JPH0963608A - Fuel cell power generating system - Google Patents
Fuel cell power generating systemInfo
- Publication number
- JPH0963608A JPH0963608A JP7210347A JP21034795A JPH0963608A JP H0963608 A JPH0963608 A JP H0963608A JP 7210347 A JP7210347 A JP 7210347A JP 21034795 A JP21034795 A JP 21034795A JP H0963608 A JPH0963608 A JP H0963608A
- Authority
- JP
- Japan
- Prior art keywords
- fuel cell
- gas
- hot air
- power generation
- generating furnace
- 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
-
- 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
Abstract
Description
【０００１】[0001]
【発明の属する技術分野】本発明は、溶融炭酸塩型燃料
電池を用いた燃料電池発電設備に関する。The present invention relates to a fuel cell power generation facility using a molten carbonate fuel cell.
【０００２】[0002]
【従来の技術】溶融炭酸塩型燃料電池は、高効率、かつ
環境への影響が少ないなど、従来の発電装置にはない特
徴を有しており、水力・火力・原子力に続く発電システ
ムとして注目を集め、現在世界各国で鋭意研究開発が行
われている。特に天然ガスを燃料とする溶融炭酸塩型燃
料電池を用いた発電設備では、図２に示すように天然ガ
ス等の燃料ガス１を水素を含むアノードガス２に改質す
る改質器１０と、アノードガス２と酸素を含むカソード
ガス３とから発電する燃料電池１１とを備えており、改
質器１０で作られたアノードガス２は燃料電池に供給さ
れ、燃料電池内でその大部分（例えば８０％）を消費し
た後、アノード排ガス４として改質器の燃焼室Ｃｏに供
給される。改質器１０ではアノード排ガス中の可燃成分
（水素、一酸化炭素、メタン等）がカソード排ガスによ
り燃焼し、高温の燃焼ガスにより改質室Ｒｅを加熱し改
質室の燃料を改質する。改質室を出た燃焼排ガス５は空
気予熱器１３ｂ、凝縮器１６ａ、気水分離器１５を通っ
て水分を除去され、低温ブロア１７ｃで加圧され、ター
ビン圧縮機１２から供給される加圧空気６と合流してカ
ソードガス３となり、燃料電池のカソード側に電池反応
に必要な二酸化炭素を供給する。燃料電池内でその一部
が反応したカソードガス（カソード排ガス７）は、高温
ブロア１７ｂにより燃料電池の上流側に一部が循環さ
れ、残りの一部７ａは改質器に燃焼用空気として供給さ
れ、残り７ｂはタービン圧縮機１２で圧力を回収され、
排熱回収装置１９による熱回収後に系外に排出される。
なお、図２において、１３ａは燃料予熱器、１４は脱硫
器、１６ｂは加熱器、１７ｄは空気ブロア、１８は熱風
発生炉である。2. Description of the Related Art Molten carbonate fuel cells have features that are not found in conventional power generation devices, such as high efficiency and little impact on the environment, and have attracted attention as power generation systems following hydro, thermal and nuclear power. Are being researched and developed in various countries around the world. Particularly in a power generation facility using a molten carbonate fuel cell using natural gas as a fuel, a reformer 10 for reforming a fuel gas 1 such as natural gas into an anode gas 2 containing hydrogen as shown in FIG. The reformer 10 is provided with a fuel cell 11 that generates electric power from an anode gas 2 and a cathode gas 3 containing oxygen. The anode gas 2 produced in the reformer 10 is supplied to the fuel cell, and most of it (for example, in the fuel cell) (for example, After consuming 80%), the anode exhaust gas 4 is supplied to the combustion chamber Co of the reformer. In the reformer 10, combustible components (hydrogen, carbon monoxide, methane, etc.) in the anode exhaust gas are burned by the cathode exhaust gas, and the high temperature combustion gas heats the reforming chamber Re to reform the fuel in the reforming chamber. The combustion exhaust gas 5 that has exited the reforming chamber passes through the air preheater 13b, the condenser 16a, and the steam separator 15 to remove moisture, is pressurized by the low temperature blower 17c, and is supplied from the turbine compressor 12. It joins with the air 6 to become the cathode gas 3, and supplies the carbon dioxide necessary for the cell reaction to the cathode side of the fuel cell. A part of the cathode gas (cathode exhaust gas 7), a part of which has reacted in the fuel cell, is circulated upstream of the fuel cell by the high temperature blower 17b, and the remaining part 7a is supplied to the reformer as combustion air. The remaining 7b is pressure-recovered by the turbine compressor 12,
After the heat recovery by the exhaust heat recovery device 19, it is discharged to the outside of the system.
In FIG. 2, 13a is a fuel preheater, 14 is a desulfurizer, 16b is a heater, 17d is an air blower, and 18 is a hot air generating furnace.
【０００３】[0003]
【発明が解決しようとする課題】従来、かかる燃料電池
発電設備の起動は、内部に窒素ガスを充填した状態
で、熱風発生炉１８により加熱器１６ｂに熱風を供給
し、加熱器１６ｂで内部を循環する窒素ガスを加熱し、
この窒素ガスの循環により、燃料電池１１と改質器１
０を加熱し、これらが所定の温度に達したときに、ター
ビン圧縮機１２から空気を導入して、燃料電池１１を介
して改質器１０の燃焼室Ｃｏに空気を供給し、次いで
水蒸気８と燃料ガス１を改質器に供給して、燃料電池１
１を介して改質器１０の燃焼室Ｃｏに燃料ガスを供給し
て燃焼させ、その熱で改質室Ｒｅを流れる燃料ガス１を
改質して改質ガス（アノードガス２）を燃料電池１１に
供給し発電を開始する。Conventionally, such a fuel cell power generation facility is started up by supplying hot air to the heater 16b by the hot air generating furnace 18 with the inside filled with nitrogen gas, and then heating the inside by the heater 16b. Heat the circulating nitrogen gas,
By circulating this nitrogen gas, the fuel cell 11 and the reformer 1
0 are heated, and when they reach a predetermined temperature, air is introduced from the turbine compressor 12 to supply air to the combustion chamber Co of the reformer 10 via the fuel cell 11, and then steam 8 And the fuel gas 1 are supplied to the reformer, and the fuel cell 1
Fuel gas is supplied to the combustion chamber Co of the reformer 10 through 1 to burn the fuel gas, and the heat of the fuel gas reforms the fuel gas 1 flowing in the reforming chamber Re to generate the reformed gas (anode gas 2) as a fuel cell. 11 and power generation is started.
【０００４】熱風発生炉１８は、発電開始後は熱風の供
給を停止し、燃料電池の温度制御は高温ブロア１７ｂに
よるカソードガスの循環により行うようになっている。
しかし、実際には燃料電池の運転中も加熱器１６ｂや循
環ラインからの放熱が大きく、燃料電池の反応熱だけで
は燃料電池の温度が維持できない問題点があった。その
ため、発電開始後であっても、熱風発生炉１８を運転し
て熱風を供給する必要があり、余分な燃料を必要とし、
プラント効率が悪化する問題点があった。The hot air generating furnace 18 stops the supply of hot air after the start of power generation, and the temperature of the fuel cell is controlled by circulating the cathode gas by the high temperature blower 17b.
However, in reality, the heat radiated from the heater 16b and the circulation line is large even during the operation of the fuel cell, and there is a problem that the temperature of the fuel cell cannot be maintained only by the reaction heat of the fuel cell. Therefore, even after the start of power generation, it is necessary to operate the hot air generating furnace 18 to supply hot air, which requires extra fuel,
There was a problem that the plant efficiency deteriorated.
【０００５】また、従来の燃料電池発電設備では、上述
したように、改質器１０を出た燃焼排ガスを冷却・凝縮
して水分を除去しているため、例えば空気予熱器１３
ｂ、凝縮器１６ａ、気水分離器１５等を必要するとと共
に、凝縮熱によるヒートロスが大きく、プラント効率の
向上を妨げる一因となっていた。Further, in the conventional fuel cell power generation facility, as described above, the combustion exhaust gas discharged from the reformer 10 is cooled and condensed to remove water, so that, for example, the air preheater 13 is used.
b, the condenser 16a, the steam separator 15 and the like are required, and the heat loss due to the heat of condensation is large, which is one of the factors that hinder the improvement of plant efficiency.
【０００６】本発明はかかる問題点を解決するために創
案されたものである。すなわち、本発明の目的は、余分
な燃料を用いることなく、燃料電池の温度を所定範囲に
維持することができ、かつ排ガスの冷却・凝縮を最小限
に抑えて凝縮熱によるヒートロスを大幅に低減すると共
に、冷却・凝縮に必要な機器をなくし、設備のコンパク
ト化を図ることができる燃料電池発電設備を提供するこ
とにある。The present invention has been made to solve such a problem. That is, the object of the present invention is to maintain the temperature of the fuel cell within a predetermined range without using extra fuel, and to minimize the cooling / condensation of exhaust gas to significantly reduce the heat loss due to the heat of condensation. At the same time, it is an object of the present invention to provide a fuel cell power generation facility in which equipment required for cooling / condensing is eliminated and the equipment can be made compact.
【０００７】[0007]
【課題を解決するための手段】本発明によれば、燃料電
池のカソードガスを間接加熱する加熱器と、該加熱器に
高温ガスを供給する熱風発生炉と、該熱風発生炉に改質
器の燃焼室を出た燃焼排ガスを供給する排ガスライン
と、を備え、発電開始後に燃焼排ガスを熱風発生炉を通
して前記加熱器に供給する、ことを特徴とする燃料電池
発電設備が提供される。この構成により、燃焼室を出た
燃焼排ガスによりカソードガスを間接加熱することがで
き、余分な燃料を用いることなく、燃料電池の温度を所
定範囲に維持することができ、かつ燃焼排ガスの冷却・
凝縮によるヒートロスをなくし、プラント効率を大幅に
向上することができる。According to the present invention, a heater for indirectly heating cathode gas of a fuel cell, a hot air generating furnace for supplying high temperature gas to the heater, and a reformer for the hot air generating furnace. An exhaust gas line for supplying the combustion exhaust gas that has left the combustion chamber, and the combustion exhaust gas is supplied to the heater through a hot air generating furnace after the start of power generation. With this configuration, the cathode gas can be indirectly heated by the combustion exhaust gas that has left the combustion chamber, the temperature of the fuel cell can be maintained within a predetermined range without using extra fuel, and the combustion exhaust gas can be cooled and cooled.
Heat loss due to condensation can be eliminated, and plant efficiency can be significantly improved.
【０００８】本発明の好ましい実施形態によれば、ター
ビン圧縮機で加圧された空気を前記熱風発生炉に供給す
る空気供給ラインと、該空気供給ラインに設けられた空
気ブロアと、外気を空気ブロアに導く逆止弁と、を備え
る。この構成により、内圧が低い起動時には、空気ブロ
アにより逆止弁を通して外気を熱風発生炉に供給するこ
とができ、タービン圧縮機が駆動され内圧が高まってき
た段階では、タービン圧縮機で加圧された空気を空気ブ
ロアにより更に高圧にして熱風発生炉に供給することが
でき、起動から加圧運転時まで熱風発生炉に効率的に空
気を供給することができる。According to a preferred embodiment of the present invention, an air supply line for supplying the air pressurized by the turbine compressor to the hot air generating furnace, an air blower provided in the air supply line, and the outside air as air. And a check valve leading to the blower. With this configuration, at startup when the internal pressure is low, the outside air can be supplied to the hot air generating furnace by the air blower through the check valve, and when the turbine compressor is driven and the internal pressure increases, it is pressurized by the turbine compressor. The generated air can be supplied to the hot air generating furnace with a higher pressure by an air blower, and the air can be efficiently supplied to the hot air generating furnace from start-up to pressurization operation.
【０００９】また、排気用開閉弁を有し、加熱器を通過
した高温ガスをタービン圧縮機のタービン上流側に導く
排気ラインと、循環用開閉弁を有し、前記高温ガスを燃
料電池の上流側のカソードガスに導入する循環ライン
と、を備え、起動時には排気用開閉弁のみを開いて高温
ガスにより、タービン圧縮機を駆動し、発電開始後には
循環用開閉弁のみを開いて燃焼排ガスをカソードガスに
導入する、ことが好ましい。この構成により、起動時
に、高温ガスによりタービン圧縮機を駆動して空気を内
部に導入することができ、発電開始後にはＣＯ2 ガスを
含む燃焼排ガスをカソードガスに導入して電池反応に用
いることができる。なお、燃焼排ガスが混入されたカソ
ードガスは、燃料電池を通過後にその一部がタービン圧
縮機に供給されるため、発電開始後もタービン圧縮機に
より空気が導入される。[0009] Further, the exhaust gas has an on-off valve for exhausting the high-temperature gas passing through the heater to the upstream side of the turbine of the turbine compressor, and an on-off valve for circulation. A circulation line that is introduced into the cathode gas on the side of the turbine, and at startup, only the exhaust on-off valve is opened to drive the turbine compressor with high-temperature gas. It is preferably introduced into the cathode gas. With this configuration, the turbine compressor can be driven by the high temperature gas at the time of start-up to introduce the air into the inside, and after the power generation is started, the combustion exhaust gas containing the CO 2 gas is introduced into the cathode gas for use in the cell reaction. You can The cathode gas mixed with the combustion exhaust gas is partly supplied to the turbine compressor after passing through the fuel cell, so that air is introduced by the turbine compressor even after the start of power generation.
【００１０】[0010]
【発明の実施の形態】以下、本発明の好ましい実施形態
を図面を参照して説明する。なお、各図において共通す
る部分には同一の符号を付して使用する。図１は、本発
明による燃料電池発電設備の全体構成図である。この図
において、燃料電池発電設備は、燃料電池１１のカソー
ドガス３を間接加熱する加熱器１６ｂと、加熱器１６ｂ
に高温ガスを供給する熱風発生炉１８と、熱風発生炉１
８に改質器１０の燃焼室Ｃｏを出た燃焼排ガス５を供給
する排ガスライン２１と、を備え、発電開始後に燃焼排
ガス５を熱風発生炉１８を通して加熱器１６ｂに供給す
るようになっている。すなわち、本発明の燃料電池発電
設備には、図２の従来例に示した空気予熱器１３ｂ，凝
縮器１６ａ，気水分離器１５等がなく、燃焼室Ｃｏを出
た燃焼排ガス５が排ガスライン２１を介して熱風発生炉
１８に直接供給されるようになっている。DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will be described below with reference to the drawings. In the drawings, common parts are denoted by the same reference numerals. FIG. 1 is an overall configuration diagram of a fuel cell power generation facility according to the present invention. In this figure, the fuel cell power generation facility includes a heater 16b for indirectly heating the cathode gas 3 of the fuel cell 11 and a heater 16b.
Hot air generating furnace 18 for supplying high temperature gas to the hot air generating furnace 1
8 is provided with an exhaust gas line 21 for supplying the combustion exhaust gas 5 exiting the combustion chamber Co of the reformer 10, and the combustion exhaust gas 5 is supplied to the heater 16b through the hot air generating furnace 18 after the start of power generation. . That is, in the fuel cell power generation equipment of the present invention, the air preheater 13b, the condenser 16a, the steam separator 15 and the like shown in the conventional example of FIG. 2 are not provided, and the combustion exhaust gas 5 exiting the combustion chamber Co is the exhaust gas line. It is adapted to be directly supplied to the hot air generating furnace 18 via 21.
【００１１】この構成により、燃焼室Ｃｏを出た燃焼排
ガス５によりカソードガス３を間接加熱することがで
き、余分な燃料を用いることなく、燃料電池１１の温度
を所定範囲に維持することができ、かつ燃焼排ガス５の
冷却・凝縮によるヒートロスをなくし、プラント効率を
大幅に向上することができる。With this configuration, the cathode gas 3 can be indirectly heated by the combustion exhaust gas 5 exiting the combustion chamber Co, and the temperature of the fuel cell 11 can be maintained within a predetermined range without using extra fuel. In addition, heat loss due to cooling and condensation of the combustion exhaust gas 5 can be eliminated, and plant efficiency can be significantly improved.
【００１２】また、図１の燃料電池発電設備は、タービ
ン圧縮機１２で加圧された空気６を熱風発生炉１８に供
給する空気供給ライン２３と、空気供給ライン２３に設
けられた空気ブロア１７ｄと、外気を空気ブロア１７ｄ
に導く逆止弁２２と、を備えている。この構成により、
内圧が低い起動時には、空気ブロア１７ｄにより逆止弁
２２を通して外気を熱風発生炉１８に供給することがで
き、タービン圧縮機１２が駆動され内圧が高まってきた
段階では、タービン圧縮機１２で加圧された空気を空気
ブロア１７ｄにより更に高圧にして熱風発生炉１８に供
給することができ、起動から加圧運転時まで熱風発生炉
１８に効率的に空気を供給することができる。Further, in the fuel cell power generation facility of FIG. 1, an air supply line 23 for supplying the air 6 pressurized by the turbine compressor 12 to the hot air generating furnace 18 and an air blower 17d provided in the air supply line 23. And the outside air to the air blower 17d
And a check valve 22 that leads to. With this configuration,
At the time of starting when the internal pressure is low, the outside air can be supplied to the hot air generating furnace 18 through the check valve 22 by the air blower 17d, and when the turbine compressor 12 is driven and the internal pressure increases, the turbine compressor 12 pressurizes. The generated air can be further increased in pressure by the air blower 17d and supplied to the hot air generating furnace 18, and the air can be efficiently supplied to the hot air generating furnace 18 from startup to the pressurizing operation.
【００１３】更に、この発電設備は、加熱器１６ｂを通
過した高温ガスをタービン圧縮機１２のタービン上流側
に導く排気ライン２５と、高温ガスを燃料電池１１の上
流側のカソードガス３に導入する循環ライン２６と、を
備えている。また、排気ライン２５と循環ライン２６に
はそれぞれのラインを開閉させる排気用開閉弁２０ｂと
循環用開閉弁２０ａが設けられている。なお、この図で
２０ｃは、遮断弁であり、２４は、発電開始後の燃焼排
ガス５の流れを容易にするためのオリフィスである。Further, the power generation equipment introduces the high temperature gas, which has passed through the heater 16b, to the upstream side of the turbine of the turbine compressor 12, and the high temperature gas to the cathode gas 3 on the upstream side of the fuel cell 11. And a circulation line 26. The exhaust line 25 and the circulation line 26 are provided with an exhaust on-off valve 20b and a circulation on-off valve 20a for opening and closing the respective lines. In this figure, 20c is a shutoff valve, and 24 is an orifice for facilitating the flow of the combustion exhaust gas 5 after the start of power generation.
【００１４】この構成により、起動時には排気用開閉弁
２０ｂのみを開いて高温ガスにより、タービン圧縮機１
２を駆動し空気６を内部に導入することができ、発電開
始後には循環用開閉弁２０ａのみを開いてＣＯ2 ガスを
含む燃焼排ガス５をカソードガス３に導入して電池反応
に用いることができる。その他の構成は、図２と同様で
ある。With this configuration, at the time of startup, only the exhaust on-off valve 20b is opened and the high temperature gas allows the turbine compressor 1
2 can be driven to introduce air 6 into the interior, and after the start of power generation, only the circulation on-off valve 20a is opened to introduce the combustion exhaust gas 5 containing CO 2 gas into the cathode gas 3 for use in the cell reaction. it can. Other configurations are similar to those in FIG.
【００１５】なお、本発明は上述した実施形態に限定さ
れず、本発明の要旨を逸脱しない範囲で種々変更できる
ことは勿論である。The present invention is not limited to the above-mentioned embodiments, and it goes without saying that various modifications can be made without departing from the gist of the present invention.
【００１６】[0016]
【発明の効果】上述したように、本発明の燃料電池発電
設備は、余分な燃料を用いることなく、燃料電池の温度
を所定範囲に維持することができ、かつ排ガスの冷却・
凝縮を最小限に抑えて凝縮熱によるヒートロスを大幅に
低減すると共に、冷却・凝縮に必要な機器をなくし設備
のコンパクト化を図ることができる、等の優れた効果を
有する。As described above, the fuel cell power generation facility of the present invention can maintain the temperature of the fuel cell within a predetermined range without using extra fuel, and can cool exhaust gas.
Condensation is minimized to significantly reduce heat loss due to condensation heat, and the equipment required for cooling / condensation can be eliminated and equipment can be made compact.
【図１】本発明による燃料電池発電設備の全体構成図で
ある。FIG. 1 is an overall configuration diagram of a fuel cell power generation facility according to the present invention.
【図２】従来の燃料電池発電設備の全体構成図である。FIG. 2 is an overall configuration diagram of a conventional fuel cell power generation facility.
１ 燃料ガス ２ アノードガス ３ カソードガス ４ アノード排ガス ５ 燃焼排ガス ６ 空気 ７ カソード排ガス ８ 水蒸気 １０ 改質器 １１ 燃料電池 １２ タービン圧縮機 １３ａ 燃料予熱器 １３ｂ 空気予熱器 １４ 脱硫器 １５ 気水分離器 １６ａ 凝縮器 １６ｂ 加熱器 １７ａ 燃料ブロア １７ｂ 高温ブロア １７ｃ 低温ブロア １７ｄ 空気ブロア １８ 熱風発生炉 ２０ａ 循環用開閉弁 ２０ｂ 排気用開閉弁 ２０ｃ 遮断弁 ２１ 排ガスライン ２２ 逆止弁 ２３ 空気供給ライン ２４ オリフィス ２５ 排気ライン ２６ 循環ライン 1 Fuel Gas 2 Anode Gas 3 Cathode Gas 4 Anode Exhaust Gas 5 Combustion Exhaust Gas 6 Air 7 Cathode Exhaust Gas 8 Steam 10 Reformer 11 Fuel Cell 12 Turbine Compressor 13a Fuel Preheater 13b Air Preheater 14 Desulfurizer 15 Air Water Separator 16a Condenser 16b Heater 17a Fuel blower 17b High temperature blower 17c Low temperature blower 17d Air blower 18 Hot air generator 20a Circulation on / off valve 20b Exhaust on / off valve 20c Shutoff valve 21 Exhaust gas line 22 Check valve 23 Air supply line 24 Orifice 25 Exhaust line 26 Circulation line
Claims (3)
加熱器と、該加熱器に高温ガスを供給する熱風発生炉
と、該熱風発生炉に改質器の燃焼室を出た燃焼排ガスを
供給する排ガスラインと、を備え、発電開始後に燃焼排
ガスを熱風発生炉を通して前記加熱器に供給する、こと
を特徴とする燃料電池発電設備。1. A heater for indirectly heating a cathode gas of a fuel cell, a hot air generating furnace for supplying a high temperature gas to the heater, and a combustion exhaust gas discharged from a combustion chamber of a reformer for the hot air generating furnace. And a flue gas line for supplying combustion flue gas to the heater through a hot air generating furnace after power generation is started.
熱風発生炉に供給する空気供給ラインと、該空気供給ラ
インに設けられた空気ブロアと、外気を空気ブロアに導
く逆止弁と、を備えたことを特徴とする請求項１に記載
の燃料電池発電設備。2. An air supply line for supplying air pressurized by a turbine compressor to the hot air generating furnace, an air blower provided in the air supply line, and a check valve for guiding outside air to the air blower. The fuel cell power generation facility according to claim 1, further comprising:
高温ガスをタービン圧縮機のタービン上流側に導く排気
ラインと、循環用開閉弁を有し、前記高温ガスを燃料電
池の上流側のカソードガスに導入する循環ラインと、を
備え、起動時には排気用開閉弁のみを開いて高温ガスに
より、タービン圧縮機を駆動し、発電開始後には循環用
開閉弁のみを開いて燃焼排ガスをカソードガスに導入す
る、ことを特徴とする請求項１に記載の燃料電池発電設
備。3. An exhaust line having an exhaust on-off valve for guiding the high-temperature gas passing through the heater to a turbine upstream side of a turbine compressor, and a circulation on-off valve for transferring the high-temperature gas to an upstream side of a fuel cell. A circulation line that is introduced into the cathode gas on the side of the turbine, and at startup, only the exhaust on-off valve is opened to drive the turbine compressor with high-temperature gas. The fuel cell power generation facility according to claim 1, wherein the fuel cell power generation facility is introduced into the cathode gas.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21034795A JP3564812B2 (en) | 1995-08-18 | 1995-08-18 | Fuel cell power generation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21034795A JP3564812B2 (en) | 1995-08-18 | 1995-08-18 | Fuel cell power generation equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0963608A true JPH0963608A (en) | 1997-03-07 |
| JP3564812B2 JP3564812B2 (en) | 2004-09-15 |
Family
ID=16587902
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP21034795A Expired - Fee Related JP3564812B2 (en) | 1995-08-18 | 1995-08-18 | Fuel cell power generation equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3564812B2 (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1670090A1 (en) * | 2004-12-13 | 2006-06-14 | Ngk Insulators, Ltd. | Molten carbonate fuel cell, operating method thereof, sintering furnace, and power generator |
| CN100440596C (en) * | 2004-12-13 | 2008-12-03 | 日本碍子株式会社 | Fuel cell, operating method thereof, sintering furnace, and power generator |
| JP2009107915A (en) * | 2007-10-30 | 2009-05-21 | Samsung Sdi Co Ltd | Fuel reforming device and fuel cell system |
| USD922746S1 (en) | 2019-12-06 | 2021-06-22 | Nike, Inc. | Shoe |
| USD965262S1 (en) | 2020-03-24 | 2022-10-04 | Nike, Inc. | Shoe |
-
1995
- 1995-08-18 JP JP21034795A patent/JP3564812B2/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1670090A1 (en) * | 2004-12-13 | 2006-06-14 | Ngk Insulators, Ltd. | Molten carbonate fuel cell, operating method thereof, sintering furnace, and power generator |
| JP2006332017A (en) * | 2004-12-13 | 2006-12-07 | Ngk Insulators Ltd | Fuel cell and its operation method, baking furnace, and power generator |
| CN100440596C (en) * | 2004-12-13 | 2008-12-03 | 日本碍子株式会社 | Fuel cell, operating method thereof, sintering furnace, and power generator |
| JP2009107915A (en) * | 2007-10-30 | 2009-05-21 | Samsung Sdi Co Ltd | Fuel reforming device and fuel cell system |
| USD922746S1 (en) | 2019-12-06 | 2021-06-22 | Nike, Inc. | Shoe |
| USD965262S1 (en) | 2020-03-24 | 2022-10-04 | Nike, Inc. | Shoe |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3564812B2 (en) | 2004-09-15 |
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