JPS5913152B2 - How to start a fuel cell power generation system - Google Patents
How to start a fuel cell power generation systemInfo
- Publication number
- JPS5913152B2 JPS5913152B2 JP55014034A JP1403480A JPS5913152B2 JP S5913152 B2 JPS5913152 B2 JP S5913152B2 JP 55014034 A JP55014034 A JP 55014034A JP 1403480 A JP1403480 A JP 1403480A JP S5913152 B2 JPS5913152 B2 JP S5913152B2
- Authority
- JP
- Japan
- Prior art keywords
- fuel cell
- inverter
- voltage
- power generation
- generation system
- 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.)
- Expired
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
- H01M8/04298—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
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
- H01M8/04694—Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
- H01M8/04955—Shut-off or shut-down of 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
- H01M8/04694—Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
- H01M8/04858—Electric variables
- H01M8/04865—Voltage
-
- 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
- H01M8/04694—Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
- H01M8/04858—Electric variables
- H01M8/04895—Current
- H01M8/0491—Current of fuel cell stacks
-
- 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
- H01M8/04694—Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
- H01M8/04746—Pressure; Flow
- H01M8/04753—Pressure; Flow of fuel cell reactants
-
- 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
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Inverter Devices (AREA)
- Fuel Cell (AREA)
Description
【発明の詳細な説明】
本発明は、燃料電池からインバータを介して交流系統へ
電力を供給する熱料電池発電システムの始動方法に関す
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for starting a thermal power generation system that supplies power from a fuel cell to an AC system via an inverter.
第1図はこの種の燃料電池発電システムの原理的構成を
示す。FIG. 1 shows the basic configuration of this type of fuel cell power generation system.
燃料電池1はここでは、燃料ガスとして水素ガスを使用
し、酸化剤ガスとして空気を使用するタイプの燃料電池
として略示されている。燃料電池の正、負極端子間には
直流リアクトル20を介してインバータ2が接続され、
このインバータ2の交流出力端子は変圧器30を介して
交流系統3に接続されている。インバータ2は、例えば
3相ブリッジ結線されたサイリスタからなる他励インバ
ータとして構成することができる。このインバータの制
御進み角βは、例えば直流電流Idを目標値Id”に一
致させる働きをする電流調節器21によつて制御される
。目標値Idは図示されていないポテンショメータある
いは電力調節器によつて与えることができる。制御進み
角βを決定する調節器21の出力信号は逆変換動作領域
において定められた最大制御進み角βm急xと逆変換動
作転流限界に応じて定められた最小制御進み角β一との
間でのみ制御進み角が変化されるように制限される。イ
ンバータ2の直流側には系統電圧が燃料電池1の電圧E
1に対抗する直流逆電圧E2として現われ、燃料電池1
とインバータ・との間の差電圧E1−E2によつて直流
電流11が流される。The fuel cell 1 is schematically shown here as a fuel cell of the type that uses hydrogen gas as the fuel gas and air as the oxidant gas. An inverter 2 is connected between the positive and negative terminals of the fuel cell via a DC reactor 20.
An AC output terminal of this inverter 2 is connected to an AC system 3 via a transformer 30. The inverter 2 can be configured as a separately excited inverter including, for example, three-phase bridge-connected thyristors. The control advance angle β of this inverter is controlled by a current regulator 21 that functions to match, for example, the DC current Id with a target value Id.The target value Id is controlled by a potentiometer or a power regulator (not shown). The output signal of the regulator 21 that determines the control advance angle β is the maximum control advance angle βm steep x determined in the inverse conversion operation region and the minimum control determined according to the inverse conversion operation commutation limit. The control advance angle is limited to be changed only between the advance angle β and the lead angle β.The system voltage on the DC side of the inverter 2 is
appears as a DC reverse voltage E2 opposing the fuel cell 1
A direct current 11 is caused to flow due to the voltage difference E1-E2 between the inverter and the inverter.
インバータ直流逆電圧E2はイン’S■、制御進み角β
の関数であり、制御進み角β゛が小、さいほど大b値を
とる。一般的な他励インパータシネテ^にキいては、始
動時に制、御進み角βを最大値′一から出発させてゆる
やかに大きくしてゆ〈ことによつて直流電流の立上がり
速度を管理しながら、いわゆるソフトスタートを行なつ
ている。か\るソフトスタートを可能にするためには、
インバータ2の最大可能な逆電圧(β=βiのときのE
2の値)が燃料電池1の無負荷電圧(Id=0のときの
E1の値)よシも大きいことが必要である。ところが、
燃料電池1はかなジ激しい垂下特性を有し、定格負荷時
の燃料電池電圧は無負荷電圧値に比べてかなり降下する
ために、上述のようにソフトスタートのために燃料電池
無負荷電圧に十分に対抗できるインバータ直流逆電圧を
出し得るようにインバータの交流側の電圧値を選ぶと、
定格電流を与える動作点では制御進み角βがかなり大き
くなつてしまう。制御進み角βはインバータの運転力率
に相当するものであるので、制御進み角βが大きくなる
ということは、インバータ運転力率が悪くなり、インバ
ータが交流系統に生ぜしめる無幼電力が大きくなるとい
うことを意味する。この不都合を避けるために定格負荷
時のインバータ運転力率が良好になるようにインバータ
の交流側の電圧値を選べば、燃料電池の無負荷電圧に十
分対抗し得るインバータ直流逆電圧を出させることがで
きなくなり、ソフトスタートが不可能となつて始動時に
電流突入が起きてしまう。そこで、ソフトスタートと定
格負荷時の良好なるインバータカ率とのいずれをも満足
するために、種々の方法が検討されてきた。Inverter DC reverse voltage E2 is in'S■, control advance angle β
It is a function of , and the smaller the control advance angle β', the larger the b value. In a typical separately-excited inverter, the control and advance angle β is started from the maximum value '1 and then gradually increased at the time of startup, thereby controlling the rising speed of the DC current. A so-called soft start is being performed. In order to enable a soft start,
Maximum possible reverse voltage of inverter 2 (E when β = βi
2) is required to be larger than the no-load voltage of the fuel cell 1 (the value of E1 when Id=0). However,
The fuel cell 1 has a drooping characteristic and the fuel cell voltage under rated load drops considerably compared to the no-load voltage value. If you choose the voltage value on the AC side of the inverter so that it can produce an inverter DC reverse voltage that can counter the
At the operating point where the rated current is given, the control advance angle β becomes considerably large. Since the control advance angle β corresponds to the inverter's operating power factor, an increase in the control advance angle β means that the inverter's operating power factor becomes worse and the inverter's inert power generated in the AC system increases. It means that. In order to avoid this inconvenience, if the voltage value on the AC side of the inverter is selected so that the inverter operating power factor at rated load is good, the inverter can generate a DC reverse voltage that can sufficiently counter the no-load voltage of the fuel cell. As a result, soft start becomes impossible and current inrush occurs at startup. Therefore, various methods have been studied in order to satisfy both soft start and good inverter power ratio at rated load.
その一つとしてインバータの交流側の電圧値を負荷状態
に応じて切り換えることにより、ソフトスタートを可能
にすると同時に無負荷から定格負荷までの全範囲にわた
つてインバータ運転力率を良好に保つ方法がある。しか
しながら、この方法を実施するためには変圧器30とし
て非常に高価な負荷時タツプ切換装置付き変圧器を使用
しなければならない。また、燃料電池とインバータとの
間の直流回路にサイリスタチヨツパおよび電圧平滑フイ
ルタを挿入することにより、燃料電池電圧が負荷に依存
して変化してもほY一定の平滑された電圧が直流リアク
トル20を介してインパータ2に印加されるようにする
という方法も考えられた。しかしながら、この方法も同
様に高価な付加的設備を必要とする難点がある。さらに
、複数個の抵抗器からなる始動抵抗器を直流電流器に挿
入して、それらの抵抗器を順次短絡してゆくことにより
電流を制限しながら始動を行なう方法、あるいは複数個
の抵抗器からなるダミー負荷を燃料電池に接続して燃料
電池電圧を引き下げておいてそれらの抵抗器を順次切り
離してゆくことにより燃料電池電圧の変動幅を小さく抑
えながら始動する方法が検討されてきた。しかしながら
、これらの方法も抵抗器群とこれらの順次短絡ないし開
放のための開閉装置とを設ける必要があり、これらは無
視できない費用を必要とし、大がかりな付加的設備とな
るという難点を有する。本発明の目的は上記に鑑み、小
規模な安価な付加的装置にて、もしくはとくに取り挙げ
て言うほどの付加的装置なしに、定格負荷時のインバー
タ運転力率を犠性にすることなしに円滑な始動を可能に
する方法を提供することにある。One method is to switch the voltage value on the AC side of the inverter according to the load condition, thereby making soft start possible and at the same time maintaining a good inverter operating power factor over the entire range from no load to rated load. be. However, in order to carry out this method, a very expensive transformer with an on-load tap changer must be used as the transformer 30. In addition, by inserting a thyristor chopper and a voltage smoothing filter into the DC circuit between the fuel cell and the inverter, even if the fuel cell voltage changes depending on the load, a smoothed voltage that remains constant is maintained as a direct current. A method of applying power to the imperter 2 via the reactor 20 has also been considered. However, this method also has the disadvantage of requiring expensive additional equipment. Furthermore, there is a method of starting while limiting the current by inserting a starting resistor consisting of multiple resistors into a DC current generator and short-circuiting those resistors one after another, or a method of starting while limiting the current. Consideration has been given to a method of starting the engine while minimizing fluctuations in the fuel cell voltage by connecting a dummy load to the fuel cell to lower the fuel cell voltage and sequentially disconnecting the resistors. However, these methods also require the provision of a resistor group and a switching device for sequentially shorting or opening them, which requires considerable expense and has the disadvantage of requiring large-scale additional equipment. In view of the above, an object of the present invention is to provide a small-scale, inexpensive additional device, or without any special additional device, without sacrificing the inverter operating power factor at rated load. The object of the present invention is to provide a method that enables smooth startup.
この目的は、本発明によれば、特許請求の範囲に記載さ
れている構成事項からなる始動方法によつて達成される
。This object is achieved according to the invention by a starting method comprising the features specified in the claims.
本発明による始動方法において重要なことは、まず燃料
電池内のガス室の少なくとも一方が不活性ガス雰囲気に
置かれている状態でそのガス室に反応ガスの供給を開始
することである。What is important in the startup method according to the present invention is to first start supplying the reactant gas to at least one of the gas chambers in the fuel cell while the gas chamber is placed in an inert gas atmosphere.
これにより燃料電池電圧は、零もしくは低い値から出発
して、該当反応ガスの供給により不活性ガス濃度が減少
してゆくのにともなつてゆるやかに上昇してゆく。不活
性ガスとしては窒素ガスを使用することができる。不活
性ガスを満たされるガス室は酸化剤ガス室および燃料ガ
ス室の両方であつてもよいが、しかしいずれか一方で十
分であり、このほうが、とくに外部からの不活性ガス供
給を行なう場合にはその都度必要な不活性ガス量が少な
くてすむ。不活性ガス雰囲気を形成させるため付加され
る不活性ガス源は、従来の解決法において必要な付加的
設備に比べれば小規模で安価なものにすることができる
ばかりでなく、次のような場合には特別な不活性ガス源
は省略することができる。すなわち、燃料電池の緊急停
止を可能にする目的で、緊急停止時に例えば燃料ガス室
に不活性ガスを注入する不活性ガス源が設置されている
場合には、これを流用することができる。さらに、空気
を酸化剤ガスとして使用する燃料電池にあつては、空気
供給をしや断することにより停止を行なうようにすれば
、空気供給しや断後ガス室内の空気中の酸素のみが放電
により消費されて不活性ガスがガス室に残留するので、
次に始動するときには外部から不活性ガスを供給する必
要がなくなる。したがつて、この場合には最初の始動も
しくは万一のために小形の窒素ボンベを用意するだけで
十分である。しかし、燃料電池に直接に接続できる適当
な負荷が存在する場合には、空気供給しや断状態でこの
負荷を接続して燃料電池を予備運転すれば、酸化剤ガス
室を不活性ガス雰囲気状態にすることができる。したが
つて、必要に応じてその負荷を切り離した後、インバー
タを組み合せた正規運転に移行するようにすれば、不活
性ガス源なしに本発明による始動方法を実行することが
できる。本発明による始動方法におけるもう一つの重要
な点はインバータ制御パルスの供給開始直後に燃料電池
電圧E1がこのときに生じるインバータ直流逆電圧E2
を既に本質的に土回つてしまうほど、すなわち許容でき
ない電流突入が生じてしまうほどインバータ制御パルス
の供給開始を遅らせてはならないことである。インバー
タ制御パルスの供給開始時点でのインバータ制御進み角
βの値が決まつている場合にはこれに対応するインバー
タ直流逆電圧の値を燃料電池電圧が上回るや否やインバ
ータへの制御パルスの供給を開始するのが理想的である
。しかしながら、このためには燃料電池電圧を監視する
必要があシめんどうであるし、インバータへの制御パル
ス供給開始を燃料電池への反応ガス(例えば空気)供給
開始と同時に行なつたとしても何ら問題は生じないので
、これで十分である。この場合にはインバータ制御進み
角に対応するインバータ直流逆電圧に相当する値まで燃
料電流電圧が上昇したときに直流電流1dが流れ始める
。第2図は、本発明者らが行なつた実験例での空気一水
素式燃料電池の電圧E1と直流電流1dの時間経過の一
例を示す。As a result, the fuel cell voltage starts from zero or a low value and gradually increases as the inert gas concentration decreases due to the supply of the corresponding reactant gas. Nitrogen gas can be used as the inert gas. The gas chamber filled with inert gas can be both an oxidizer gas chamber and a fuel gas chamber, but either one is sufficient, especially if an external inert gas supply is provided. The amount of inert gas required each time is small. The inert gas source added to create the inert gas atmosphere can not only be small and inexpensive compared to the additional equipment required in traditional solutions, but also A special inert gas source can be omitted. That is, if an inert gas source is installed, for example, to inject inert gas into the fuel gas chamber at the time of an emergency stop in order to enable an emergency stop of the fuel cell, this can be used. Furthermore, in the case of fuel cells that use air as the oxidant gas, if the shutdown is performed by cutting off the air supply, only the oxygen in the air in the gas chamber will be discharged after the air supply is cut off. Since the inert gas is consumed by and remains in the gas chamber,
When starting the engine next time, there is no need to supply inert gas from outside. Therefore, in this case it is sufficient to have a small nitrogen cylinder available for initial startup or just in case. However, if there is a suitable load that can be directly connected to the fuel cell, if the load is connected and the fuel cell is pre-operated with the air supply cut off, the oxidizer gas chamber will be in an inert gas atmosphere. It can be done. Therefore, the starting method according to the present invention can be carried out without an inert gas source by disconnecting the load as necessary and then proceeding to normal operation using the inverter. Another important point in the starting method according to the present invention is that immediately after the start of supply of inverter control pulses, the fuel cell voltage E1 changes from the inverter DC reverse voltage E2 generated at this time.
The start of the supply of the inverter control pulses must not be delayed so much that it essentially undermines the current flow, ie, an unacceptable current inrush occurs. If the value of the inverter control advance angle β at the time of starting the supply of inverter control pulses is determined, the control pulses are supplied to the inverter as soon as the fuel cell voltage exceeds the value of the corresponding inverter DC reverse voltage. Ideally, start. However, for this purpose, it is necessary to monitor the fuel cell voltage, which is troublesome, and even if the supply of control pulses to the inverter is started at the same time as the supply of reactant gas (for example, air) to the fuel cell, there will be no problem. does not occur, so this is sufficient. In this case, when the fuel current voltage rises to a value corresponding to the inverter DC reverse voltage corresponding to the inverter control advance angle, the DC current 1d starts flowing. FIG. 2 shows an example of the time course of voltage E1 and direct current 1d of an air-hydrogen fuel cell in an experimental example conducted by the present inventors.
インバータ2の制御は第1図に示すように電流調節器2
1による定電流制御とし、目標値1d*として一定値2
0Aを設定した。燃料電池1の酸化剤ガス室は窒素雰囲
気状態におき時点t=oにおいて空気供給とインバータ
制御パルス供給とを開始する指令を与えた。この時点か
ら遅れた時点t1で燃料電池電圧E1が立上がり始める
。このとき調節器21の出力信号は、E1くE2のため
電流1dが流れないことから最大制御進み角βMax(
80流程度に設定)に相当する値にへばりついている。
燃料電池電圧E1がインバータ直流逆電圧E2を土回る
や否や(時点T2)直流電流1dが立ち上がシ始める。
それから直流電流1dは燃料電池電圧E1の上昇にとも
なつて上昇してゆき、時点T3において目標値1d*=
20Aに達する。これ以降電流調節器21による定電流
制御ループが働き、燃料電池電圧E1の上昇にともなつ
て、それまでは最大制御進み角βMaxにへばりついて
いた制御進み角βが最小制御進み角βiの方向へ移動し
てゆく。時点T4−CWil化剤ガス内のガス状態が定
常状態に達し、始動過程が完了する。この状態において
制御進み角βは小さく、良好なる力率でインバータは運
転される。以上のように、本発明による始動方法によれ
ば、燃料電池発電システムを始動するために必要な付加
的装置として小規模の不活性ガス源を用意するだけでよ
く、あるいはその不活性ガス源として他の使用目的で設
けられているものを流用するか、もしくは停止時の空気
供給しや断ないしは適当な負荷による予備運転による不
活性ガス雰囲気形成を行なわせることによつて取りたて
挙げるほどの付加的装置を必要としない。The inverter 2 is controlled by the current regulator 2 as shown in FIG.
Constant current control is based on 1, and a constant value 2 is set as the target value 1d*.
0A was set. The oxidant gas chamber of the fuel cell 1 was placed in a nitrogen atmosphere and a command was given to start the air supply and the inverter-controlled pulse supply at time t=o. At a time t1 delayed from this time, the fuel cell voltage E1 begins to rise. At this time, the output signal of the regulator 21 is the maximum control advance angle βMax(
(set to about 80 degrees).
As soon as the fuel cell voltage E1 exceeds the inverter DC reverse voltage E2 (time T2), the DC current 1d starts to rise.
Then, the DC current 1d increases as the fuel cell voltage E1 increases, and at time T3, the target value 1d*=
It reaches 20A. From this point on, the constant current control loop by the current regulator 21 works, and as the fuel cell voltage E1 increases, the control advance angle β, which had been stuck at the maximum control advance angle βMax, shifts toward the minimum control advance angle βi. Moving on. Time T4 - The gas condition in the CWilating agent gas reaches a steady state and the start-up process is completed. In this state, the control advance angle β is small and the inverter is operated with a good power factor. As described above, according to the starting method according to the present invention, it is only necessary to prepare a small-scale inert gas source as an additional device necessary to start the fuel cell power generation system, or as an inert gas source. A considerable additional amount can be added by reusing equipment already provided for other purposes, or by creating an inert gas atmosphere by supplying air during shutdown, cutting off the air supply, or pre-operating with an appropriate load. No equipment required.
第1図は燃料電池発電システムの原理的構成を示し、第
2図は本発明による方法より始動された場合における燃
料電池電圧と直流電流の時間経過例を示す。
1・・・・・・燃料電池、2・・・・・・インバータ、
3・・・・・・交流系統、21・・・・・・電流調節器
、E1・・・・・・燃料電池電圧、Id・・・・・・直
流電流。FIG. 1 shows the basic configuration of a fuel cell power generation system, and FIG. 2 shows an example of the time course of the fuel cell voltage and direct current when started by the method according to the present invention. 1...Fuel cell, 2...Inverter,
3...AC system, 21...Current regulator, E1...Fuel cell voltage, Id...DC current.
Claims (1)
供給する燃料電池発電システムにおいて、燃料電池内の
少なくとも一方のガス室を不活性ガス雰囲気にした状態
でそのガス室への反応ガスの供給を開始することにより
燃料電池電圧を徐々に立上がらせ、インバータへの制御
パルス供給開始は燃料電池電圧が制御パルス供給開始直
後に現われるインバータ直流逆電圧相当値を実質的に上
回る以前に行なうようにしたことを特徴とする燃料電池
発電システムの始動方法。1. In a fuel cell power generation system that supplies power from a fuel cell to an AC system via an inverter, supply of reactant gas to the gas chamber is started with at least one gas chamber in the fuel cell in an inert gas atmosphere. By doing so, the fuel cell voltage is gradually raised, and the control pulse supply to the inverter is started before the fuel cell voltage substantially exceeds the value equivalent to the inverter DC reverse voltage that appears immediately after the control pulse supply starts. A method for starting a fuel cell power generation system characterized by:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55014034A JPS5913152B2 (en) | 1980-02-07 | 1980-02-07 | How to start a fuel cell power generation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55014034A JPS5913152B2 (en) | 1980-02-07 | 1980-02-07 | How to start a fuel cell power generation system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56112073A JPS56112073A (en) | 1981-09-04 |
| JPS5913152B2 true JPS5913152B2 (en) | 1984-03-28 |
Family
ID=11849850
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55014034A Expired JPS5913152B2 (en) | 1980-02-07 | 1980-02-07 | How to start a fuel cell power generation system |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5913152B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58164163A (en) * | 1982-03-25 | 1983-09-29 | Kansai Electric Power Co Inc:The | Stop control method of fuel cell generator |
| JPH06101346B2 (en) * | 1989-06-20 | 1994-12-12 | 関西電力株式会社 | Operating method of fuel cell power generator |
-
1980
- 1980-02-07 JP JP55014034A patent/JPS5913152B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56112073A (en) | 1981-09-04 |
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