JPS59111272A - Fuel-cell control device - Google Patents

Fuel-cell control device

Info

Publication number
JPS59111272A
JPS59111272A JP57218322A JP21832282A JPS59111272A JP S59111272 A JPS59111272 A JP S59111272A JP 57218322 A JP57218322 A JP 57218322A JP 21832282 A JP21832282 A JP 21832282A JP S59111272 A JPS59111272 A JP S59111272A
Authority
JP
Japan
Prior art keywords
pressure
hydrogen
oxygen
fuel cell
valve
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.)
Pending
Application number
JP57218322A
Other languages
Japanese (ja)
Inventor
Susumu Tanaka
進 田中
Masayuki Narita
正幸 成田
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.)
Toshiba Corp
Original Assignee
Toshiba 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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP57218322A priority Critical patent/JPS59111272A/en
Publication of JPS59111272A publication Critical patent/JPS59111272A/en
Pending legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04694Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
    • H01M8/04746Pressure; Flow
    • H01M8/04753Pressure; Flow of fuel cell reactants
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04082Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04089Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
    • H01M8/04104Regulation of differential pressures
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04313Processes for controlling fuel cells or fuel cell systems characterised by the detection or assessment of variables; characterised by the detection or assessment of failure or abnormal function
    • H01M8/0438Pressure; Ambient pressure; Flow
    • H01M8/04388Pressure; Ambient pressure; Flow of anode reactants at the inlet or inside the fuel cell
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04313Processes for controlling fuel cells or fuel cell systems characterised by the detection or assessment of variables; characterised by the detection or assessment of failure or abnormal function
    • H01M8/0438Pressure; Ambient pressure; Flow
    • H01M8/04395Pressure; Ambient pressure; Flow of cathode reactants at the inlet or inside the fuel cell
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04313Processes for controlling fuel cells or fuel cell systems characterised by the detection or assessment of variables; characterised by the detection or assessment of failure or abnormal function
    • H01M8/0438Pressure; Ambient pressure; Flow
    • H01M8/04432Pressure differences, e.g. between anode and cathode
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04694Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
    • H01M8/04746Pressure; Flow
    • H01M8/04783Pressure differences, e.g. between anode and cathode
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04082Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04089Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
    • H01M8/04097Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with recycling of the reactants
    • 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

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)
  • Fuel Cell (AREA)

Abstract

PURPOSE:To provide a fuel-cell control device which can control flow rates at which oxygen and hydrogen are supplied to a fuel cell commensurately with the load of the fuel cell while controlling the fifferential pressure between the supplied oxygen and hydrogen without mixing them. CONSTITUTION:Pressure signals (PH) and (PO) obtained through pressure-detecting elements 16 and 17 installed in downstream from flow-rate controlling valves 6 and 7 are sent to a computer unit 18 where the pressures of the oxygen and the hydrogen sides are compared with each other to obtain a signal of high value preferred operation by which a pressure control valve 10 or 11 is driven. Owing to the operation of the valve 10 or 11, the fluid of higher pressure is exhausted downstream from an exhaust check valve 8 or 9, after bypassing the fuel cell body 5. In addition, even in a state of emergency when a pressure difference becomes over 0.7kg/cm<2> at the time of a sudden change in the supply pressure of oxygen or hydrogen or supply pressure of either oxygen or hydrogen becomes abnormally high, any breakage of an electrolyte chamber 1 can be prevented by driving either pressure-controlling valve 10 or 11 on higher pressure side.

Description

【発明の詳細な説明】 〔発明の技術分野〕 杢元明は、燃料磁北兄礒設備における、水素および空気
の供、目早の制御に関するものでお金。   ′〔発明
の技術旧背景〕 便来、発電設備は化石燃料、地熱、ウラン等のノく然資
源を用い、これらのエネルギを醸力に変換するために火
力発峨設備、地熱9t=電設備、原子力91 ’rJX
設備が盛んに利用されてい心ことは良く知られていると
ころであろうしかしながら、これらの設備はわが国の゛
屯力漸要の飛躍的増加によって超大形化の途を仙ってい
るため、その施設規模は超大化し、立地難にみまわれて
おり、また発電設備が超大形化ずれば、これに伴い温排
水、排ガス等の公害問題も多く発生し、きひしい環境下
にある他方、仮にこれらの設備に対して用地が確保され
たとしても、 地であるため、建設に要する動力源、水
力源が得られに<<、建設工期の長期化を招ねき、さら
に竜力需喪地に岨力な送る送電線設備の製作・貼付にも
多大の費用・労ノJを要する等積々の問題を呈している
[Detailed Description of the Invention] [Technical Field of the Invention] Motoaki Motoki is involved in the rapid control of hydrogen and air supply in fuel-magnetic equipment. [Technical background of the invention] Power generation equipment uses natural resources such as fossil fuels, geothermal heat, and uranium, and in order to convert these energies into brewing power, thermal power generation equipment, geothermal 9 tons = electric equipment , nuclear power 91'rJX
It is well known that these facilities are actively used, but these facilities are on the verge of becoming extremely large due to the dramatic increase in Japan's capacity requirements. As the scale of power generation equipment increases, it becomes difficult to find a suitable location, and if power generation equipment becomes extremely large, many pollution problems such as heated wastewater and exhaust gas will occur, creating a harsh environment. Even if land is secured for the equipment, the power source and water power required for construction cannot be obtained because the land is landlocked, resulting in a prolonged construction period and the need to build a land in a land with no demand for power. The production and installation of powerful power transmission line equipment also poses a number of problems, such as requiring a large amount of cost and labor.

ところで、近時、省エネルギ発<、、1@設規模の小形
化光重・無公害うむ竜の一つとして燃料゛電池発車設備
が脚光をあび日夜研究が車ねられている。
By the way, recently, fuel cell starting equipment has been in the spotlight as one of the energy-saving, light-duty, non-polluting, compact, light-duty, non-polluting devices, and research is being conducted day and night.

この燃料1池設備は周知のように、水素と酸素を反応さ
せ、その反応によって生成される電子エネルギーを取り
出すものである。
As is well known, this single fuel tank facility reacts hydrogen and oxygen and extracts the electronic energy generated by the reaction.

ここで第1図を使用して、燃料電池の発亀涼理について
詳述するっ符号5は燃料電池本体を示し、この燃料電池
本体5には4%液室1を挾んで両側に導岨性の尚いアノ
ード2.水素室2aが、またカソード3.混合室8aが
それぞれ1哄次閂じ設されテイル、水累至2 aに送ら
れた水g1(はアノード2において、112→2H+2
β の化字又応がなされ、この反応によって生成された
水素イオン■1は電解液室1を、出ってカソード3に送
られ、ここで(昆台室3aからの酸素0と化合し、水W
aが生成されるっ一方、アノード2で得られた電子e−
は外部4坏4を辿してカソード3に送られ、ここでユO
,+28− +2−g−−+H,Oc7) 4気化学反
応カナサれ、その結果、旦流也圧が得られるようになっ
ている。
Here, using FIG. 1, we will explain in detail how the fuel cell is developed. Reference numeral 5 indicates the fuel cell main body, and the fuel cell main body 5 has guide holes on both sides with a 4% liquid chamber 1 in between. Low quality anode 2. The hydrogen chamber 2a is also connected to the cathode 3. The mixing chambers 8a are each opened one after another, and the water g1 sent to the tail and water flow 2a (is 112→2H+2 at the anode 2).
The hydrogen ion 1 produced by this reaction leaves the electrolyte chamber 1 and is sent to the cathode 3, where it combines with oxygen 0 from the Kuntai chamber 3a, Water W
While a is generated, the electron e- obtained at the anode 2
is sent to the cathode 3 following the external 4
, +28- +2-g--+H, Oc7) A four-gas chemical reaction is carried out, and as a result, a pressure is obtained.

〔背景孜術の問題点〕[Problems with background art]

ところで、上記゛電解液室1はその構造、材質上水素室
2aおよび混付室3a間の差圧が0.7 kp77以上
になった場合破壊される恐れがあるため、水素および酸
素の燃料電池本体5への供給圧力を十分百理する盛装が
あろう 〔発明の目的J そこで、本発明は上記の事情に基づき、燃料゛電池へ供
給される水素および酸素の差圧を両者を混合させること
なくコントロールしつつそのbIL 亀もまた燃料電池
の負荷に見合った襞に調節できる1然料屯池の両++1
1装置を提供することを目的とするものであ金っ 〔発明の実施レリ〕 以F本発明の一実施例を第2図を参照して説明する。
By the way, due to its structure and material, the electrolyte chamber 1 may be destroyed if the differential pressure between the hydrogen chamber 2a and the mixing chamber 3a exceeds 0.7 kp77. Therefore, based on the above-mentioned circumstances, the present invention proposes to mix the pressure difference between hydrogen and oxygen supplied to the fuel cell. The turtle can also adjust the folds to match the load of the fuel cell while controlling it.
[Embodiment of the Invention] Hereinafter, an embodiment of the present invention will be described with reference to FIG. 2.

燃料ヒ1池本体5への水素および識素の供給系統に谷々
lAf、量動嫂弁6,7、水素室2aおよび混けM3a
の出口に各々排気逆止弁8,9、また水素室2a督よひ
混合室3aの入口から各室をバイパスする各々圧力調節
弁10.11を設置する。尚′電気回路は省略する。
The supply system for hydrogen and hydrogen to the fuel tank main body 5 includes Tani lAf, quantity valves 6 and 7, hydrogen chamber 2a, and mixture M3a.
Exhaust check valves 8 and 9 are installed at the outlets of the hydrogen chamber 2a, and pressure regulating valves 10 and 11 are installed to bypass each chamber from the inlet of the hydrogen chamber 2a and the mixing chamber 3a. Note that the electrical circuit is omitted.

各々の流量m;JIII4I弁6,7は、各流体の流量
検出器12,18から送られる流量1g号Ql(l Q
O%燃料電池の実出力1g号Wおよび出力設定信号W8
を受けて比較演算する演算器14.15よシの演算出力
信号によシ動作し、燃料電池の出力を設定出力に制御卸
すQo 各々の排気逆止弁8.9は各流体の供TIa圧力より排
気圧力が高い場合に排気が各室に、史流し、正常な化学
反応を妨げることを防止すりために設置し、排気圧力上
列により自動的に閉鎖する。
Each flow rate m;
O% fuel cell actual output 1g W and output setting signal W8
Qo, each exhaust check valve 8.9 operates according to the calculation output signal of the calculation unit 14.15 which receives and compares the output signal, and controls the output of the fuel cell to the set output. When the exhaust pressure is higher than the exhaust pressure, the exhaust gas is installed in each chamber to prevent it from flowing and hindering the normal chemical reaction, and the exhaust pressure is automatically closed by the upper row.

一方、流皇割41弁6,7の下流に設置された圧力検出
器16.17により検出された圧力1g号P□、Poは
、演算器18に送られ、ここで水素および酸素側の圧力
を比較演算し、冒値優先の演算出力信号により、圧力調
節弁10または11を動作させる。この動作により、圧
力の商い方の流体は、燃料+i4池本I4−5をバイパ
スして、1)l:ヌ()更止弁8捷たは9の下f危1u
llへ排気される。
On the other hand, the pressure 1g P are compared and calculated, and the pressure control valve 10 or 11 is operated based on the calculation output signal giving priority to the incorrect value. Due to this operation, the pressure fluid bypasses the fuel + i4 pond I4-5 and 1) l: nu () under the check valve 8 or 9.
ll is exhausted.

また非常状態に伜いて水素または、酸素の供給圧力突変
時差圧が0.7に〆d以−ヒになった喝せ、捷たは供給
圧力が異常高になった場打も、圧力の高い方の圧力調声
す弁10または11を動作びせ、電解液室1の破j表を
防止することができる。
In addition, during an emergency situation, when the supply pressure of hydrogen or oxygen suddenly changes, the differential pressure drops to 0.7 or more, or the supply pressure becomes abnormally high. By operating the higher pressure adjustment valve 10 or 11, it is possible to prevent the electrolyte chamber 1 from being ruptured.

〔発明の効果〕〔Effect of the invention〕

以上祝明したように本発明によれば、水素と酸素を混付
させることなく安全に両者の供給差圧を調整できるため
、゛電解液室を(員イ鳩することなく、かつ水素および
酸素を排気にバイパスさせることにより、水素はたとえ
ば燃料改質用に、酸素はたとえばターボコングレツサ鳴
動用に有効に411用することができ、しかも負荷要求
1g号に応じで燃料電池出力を1iilI御する装置が
提供できろう
As described above, according to the present invention, the supply differential pressure between hydrogen and oxygen can be adjusted safely without mixing hydrogen and oxygen. By bypassing the fuel to the exhaust gas, hydrogen can be effectively used for, for example, fuel reforming, and oxygen can be effectively used, for example, for turbo congressor sounding, and the fuel cell output can be controlled in response to load demands of 1g. equipment could be provided

【図面の簡単な説明】 第1図は燃料電池の発電原理を説明するための図、!1
F82図は本発明による水素、酸素両両装置の一実施例
を祝明するブロック図である 1・・・竜)弄液室   14 、15・・・演算器2
・・アノード   16.17・・・圧力検出器3・・
・カソード   18・・・濱n器5・・・燃料riジ
池本体 6.7・・・流量制御弁 8.9・・・排気逆屯弁 10.11・・・圧力A動弁 12.18・・・流量検出器 代理人 弁理士 則 近 憲 佑 (ほか1名)第1図 H 第2図
[Brief explanation of the drawings] Figure 1 is a diagram for explaining the power generation principle of a fuel cell. 1
Figure F82 is a block diagram showing an embodiment of the hydrogen and oxygen device according to the present invention.
...Anode 16.17...Pressure detector 3...
・Cathode 18...Fuel tank body 6.7...Flow rate control valve 8.9...Exhaust back pressure valve 10.11...Pressure A valve 12.18 ...Flow rate detector agent Patent attorney Kensuke Chika (and 1 other person) Figure 1 H Figure 2

Claims (1)

【特許請求の範囲】[Claims] ;然料電池光也設備において水素および酸素供胞系統に
各々実電池出力、磁北設定出力、各流体の流電の演算出
力で制御される流量制御弁、および水素、酸素の差圧演
其イぎ号で動作する圧力調節弁を設置し、この下流管を
燃料蔦池各排気管に設置された排気逆止弁下流に接続し
たことを:+′!f徴とする燃料電池補・電−股−義勇
−制御装置、
In the natural battery Mitsuya equipment, the hydrogen and oxygen supply systems each have flow control valves that are controlled by the actual battery output, magnetic north setting output, and calculation output of the current flow of each fluid, and the differential pressure calculation equipment for hydrogen and oxygen. We installed a pressure control valve that operates at the same time, and connected this downstream pipe to the downstream of the exhaust check valve installed in each exhaust pipe of the fuel tank: +'! Fuel cell auxiliary/electrical control device with f characteristics,
JP57218322A 1982-12-15 1982-12-15 Fuel-cell control device Pending JPS59111272A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57218322A JPS59111272A (en) 1982-12-15 1982-12-15 Fuel-cell control device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57218322A JPS59111272A (en) 1982-12-15 1982-12-15 Fuel-cell control device

Publications (1)

Publication Number Publication Date
JPS59111272A true JPS59111272A (en) 1984-06-27

Family

ID=16718027

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57218322A Pending JPS59111272A (en) 1982-12-15 1982-12-15 Fuel-cell control device

Country Status (1)

Country Link
JP (1) JPS59111272A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996020508A1 (en) * 1994-12-23 1996-07-04 Ballard Power Systems Inc. Electrochemical fuel cell system with a regulated vacuum ejector for recirculation of the fluid fuel stream
US6638652B1 (en) 1998-10-02 2003-10-28 Toyota Jidosha Kabushiki Kaisha Fuel cell control apparatus
JP2006147550A (en) * 2004-10-19 2006-06-08 Toshiba Fuel Cell Power Systems Corp Fuel cell system, and its stopping, retaining and starting method, and stopping, retaining and starting program
US7919211B2 (en) 2001-01-18 2011-04-05 Toyota Jidosha Kabushiki Kaisha On-board fuel cell system and method of controlling the same
JP2014209489A (en) * 2010-01-25 2014-11-06 ラモット アット テル−アヴィヴ ユニヴァーシテイ リミテッドRamot At Tel−Avivuniversity Ltd Energy storage and generation system

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996020508A1 (en) * 1994-12-23 1996-07-04 Ballard Power Systems Inc. Electrochemical fuel cell system with a regulated vacuum ejector for recirculation of the fluid fuel stream
AU699082B2 (en) * 1994-12-23 1998-11-19 Ballard Power Systems Inc. Electrochemical fuel cell system with a regulated vacuum ejector for recirculation of the fluid fuel stream
US6638652B1 (en) 1998-10-02 2003-10-28 Toyota Jidosha Kabushiki Kaisha Fuel cell control apparatus
US7919211B2 (en) 2001-01-18 2011-04-05 Toyota Jidosha Kabushiki Kaisha On-board fuel cell system and method of controlling the same
JP2006147550A (en) * 2004-10-19 2006-06-08 Toshiba Fuel Cell Power Systems Corp Fuel cell system, and its stopping, retaining and starting method, and stopping, retaining and starting program
JP2014209489A (en) * 2010-01-25 2014-11-06 ラモット アット テル−アヴィヴ ユニヴァーシテイ リミテッドRamot At Tel−Avivuniversity Ltd Energy storage and generation system
US9627693B2 (en) 2010-01-25 2017-04-18 Ramot At Tel-Aviv University Ltd. Energy storage and generation systems

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