JPH0722044A - Fuel cell power generating system - Google Patents

Fuel cell power generating system

Info

Publication number
JPH0722044A
JPH0722044A JP5164951A JP16495193A JPH0722044A JP H0722044 A JPH0722044 A JP H0722044A JP 5164951 A JP5164951 A JP 5164951A JP 16495193 A JP16495193 A JP 16495193A JP H0722044 A JPH0722044 A JP H0722044A
Authority
JP
Japan
Prior art keywords
exhaust gas
gas
fuel cell
cathode
concentration
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
Application number
JP5164951A
Other languages
Japanese (ja)
Other versions
JP3509132B2 (en
Inventor
Hajime Saito
一 斉藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
IHI Corp
Original Assignee
IHI Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by IHI Corp filed Critical IHI Corp
Priority to JP16495193A priority Critical patent/JP3509132B2/en
Publication of JPH0722044A publication Critical patent/JPH0722044A/en
Application granted granted Critical
Publication of JP3509132B2 publication Critical patent/JP3509132B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

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  • Fuel Cell (AREA)

Abstract

PURPOSE:To ensure safety even with gas leaks so as to restrain corrosion by providing a purge line, and supplying combustion exhaust that contains oxygen controlled to a predetermined concentration into a containment vessel. CONSTITUTION:A fuel cell 20 is contained in a containment vessel 22 and generates power from anode gas 2 containing hydrogen and cathode gas 3 containing oxygen. A node exhaust 4 emitted from the fuel cell 20 is burned with part of cathode exhaust 7, and a reformer 10 reforms combustion gas into anode gas by the heat of the burning. An exhaust circulation line 30 supplies the combustion exhaust from the reformer 10 to the cathode gas that enters the fuel cell 20, and a power recovery system 40 compresses air with the rest of the cathode gas from the fuel cell 20 and supplies the air to the line 30. Further, a controller 35 controls oxygen contained in the combustion exhaust 5 on line 30 to a predetermined concentration and a purge line 36 supplies the combustion exhaust with the controlled oxygen concentration to the vessel 22. Thereby safety is ensured even with leakage of the anode gas, and corrosion of the cell can be restrained while the operating cost of the purge gas is reduced.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、燃料電池発電装置に係
わり、更に詳しくは、溶融炭酸塩型燃料電池を用いた燃
料電池発電装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fuel cell power generator, and more particularly to a fuel cell power generator 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20とを一般的に備えて
おり、改質器で作られたアノードガスは燃料電池に供給
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10の燃焼室C
oに供給される。燃料ガス1は燃料予熱器11により予
熱されて改質器の改質室Reに入る。改質器ではアノー
ド排ガス中の可燃成分(水素、一酸化炭素、メタン等)
を燃焼室で燃焼し、高温の燃焼ガスにより改質室Reを
加熱し内部を流れる燃料を改質する。改質室を出た燃焼
排ガス5は、空気予熱器32で熱回収され、凝縮器33
と気水分離器34で水分を除去され、タービン圧縮機
(動力回収装置40)で加圧された空気6が混入し、こ
の混合ガスが空気予熱器32で加熱されてカソードガス
3に合流する。これにより、電池のアノード側で発生し
た二酸化炭素が、燃焼排ガス5を介して燃料電池用のカ
ソードガス3に入り、燃料電池のカソード反応に必要な
二酸化炭素をカソード側Cに供給する。カソードガス3
は燃料電池内でその一部が反応してカソード排ガス7と
なり、その一部はカソード入口側に再循環され、一部は
改質器10の燃焼室Coに供給されてアノード排ガス4
を燃焼させ、残りは動力回収装置40に供給されて圧力
回収され、系外に排出される。
2. Description of the Related Art Molten carbonate fuel cells have characteristics that conventional power generators do not have, such as high efficiency and little impact on the environment, and they are attracting attention as a power generation system following hydropower, thermal power, and nuclear power. Is currently being researched and developed all over the world. In particular, 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. A fuel cell 20 for generating power from an anode gas 2 and a cathode gas 3 containing oxygen is generally provided, and the anode gas produced by the reformer is supplied to the fuel cell, and most of it (in the fuel cell) (For example, 80%), the combustion chamber C of the reformer 10 is used as the anode exhaust gas 4.
supplied to the o. The fuel gas 1 is preheated by the fuel preheater 11 and enters the reforming chamber Re of the reformer. In the reformer, combustible components (hydrogen, carbon monoxide, methane, etc.) in the anode exhaust gas
Are burned in the combustion chamber and the high temperature combustion gas heats the reforming chamber Re to reform the fuel flowing inside. The combustion exhaust gas 5 that has exited the reforming chamber is subjected to heat recovery by the air preheater 32, and the condenser 33
The water 6 is removed by the steam separator 34 and the air 6 pressurized by the turbine compressor (power recovery device 40) is mixed, and this mixed gas is heated by the air preheater 32 and joins the cathode gas 3. . As a result, carbon dioxide generated on the anode side of the cell enters the cathode gas 3 for the fuel cell via the combustion exhaust gas 5, and supplies carbon dioxide required for the cathode reaction of the fuel cell to the cathode side C. Cathode gas 3
Is partially reacted in the fuel cell to form cathode exhaust gas 7, part of which is recirculated to the cathode inlet side, and part of which is supplied to the combustion chamber Co of the reformer 10 to form the anode exhaust gas 4
Is burned, and the rest is supplied to the power recovery device 40 to recover the pressure and is discharged to the outside of the system.

【0003】[0003]

【発明が解決しようとする課題】上述した燃料電池発電
装置では、燃料電池20は通常格納容器22に格納され
る。この場合、格納容器内には、アノードガスが漏洩し
た場合の安全対策のため、不活性ガス8(例えば、窒素
ガス)がパージガスとして供給されていた。しかし、酸
素を全く含まない不活性ガスをパージガスとすると、燃
料電池内の局所反応により電池を構成する金属部品(例
えばセパレータ)が激しく腐食することがわかった。ま
た、不活性ガスをパージガスとする場合、運転コストが
かかる問題点があった。
In the above-mentioned fuel cell power generator, the fuel cell 20 is normally stored in the storage container 22. In this case, an inert gas 8 (for example, nitrogen gas) was supplied as a purge gas into the storage container as a safety measure when the anode gas leaks. However, it has been found that when an inert gas containing no oxygen is used as a purge gas, a metal component (eg, a separator) constituting the cell is severely corroded by a local reaction in the fuel cell. Further, there is a problem in that operating cost is required when the inert gas is used as the purge gas.

【0004】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、アノ
ードガスが漏洩しても安全であり、電池の腐食を抑える
ことができ、かつパージガスの運転コストがかからない
燃料電池発電装置を提供することにある。
The present invention was created to solve such problems. That is, an object of the present invention is to provide a fuel cell power generator that is safe even if the anode gas leaks, can suppress the corrosion of the cell, and does not incur the operating cost of the purge gas.

【0005】[0005]

【課題を解決するための手段】本発明によれば、格納容
器内に格納され、水素を含むアノードガスと酸素を含む
カソードガスとから発電する燃料電池と、燃料電池を出
たアノード排ガスをカソード排ガスの一部で燃焼させそ
の熱で燃料ガスをアノードガスに改質する改質器と、改
質器を出た燃焼排ガスを燃料電池に入るカソードガスに
供給する排ガス循環ラインと、燃料電池を出たカソード
排ガスの残部で空気を圧縮して排ガス循環ラインに供給
する動力回収装置と、を備えた燃料電池発電装置におい
て、前記排ガス循環ラインは、燃焼排ガスに含まれる酸
素を所定の濃度に制御する濃度制御装置と、酸素濃度が
制御された燃焼排ガスを格納容器内に供給するパージラ
インとを備える、ことを特徴とする燃料電池発電装置が
提供される。
According to the present invention, a fuel cell which is stored in a storage container and generates electricity from an anode gas containing hydrogen and a cathode gas containing oxygen, and an anode exhaust gas discharged from the fuel cell to a cathode A reformer that burns part of the exhaust gas and uses the heat to reform the fuel gas into the anode gas, an exhaust gas circulation line that supplies the combustion exhaust gas that exits the reformer to the cathode gas that enters the fuel cell, and the fuel cell In a fuel cell power generator comprising: a power recovery device that compresses air with the remaining cathode exhaust gas and supplies the compressed air to the exhaust gas circulation line, the exhaust gas circulation line controls oxygen contained in the combustion exhaust gas to a predetermined concentration. And a purge line for supplying the combustion exhaust gas with controlled oxygen concentration into the storage container.

【0006】本発明の好ましい実施例によれば、前記濃
度制御装置は、燃焼排ガスに含まれる酸素濃度を検出す
る酸素センサーと、該酸素センサーによる検出濃度が所
定濃度になるように排ガス循環ラインに設けられたブロ
アの流量を制御する流量制御装置とを備える。前記所定
の濃度は約3%である、ことが好ましい。
According to a preferred embodiment of the present invention, the concentration control device comprises an oxygen sensor for detecting the oxygen concentration contained in the combustion exhaust gas, and an exhaust gas circulation line so that the concentration detected by the oxygen sensor becomes a predetermined concentration. And a flow rate control device for controlling the flow rate of the blower provided. Preferably, the predetermined concentration is about 3%.

【0007】[0007]

【作用】上記本発明の構成によれば、排ガス循環ライン
が濃度制御装置を備えており、この濃度制御装置によ
り、燃焼排ガスに含まれる酸素が所定の濃度に制御さ
れ、酸素濃度が制御された燃焼排ガスがパージラインに
より格納容器内に供給される。従って、所定濃度の酸素
を含むパージガスにより格納容器内でアノードガスが漏
洩しても安全であり、かつ電池の腐食を抑えることがで
きる。前記所定の濃度を約3%とすれば、安全性と電池
の腐食抑制の両方を満たすことができる。
According to the above-mentioned structure of the present invention, the exhaust gas circulation line is provided with the concentration control device, and by this concentration control device, the oxygen contained in the combustion exhaust gas is controlled to a predetermined concentration and the oxygen concentration is controlled. The combustion exhaust gas is supplied into the containment vessel through the purge line. Therefore, it is safe even if the anode gas leaks in the storage container due to the purge gas containing a predetermined concentration of oxygen, and the corrosion of the battery can be suppressed. When the predetermined concentration is about 3%, both safety and suppression of battery corrosion can be satisfied.

【0008】また、上記流量制御装置により、酸素セン
サーによる検出濃度が所定濃度になるように排ガス循環
ラインに設けられたブロアの流量を制御すれば、パージ
ガスを自給することができ、パージガスの運転コストを
大幅に低減することができる。
If the flow rate control device controls the flow rate of the blower provided in the exhaust gas circulation line so that the concentration detected by the oxygen sensor becomes a predetermined concentration, the purge gas can be self-supplied and the operating cost of the purge gas can be reduced. Can be significantly reduced.

【0009】[0009]

【実施例】以下に本発明の好ましい実施例を図面を参照
して説明する。なお、図2と同一の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
装置の全体構成図である。この図において、本発明によ
る燃料電池発電装置は、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20
と、改質器10を出た燃焼排ガス5から熱回収する空気
予熱器32とを備えている。改質器10は、燃料電池2
0を出たアノードガス(すなわちアノード排ガス4)を
燃料電池20を出たカソードガス(すなわちカソード排
ガス7)の一部で燃焼させその熱で燃料ガス1をアノー
ドガス2に改質するようになっている。また燃料電池2
0は、格納容器22内に格納されている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT A preferred embodiment of the present invention will be described below with reference to the drawings. The same parts as those in FIG. 2 are designated by the same reference numerals and used. FIG. 1 is an overall configuration diagram of a fuel cell power generator according to the present invention. In this figure, a fuel cell power generator according to the present invention includes a reformer 10 for reforming a fuel gas 1 into an anode gas 2 containing hydrogen, and a fuel cell 20 for generating power from an anode gas 2 and a cathode gas 3 containing oxygen.
And an air preheater 32 for recovering heat from the combustion exhaust gas 5 exiting the reformer 10. The reformer 10 is a fuel cell 2
The anode gas (ie, the anode exhaust gas 4) having a value of 0 is burned by a part of the cathode gas (ie, the cathode exhaust gas 7), which has exited the fuel cell 20, and the heat thereof reforms the fuel gas 1 into the anode gas 2. ing. Fuel cell 2
0 is stored in the storage container 22.

【0010】本発明による燃料電池発電装置は、更に、
改質器10を出た燃焼排ガス5を燃料電池20に入るカ
ソードガス3に供給する排ガス循環ライン30と、燃料
電池20を出たカソード排ガス7の残部で空気を圧縮し
て排ガス循環ライン30に供給する動力回収装置40と
を備えている。排ガス循環ライン30は、燃焼排ガス5
に含まれる酸素を所定の濃度に制御する濃度制御装置3
5と、酸素濃度が制御された燃焼排ガスを格納容器22
内に供給するパージライン36とを備える。濃度制御装
置35は、燃焼排ガスに含まれる酸素濃度を検出する酸
素センサー37と、この酸素センサーによる検出濃度が
所定濃度になるように排ガス循環ラインに設けられた循
環ブロア38の流量を制御する流量制御装置39とを備
える。前記所定の濃度は約3%であるのがよい。
The fuel cell power generator according to the present invention further comprises:
The exhaust gas circulation line 30 that supplies the combustion exhaust gas 5 that has exited the reformer 10 to the cathode gas 3 that enters the fuel cell 20, and the remaining portion of the cathode exhaust gas 7 that exits the fuel cell 20 compresses air to the exhaust gas circulation line 30. And a power recovery device 40 for supplying the power. The exhaust gas circulation line 30 is connected to the combustion exhaust gas 5
Concentration control device 3 for controlling the oxygen contained in water to a predetermined concentration
5 and the combustion exhaust gas whose oxygen concentration is controlled
And a purge line 36 for supplying the inside. The concentration control device 35 controls the flow rate of an oxygen sensor 37 for detecting the oxygen concentration contained in the combustion exhaust gas and a flow rate of a circulation blower 38 provided in the exhaust gas circulation line so that the concentration detected by the oxygen sensor becomes a predetermined concentration. And a control device 39. The predetermined concentration may be about 3%.

【0011】上述した濃度制御装置35は、次のように
作動する。 燃焼排ガス5に含まれる酸素濃度が所定の濃度より高
い場合、この濃度を酸素センサー37が検出し、流量制
御装置39により循環ブロア38の流量を小さくする。
これにより、カソード排ガス7の残部(動力回収装置4
0に導かれる)が減少し、動力回収装置40からの空気
6の供給が減って、燃焼排ガス5に含まれる酸素濃度が
減少する。 逆に、燃焼排ガス5に含まれる酸素濃度が所定の濃度
より低い場合、この濃度を酸素センサー37が検出し、
流量制御装置39により循環ブロア38の流量を大きく
する。これにより、カソード排ガス7が増大し、動力回
収装置40からの空気6の供給が増えて、燃焼排ガス5
に含まれる酸素濃度が増大する。
The above-mentioned concentration controller 35 operates as follows. When the oxygen concentration contained in the combustion exhaust gas 5 is higher than a predetermined concentration, the oxygen sensor 37 detects this concentration, and the flow control device 39 reduces the flow rate of the circulation blower 38.
As a result, the remainder of the cathode exhaust gas 7 (power recovery device 4
(Leading to 0) is reduced, the supply of air 6 from the power recovery device 40 is reduced, and the concentration of oxygen contained in the combustion exhaust gas 5 is reduced. On the contrary, when the oxygen concentration contained in the combustion exhaust gas 5 is lower than the predetermined concentration, the oxygen sensor 37 detects this concentration,
The flow controller 39 increases the flow rate of the circulation blower 38. As a result, the cathode exhaust gas 7 increases, the supply of the air 6 from the power recovery device 40 increases, and the combustion exhaust gas 5 increases.
The oxygen concentration contained in is increased.

【0012】[0012]

【発明の効果】上述した構成により、酸素濃度が制御さ
れた燃焼排ガスがパージライン36により格納容器22
内に供給され、所定濃度(好ましくは約3%)の酸素を
含むパージガスにより格納容器22内でアノードガス2
が漏洩しても安全であり、かつ電池の腐食を抑えること
ができる。また、流量制御装置39により、酸素センサ
ー37による検出濃度が前記所定濃度になるように排ガ
ス循環ライン30に設けられた循環ブロアの流量を制御
するので、パージガスを自給することができ、パージガ
スの運転コストを大幅に低減することができる。
With the above-described structure, the combustion exhaust gas with controlled oxygen concentration is supplied to the storage container 22 by the purge line 36.
Is supplied to the anode gas 2 in the storage container 22 by a purge gas containing oxygen of a predetermined concentration (preferably about 3%).
Is safe even if leaked, and the corrosion of the battery can be suppressed. Further, since the flow rate control device 39 controls the flow rate of the circulation blower provided in the exhaust gas circulation line 30 so that the concentration detected by the oxygen sensor 37 becomes the predetermined concentration, the purge gas can be self-supplied and the purge gas can be operated. The cost can be reduced significantly.

【0013】従って、本発明は、アノードガスが漏洩し
ても安全であり、電池の腐食を抑えることができ、かつ
パージガスの運転コストがかからない、等の優れた効果
を有する。
Therefore, the present invention has excellent effects such that it is safe even if the anode gas leaks, the corrosion of the battery can be suppressed, and the operating cost of the purge gas is low.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明による燃料電池発電装置の全体構成図で
ある。
FIG. 1 is an overall configuration diagram of a fuel cell power generator according to the present invention.

【図2】従来の燃料電池発電装置の全体構成図である。FIG. 2 is an overall configuration diagram of a conventional fuel cell power generator.

【符号の説明】[Explanation of symbols]

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 パージガス 10 改質器 11 燃料予熱器 20 燃料電池 22 格納容器 30 排ガス循環ライン 32 空気予熱器 33 凝縮器 34 気水分離器 35 濃度制御装置 36 パージライン 37 酸素センサー 38 循環ブロア 39 流量制御装置 40 動力回収装置 Re 改質室 Co 燃焼室 A アノード側 C カソード側 1 Fuel Gas 2 Anode Gas 3 Cathode Gas 4 Anode Exhaust Gas 5 Combustion Exhaust Gas 6 Air 7 Cathode Exhaust Gas 8 Purge Gas 10 Reformer 11 Fuel Preheater 20 Fuel Cell 22 Containment Vessel 30 Exhaust Gas Circulation Line 32 Air Preheater 33 Condenser 34 Gas Water Separator 35 Concentration control device 36 Purge line 37 Oxygen sensor 38 Circulation blower 39 Flow rate control device 40 Power recovery device Re Reforming chamber Co Combustion chamber A Anode side C Cathode side

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 格納容器内に格納され、水素を含むアノ
ードガスと酸素を含むカソードガスとから発電する燃料
電池と、燃料電池を出たアノード排ガスをカソード排ガ
スの一部で燃焼させその熱で燃料ガスをアノードガスに
改質する改質器と、改質器を出た燃焼排ガスを燃料電池
に入るカソードガスに供給する排ガス循環ラインと、燃
料電池を出たカソード排ガスの残部で空気を圧縮して排
ガス循環ラインに供給する動力回収装置と、を備えた燃
料電池発電装置において、 前記排ガス循環ラインは、燃焼排ガスに含まれる酸素を
所定の濃度に制御する濃度制御装置と、酸素濃度が制御
された燃焼排ガスを格納容器内に供給するパージライン
とを備える、ことを特徴とする燃料電池発電装置。
1. A fuel cell, which is stored in a storage container and generates electricity from an anode gas containing hydrogen and a cathode gas containing oxygen, and an anode exhaust gas that has exited the fuel cell is burned in a part of the cathode exhaust gas to generate heat. A reformer that reforms fuel gas into anode gas, an exhaust gas circulation line that supplies the combustion exhaust gas that exits the reformer to the cathode gas that enters the fuel cell, and the air that is compressed by the remainder of the cathode exhaust gas that exits the fuel cell. In the fuel cell power generation device including a power recovery device that supplies the exhaust gas circulation line to the exhaust gas circulation line, the exhaust gas circulation line is a concentration control device that controls oxygen contained in the combustion exhaust gas to a predetermined concentration, and the oxygen concentration is controlled. A purge line for supplying the generated combustion exhaust gas into the storage container.
【請求項2】 前記濃度制御装置は、燃焼排ガスに含ま
れる酸素濃度を検出する酸素センサーと、該酸素センサ
ーによる検出濃度が所定濃度になるように排ガス循環ラ
インに設けられたブロアの流量を制御する流量制御装置
とを備える、ことを特徴とする請求項1に記載の燃料電
池発電装置。
2. The concentration control device controls an oxygen sensor for detecting the oxygen concentration contained in the combustion exhaust gas, and a flow rate of a blower provided in the exhaust gas circulation line so that the concentration detected by the oxygen sensor becomes a predetermined concentration. The fuel cell power generator according to claim 1, further comprising:
【請求項3】 前記所定の濃度は約3%である、ことを
特徴とする請求項1に記載の燃料電池発電装置。
3. The fuel cell power generator according to claim 1, wherein the predetermined concentration is about 3%.
JP16495193A 1993-07-05 1993-07-05 Fuel cell power generator Expired - Fee Related JP3509132B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16495193A JP3509132B2 (en) 1993-07-05 1993-07-05 Fuel cell power generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16495193A JP3509132B2 (en) 1993-07-05 1993-07-05 Fuel cell power generator

Publications (2)

Publication Number Publication Date
JPH0722044A true JPH0722044A (en) 1995-01-24
JP3509132B2 JP3509132B2 (en) 2004-03-22

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ID=15802967

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3509132B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997044844A1 (en) * 1996-05-22 1997-11-27 Mtu Motoren- Und Turbinen-Union Friedrichshafen Gmbh Process for operating a fuel cell arrangement
DE112022003401T5 (en) 2021-07-05 2024-04-18 Blue World Technologies Holding ApS Electric motor vehicle with a fuel cell system and method for limiting fire risks

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997044844A1 (en) * 1996-05-22 1997-11-27 Mtu Motoren- Und Turbinen-Union Friedrichshafen Gmbh Process for operating a fuel cell arrangement
DE112022003401T5 (en) 2021-07-05 2024-04-18 Blue World Technologies Holding ApS Electric motor vehicle with a fuel cell system and method for limiting fire risks

Also Published As

Publication number Publication date
JP3509132B2 (en) 2004-03-22

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