the anode side of the fuel cell stack 4 via a valve 3, and is connected to a supply manifold on the anode side of the fuel cell stack 6 via a valve 5. If necessary, it is further connected to other fuel cell stacks (not shown) via valves. On the other hand, the discharge side of the preheater 2 is connected to the supply manifold on the cathode side of the fuel cell stack 4 via a valve 7 and also to the supply manifold on the cathode side of the fuel cell stack 6 via a valve 8. If necessary, it is further connected to a fuel diversion stack (not shown) via a valve. The exhaust manifold on the anode side of the fuel cell stack 4 is further connected to the supply manifold on the anode side of the next fuel cell stack 10 via a valve 9, and is connected to the exhaust system via a valve 11. ing. In addition, the discharge manifold on the cathode side of the fuel cell stack 4 is connected to the supply manifold on the cathode side of the fuel transfer stack 10 via a valve 12, and is also connected to the J and Il spinning systems via a valve 13. ing. On the other hand, the exhaust manifold on the anode side of the fuel cell stack 6 is further connected via a valve 14 to the supply manifold on the anode side of the next fuel cell stack 15, and is also connected to the exhaust system via a valve 16. ing. Further, the discharge manifold on the cathode side of the fuel cell stack 5 single-layer assembly 6 has a valve 17.
It is connected to a supply manifold on the cathode side of the fuel cell stack 15 via a valve 18, and to an exhaust system via a valve 18. These fuel cell stacks 4, 6.
Each of the exhaust systems 10.15 can be further connected to a fuel cell stack (not shown) in the next stage, if necessary.
燃料ガスＰの供給系統は、バルブ２１を介して燃料電池
積層体４のアノード側供給マニホールドに接続され、バ
ルブ２１．２２を介して燃料電池積層体６のアノード側
供給マニホールドに接続され、バルブ２３を介して燃料
電池積層体１ｏのアノード側供給マニホールドに接続さ
れ、バルブ２３．２４を介して燃料電池積層体１５のア
ノード側供給マニホールドに接続され、さらに必要に応
じて図示しない他の燃料電池積層体にバルブを介して接
続される。一方、酸化剤ガスＱの供給系統は、バルブ２
５を介して燃料電池積層体４のカソード側供給マニホー
ルドに接続され、バルブ２５．２６を介して燃料電池積
層体６のカソード６一
側供給マニホールドに接続され、バルブ２７を介して燃
料電池積層体１０のノコソード側供給マニホールドに接
続され、バルブ２７．２８を介して燃料電池積層体１５
のアノード側供給マニホールドに接続され、さらに必要
に応じて図示しない他の燃料電池積層体にバルブを介し
て接続される。The supply system for fuel gas P is connected to the anode side supply manifold of the fuel cell stack 4 via a valve 21, connected to the anode side supply manifold of the fuel cell stack 6 via valves 21 and 22, and connected to the anode side supply manifold of the fuel cell stack 6 via a valve 23. is connected to the anode side supply manifold of the fuel cell stack 1o through valves 23, 24, and connected to the anode side supply manifold of the fuel cell stack 15 via valves 23, 24, and further connected to other fuel cell stacks (not shown) as necessary. Connected to the body via a valve. On the other hand, the supply system for the oxidizing gas Q is the valve 2.
5 to the cathode side supply manifold of the fuel cell stack 4, connected to the cathode 6 side supply manifold of the fuel cell stack 6 via valves 25 and 26, and connected to the fuel cell stack 4 via the valve 27 to the cathode side supply manifold of the fuel cell stack 6. 10 to the fuel cell stack 15 via valves 27 and 28.
It is connected to the anode side supply manifold of the fuel cell, and is further connected to other fuel cell stacks (not shown) via valves as necessary.
このように構成された溶融炭酸塩型燃料電池発電システ
ムは、次のようにして起動される。The molten carbonate fuel cell power generation system configured as described above is activated as follows.
まず、第１にバルブ３．７，１１．１３を開き、他のバ
ルブを全て閉じる。これによって第２図に示す系統が形
成される。この状態でガス予熱器１゜２から加熱ガスＲ
′を燃料電池積層体４のアノードおよびカソードの供給
マニホールドに送込み、燃料電池積層体４を昇温する。First, valves 3.7 and 11.13 are opened, and all other valves are closed. As a result, the system shown in FIG. 2 is formed. In this state, the heated gas R is heated from the gas preheater 1゜2.
' is fed into the anode and cathode supply manifolds of the fuel cell stack 4 to raise the temperature of the fuel cell stack 4.
燃料電池積層体４の昇温に供された加熱ガスＲ′を、排
出系統を介して排出する。The heated gas R' used to raise the temperature of the fuel cell stack 4 is discharged via the discharge system.
燃料電池積層体４が十分に予熱されたら、次にバルブ５
．８．９．１２．１６．１８，２１゜２５を開き、伯の
バルブは閉じる。これにより、第３図に示すような系統
が形成される。この状態で燃料電池積層体４に燃料ガス
Ｐど酸化剤ガスＱとを送込み、燃料電池積層体４で発電
を行なわせる。燃料電池積層体４は発電に伴い熱を発す
るので、この熱を伴う排ガスＰ’ 、Ｑ’を次段の燃料
電池積層体１０に供給し、この排ガスＰ’ 、Ｑ’を燃
料電池積層体１０の昇温に利用する。これと同時に、ガ
ス予熱器１，２からの加熱ガスＲ′を、別の燃料電池積
層体６に供給し、この積層体６を昇温させる。After the fuel cell stack 4 is sufficiently preheated, the valve 5 is then heated.
．． 8.9.12.16.18,21°25 is opened, and the bar valve is closed. As a result, a system as shown in FIG. 3 is formed. In this state, fuel gas P and oxidant gas Q are fed into the fuel cell stack 4 to cause the fuel cell stack 4 to generate electricity. Since the fuel cell stack 4 generates heat as it generates electricity, the exhaust gases P' and Q' accompanied by this heat are supplied to the fuel cell stack 10 in the next stage. It is used to raise the temperature of At the same time, heated gas R' from the gas preheaters 1 and 2 is supplied to another fuel cell stack 6 to raise the temperature of this stack 6.
燃料電池積層体６，１０が十分に品温したら、次にバル
ブ１１．１３，１４．１７，２１．２２゜２３．２５．
２６．２７を開ぎ、他のバルブは閉じる。これによって
第４図に示すような系統が形成される。この状態で燃料
電池積層体４，６゜１０に燃料ガスＰおよび酸化剤ガス
Ｑを供給し、これらを発電させる。燃料電池ｖ４層体６
からの高温の排ガスＰ’ 、Ｑ’ は、燃料電池ｖＩ層
体重５に供給して、この＆！ｉ層体１５の昇温に利用す
る。他の燃料電池積層体４，１０の高温の１１ガスＰ′
。Once the fuel cell stacks 6 and 10 have sufficient temperature, the valves 11.13, 14.17, 21.22°23.25.
26.27 is opened and the other valves are closed. As a result, a system as shown in FIG. 4 is formed. In this state, fuel gas P and oxidant gas Q are supplied to the fuel cell stack 4, 6, 10, and these are used to generate electricity. fuel cell v4 layer body 6
The high temperature exhaust gases P' and Q' from the &! It is used to raise the temperature of the i-layer body 15. High temperature 11 gas P' of other fuel cell stacks 4 and 10
.
Ｑ′については、伯の燃料電池積層体の予熱に利用して
も、そのまま期用してム良い。Regarding Q', even if it is used for preheating the fuel cell stack, it can be used as is.
なお、上記の実施例では、特に燃料電池積層体の数につ
いては特定けず、４以上として説明したが、少なくとも
２つの積層体で構成される発電システムであれば、本発
明の効果を奏することは可能である。In the above embodiment, the number of fuel cell stacks is not specified and is explained as four or more, but the effects of the present invention can be achieved as long as the power generation system is composed of at least two stacks. It is possible.
また、ガス予熱器１．２は、電気ヒータであっても、燃
焼器であっても良い。このガス予熱器は、ただ一つの燃
料電池積層体を予熱するのに利用するものでも良い。Ｊ
：だ、ガス予熱器の電源に、運転状態の燃料電池積層体
を用いるようにしても良い。加熱ガスＲ′としては、燃
料ガスＰ、酸化剤ガスＱあるいはこれらとは全く異なる
ガスの使用が考えられる。Moreover, the gas preheater 1.2 may be an electric heater or a combustor. This gas preheater may be used to preheat only one fuel cell stack. J
: However, the fuel cell stack in operation may be used as the power source for the gas preheater. As the heating gas R', it is possible to use fuel gas P, oxidant gas Q, or a gas completely different from these.
また、本発明は、各スタックがそれぞれ別個の圧力容器
内に収容されていても、１個の容器内に複数のスタック
が直列に、あるいは並列に収容されていても、適用可能
であることは言うまでもない。Furthermore, the present invention is applicable regardless of whether each stack is housed in a separate pressure vessel or a plurality of stacks are housed in series or in parallel within one vessel. Needless to say.
第１図は本発明の一実施例に係る溶融炭酸塩型燃料電池
弁型システムの構成図、第２図〜第４図は同システムの
起動時に各バルブの開閉によって選択される各種の系統
を示す図である。
１．２．・・・ガス予熱器、３，５．７〜９．１１〜１
４．１６〜２８・・・バルブ、４，６，１０゜１５・・
・燃料電池積層体、Ｒ′・・・加熱ガス、Ｐ・・・燃料
ガス、Ｑ・・・酸化剤ガス、Ｐ’ 、Ｑ’ ・・・排ガ
ス。Fig. 1 is a block diagram of a molten carbonate fuel cell valve type system according to an embodiment of the present invention, and Figs. 2 to 4 show various systems selected by opening and closing each valve at the time of starting up the system. FIG. 1.2. ...Gas preheater, 3,5.7~9.11~1
4.16~28...Valve, 4,6,10°15...
- Fuel cell stack, R'... heating gas, P... fuel gas, Q... oxidizing gas, P', Q'... exhaust gas.
Claims (1)
型燃料電池発電システムを起動するに際し、まず所定の
溶融炭酸塩型燃料電池積層体にガス予熱器からの加熱ガ
スを供給して該燃料電池積層体を昇温した後、起動させ
、次に該燃料電池積層体からの排ガスで他の前記溶融炭
酸塩型燃料電池積層体を昇温させるようにしたことを特
徴とする溶融炭酸塩型燃料電池発電システムの起動方法
。When starting up a molten carbonate fuel cell power generation system equipped with a plurality of molten carbonate fuel cell stacks, first, heating gas from a gas preheater is supplied to a predetermined molten carbonate fuel cell stack. Molten carbonate, characterized in that the temperature of the fuel cell stack is raised and then started, and then the exhaust gas from the fuel cell stack is used to raise the temperature of the other molten carbonate fuel cell stack. How to start a type fuel cell power generation system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60280439A JPH0732024B2 (en) | 1985-12-13 | 1985-12-13 | Method for starting molten carbonate fuel cell power generation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60280439A JPH0732024B2 (en) | 1985-12-13 | 1985-12-13 | Method for starting molten carbonate fuel cell power generation system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62140376A true JPS62140376A (en) | 1987-06-23 |
| JPH0732024B2 JPH0732024B2 (en) | 1995-04-10 |
Family
ID=17625066
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60280439A Expired - Fee Related JPH0732024B2 (en) | 1985-12-13 | 1985-12-13 | Method for starting molten carbonate fuel cell power generation system |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0732024B2 (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0260061A (en) * | 1988-08-26 | 1990-02-28 | Nippon Telegr & Teleph Corp <Ntt> | Fuel cell power generating system |
| JP2000294263A (en) * | 1999-04-08 | 2000-10-20 | Toyota Motor Corp | Fuel cell system and heating method for fuel cell |
| JP2001229950A (en) * | 2000-02-14 | 2001-08-24 | Nissan Motor Co Ltd | Fuel cell system |
| EP1406332A1 (en) * | 2001-07-09 | 2004-04-07 | Zakrytoe Aktsionernoe Obschestvo Independent Power Technologies "IPT" | Method and device for removing inert impurities |
| JP2004349093A (en) * | 2003-05-22 | 2004-12-09 | Tokyo Electric Power Co Inc:The | Fuel cell plant |
| WO2010140557A1 (en) * | 2009-06-03 | 2010-12-09 | Honda Motor Co., Ltd. | Fuel cell system |
| JP2010282798A (en) * | 2009-06-03 | 2010-12-16 | Honda Motor Co Ltd | Control program for fuel cell system |
| WO2017017786A1 (en) * | 2015-07-28 | 2017-02-02 | 日産自動車株式会社 | Fuel-cell system |
-
1985
- 1985-12-13 JP JP60280439A patent/JPH0732024B2/en not_active Expired - Fee Related
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0260061A (en) * | 1988-08-26 | 1990-02-28 | Nippon Telegr & Teleph Corp <Ntt> | Fuel cell power generating system |
| JP2000294263A (en) * | 1999-04-08 | 2000-10-20 | Toyota Motor Corp | Fuel cell system and heating method for fuel cell |
| JP2001229950A (en) * | 2000-02-14 | 2001-08-24 | Nissan Motor Co Ltd | Fuel cell system |
| EP1406332A1 (en) * | 2001-07-09 | 2004-04-07 | Zakrytoe Aktsionernoe Obschestvo Independent Power Technologies "IPT" | Method and device for removing inert impurities |
| EP1406332A4 (en) * | 2001-07-09 | 2009-05-06 | Obschestvo S Ogranichennoi Otv | Method and device for removing inert impurities |
| JP4670228B2 (en) * | 2003-05-22 | 2011-04-13 | 東京電力株式会社 | Fuel cell plant |
| JP2004349093A (en) * | 2003-05-22 | 2004-12-09 | Tokyo Electric Power Co Inc:The | Fuel cell plant |
| WO2010140557A1 (en) * | 2009-06-03 | 2010-12-09 | Honda Motor Co., Ltd. | Fuel cell system |
| JP2010282798A (en) * | 2009-06-03 | 2010-12-16 | Honda Motor Co Ltd | Control program for fuel cell system |
| US8563193B2 (en) | 2009-06-03 | 2013-10-22 | Honda Motor Co., Ltd. | Fuel cell system |
| WO2017017786A1 (en) * | 2015-07-28 | 2017-02-02 | 日産自動車株式会社 | Fuel-cell system |
| JPWO2017017786A1 (en) * | 2015-07-28 | 2018-05-17 | 日産自動車株式会社 | Fuel cell system |
| US10249894B2 (en) | 2015-07-28 | 2019-04-02 | Nissan Motor Co., Ltd. | Fuel cell system |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0732024B2 (en) | 1995-04-10 |
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