Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH088111B2 - Fuel cell automatic start control method - Google Patents
[go: Go Back, main page]

JPH088111B2 - Fuel cell automatic start control method - Google Patents

Fuel cell automatic start control method

Info

Publication number
JPH088111B2
JPH088111B2 JP62312571A JP31257187A JPH088111B2 JP H088111 B2 JPH088111 B2 JP H088111B2 JP 62312571 A JP62312571 A JP 62312571A JP 31257187 A JP31257187 A JP 31257187A JP H088111 B2 JPH088111 B2 JP H088111B2
Authority
JP
Japan
Prior art keywords
fuel
oxidant
valve
fuel cell
chamber
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 - Lifetime
Application number
JP62312571A
Other languages
Japanese (ja)
Other versions
JPH01154469A (en
Inventor
義治 小林
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric Co Ltd
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 Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP62312571A priority Critical patent/JPH088111B2/en
Publication of JPH01154469A publication Critical patent/JPH01154469A/en
Publication of JPH088111B2 publication Critical patent/JPH088111B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • H01M8/04313Processes 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
    • H01M8/04664Failure or abnormal function
    • H01M8/04679Failure or abnormal function of fuel cell stacks
    • 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
    • H01M8/043Processes for controlling fuel cells or fuel cell systems applied during specific periods
    • H01M8/04302Processes for controlling fuel cells or fuel cell systems applied during specific periods applied during start-up
    • 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
    • H01M8/04223Auxiliary 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
    • H01M8/04225Auxiliary 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
    • 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
    • H01M8/04537Electric variables
    • H01M8/04544Voltage
    • H01M8/04559Voltage of fuel cell stacks
    • 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
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04694Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
    • H01M8/04955Shut-off or shut-down of fuel cells
    • 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)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明はりん酸型,アルカリ型などの燃料電池のう
ち自動起動制御装置を有する燃料電池の自動起動制御方
法、ことに燃料電池に発生した故障の早期発見を可能に
する制御方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial application] The present invention is directed to a method for automatically starting a fuel cell, such as a phosphoric acid type or alkaline type fuel cell, which has an automatic start control device. The present invention relates to a control method that enables early detection of a failure.

〔従来の技術〕[Conventional technology]

第4図に燃料電池の一般的な系統図を示す。1は電池
本体であって、燃料室2,酸化剤室3,電解液室4および電
解液室4と燃料室2,酸化剤室3にそれぞれ介在させられ
た燃料電極5および酸化剤電極6よりなる。7は燃料供
給源であって、燃料系供給弁10および圧力調整弁15を介
して燃料室2に連通される。前記燃料供給源7,燃料系供
給弁10,圧力調整弁15は全体として燃料系を構成する。
8は酸化剤供給源であって、酸化剤供給弁11,および圧
力調整弁16を介して酸化剤室3に連通される。前記酸化
剤供給源8,酸化剤供給弁11,圧力調整弁16は全体として
酸化剤系を構成する。9は置換用ガスとしての窒素供給
源であり、供給弁12,および圧力調整弁17を介して2方
向に分岐され、一端が逆止弁18を介して燃料系に連通さ
れ、他端が逆止弁19を介して酸化剤系に連通される。窒
素供給源9,供給弁12,圧力調整弁17,および逆止弁18,19
は全体として窒素系(一般には置換用ガス系)を構成す
る。13は燃料室側排出弁,14は酸化剤室側排出弁であ
る。なお、置換用ガスとしては窒素のほかにアルゴン,
ヘリウム等の不活性ガスを用いることもできるが、以下
の説明では窒素を用いた例について述べる。ここで、窒
素系の圧力調整弁17は燃料系,酸化剤系の圧力調整弁1
5,16に比して調整圧力をやや低め(差圧200mm水柱以
下)に設定してあり、このため窒素供給弁12が常時開い
た状態においても、燃料供給弁10,あるいは酸化剤供給
弁11が開けば、燃料系または酸化剤系の圧力が窒素系圧
力調整弁17の設定圧力より高めになるため窒素は流入さ
れず、逆に前記燃料供給弁10,あるいは酸化剤供給弁11
が閉じ,かつ燃料,酸化剤が系外に放出されて燃料系,
酸化剤系の圧力が窒素系圧力調整弁17の設定値以下にな
ったとき、窒素が流入する。逆止弁18,19の役割は、燃
料と酸化剤が混合されて電池本体へ流入しないためのも
のである。
FIG. 4 shows a general system diagram of the fuel cell. Reference numeral 1 denotes a battery main body, which includes a fuel chamber 2, an oxidant chamber 3, an electrolytic solution chamber 4, and a fuel electrode 5 and an oxidant electrode 6 which are interposed in the electrolytic solution chamber 4, the fuel chamber 2 and the oxidant chamber 3, respectively. Become. A fuel supply source 7 is connected to the fuel chamber 2 via a fuel system supply valve 10 and a pressure adjusting valve 15. The fuel supply source 7, the fuel system supply valve 10, and the pressure regulating valve 15 constitute a fuel system as a whole.
An oxidant supply source 8 is communicated with the oxidant chamber 3 via the oxidant supply valve 11 and the pressure adjusting valve 16. The oxidant supply source 8, the oxidant supply valve 11, and the pressure control valve 16 constitute an oxidant system as a whole. Reference numeral 9 denotes a nitrogen supply source as a replacement gas, which is branched in two directions through a supply valve 12 and a pressure adjusting valve 17, one end of which is connected to a fuel system through a check valve 18 and the other end of which is reverse. It communicates with the oxidant system via a stop valve 19. Nitrogen supply source 9, supply valve 12, pressure regulating valve 17, and check valves 18, 19
Constitutes a nitrogen system (generally a replacement gas system) as a whole. Reference numeral 13 is a fuel chamber side discharge valve, and 14 is an oxidant chamber side discharge valve. In addition to nitrogen as the replacement gas, argon,
Although an inert gas such as helium can be used, an example using nitrogen will be described below. Here, the nitrogen-based pressure control valve 17 is a fuel-based or oxidant-based pressure control valve 1
The adjustment pressure is set to a little lower than that of 5, 16 (differential pressure 200 mm water column or less). Therefore, even when the nitrogen supply valve 12 is always open, the fuel supply valve 10 or the oxidant supply valve 11 When the valve is opened, the pressure of the fuel system or the oxidant system becomes higher than the set pressure of the nitrogen system pressure adjusting valve 17, so that nitrogen does not flow in, and conversely, the fuel supply valve 10 or the oxidant supply valve 11
Is closed, and the fuel and oxidizer are released outside the system,
When the pressure of the oxidizer system becomes equal to or lower than the set value of the nitrogen system pressure adjusting valve 17, nitrogen flows in. The role of the check valves 18 and 19 is to prevent the fuel and the oxidant from being mixed and flowing into the cell body.

また、21はそれぞれの弁を起動シーケンスに基づいて
制御するシーケンス制御部、22はシーケンス制御部の起
動シーケンスに基づいて弁を開閉制御する駆動回路、23
は電池電圧の検出部であり、起動制御回路21,駆動回路2
2,および電圧検出部23は全体として自動起動制御装置を
構成する。第5図は自動起動制御装置の起動シーケンス
を示すタイムチャートであり、以下第4図および第5図
に基づいて燃料電池の起動動作を説明する。起動制御回
路21に時刻t0で起動信号が入力されると、第5図に示す
ように時刻t0で立上がる窒素(N2)系供給弁12の駆動電
圧12Eが出力され、逆止弁18,19を介して燃料室2および
酸化剤室3に窒素が供給され、両室の内圧が安定するに
要する幾分の時間をおいてt1時刻に排出弁駆動電圧13E,
14Eが出力されて燃料室排出弁13および酸化剤室排出弁1
4が開くことにより、燃料系および燃料室中の例えば空
気が窒素に置換され、あとで流入する燃料中の水素
(H2)と酸素との混触が回避される。なお酸化剤室の窒
素置換は必要に応じて行われる。燃料室および燃料系が
安全上問題のない程度に窒素ガスで置換されるに必要な
所定時間(t2‐t1時間)を経過した時刻t2で燃料系,酸
化剤系双方の供給弁駆動電圧10Eおよび11Eが出力される
と、窒素系の圧力が低いために逆止弁18,19は閉じ、燃
料室2,酸化剤室3にそれぞれ燃料(H2),酸化剤(O2
が流入して置換が行われ、これに伴なって燃料電池本体
1は起電圧Vを発生し、窒素からH2,O2への置換の進行
に対応して電池起電圧Vが上昇し、やがて規定の開回路
電圧VSに到達する。そこで、電池起電圧Vを検出部23で
検出し、この検出電圧をシーケンス制御部21で受け、検
出電圧Vが前記開回路電圧VSを超えた時点t3で排出弁駆
動電圧13Eおよび14Eの出力を停止するよう起動シーケン
スが組まれることにより燃料電池の発電運動が可能な状
態となる。
Further, 21 is a sequence control unit that controls each valve based on the activation sequence, 22 is a drive circuit that controls opening and closing of the valves based on the activation sequence of the sequence control unit, 23
Is a battery voltage detector, which includes a start control circuit 21 and a drive circuit 2.
2, and the voltage detection unit 23 collectively constitute an automatic start control device. FIG. 5 is a time chart showing the startup sequence of the automatic startup control device, and the startup operation of the fuel cell will be described below with reference to FIGS. 4 and 5. When a start signal is input to the start control circuit 21 at time t 0 , the drive voltage 12E of the nitrogen (N 2 ) system supply valve 12 rising at time t 0 is output as shown in FIG. 5, and the check valve is output. 18 and 19 the nitrogen is supplied to the fuel chamber 2 and the oxidizer chamber 3 via a discharge valve drive voltage 13E to t 1 time at a somewhat time required for the internal pressure of the two chambers is stabilized,
14E is output and the fuel chamber discharge valve 13 and the oxidant chamber discharge valve 1 are output.
By opening 4, the air in the fuel system and the fuel chamber, for example, is replaced by nitrogen, and the contact between hydrogen (H 2 ) and oxygen in the fuel that flows in later is avoided. The nitrogen replacement in the oxidant chamber is performed as needed. Fuel chamber and a predetermined time required for the fuel system is substituted with nitrogen gas to an extent no safety hazard (t 2 -t 1 hour) the fuel system at the time t 2 has elapsed, the oxidant system both supply valve driving When the voltages 10E and 11E are output, the check valves 18 and 19 are closed because the pressure of the nitrogen system is low, and the fuel (H 2 ) and the oxidant (O 2 ) are supplied to the fuel chamber 2 and the oxidant chamber 3, respectively.
Is introduced and replacement is carried out, and along with this, the fuel cell main body 1 generates an electromotive voltage V, and the cell electromotive voltage V rises in accordance with the progress of the replacement of nitrogen with H 2 , O 2 . Eventually, the specified open circuit voltage V S is reached. Therefore, the battery electromotive voltage V is detected by the detection unit 23, the detection voltage is received by the sequence control unit 21, and at the time point t 3 when the detection voltage V exceeds the open circuit voltage V S , the discharge valve drive voltages 13E and 14E are changed. The start-up sequence is set to stop the output, so that the fuel cell can perform the power generation movement.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

従来方法においては、燃料および酸化剤の供給を開始
する時刻t2から、燃料室および酸化剤室の窒素が性能上
問題のない程度に置換される時刻t3までの置換時間を、
電池電圧Vが規定の開回路電圧VSに到達したか否かによ
り判断するよう起動シーケンスが組まれていたために、
例えば燃料系,酸化剤系の一部に閉塞が生じて燃料また
は酸化剤の流量が減少するなど装置の異常が発生した場
合には、置換操作が延々と続き、t3時点での発電運転へ
の切換が著しく遅れる不都合が発生する。また、電池の
開回路電圧自体が窒素ガス混入状態でも高い電圧値を示
し、規定の開回路電圧との微少な電圧差により置換完了
か否かを判断することになり、置換完了時点t3の決定が
不正確になり易いという欠点がある。さらに、長期間使
用した燃料電池は徐々に出力電圧が低下することが考え
られるので、このような異常モードに対しては置換完了
時点t3の決定が困難になるケースの発生が予測される。
In the conventional method, fuel and from time t 2 to start the supply of the oxidizing agent, the nitrogen in the fuel chamber and oxidant chamber replacement time to time t 3 when substituted to a degree no problem in performance,
Since the start-up sequence is designed to judge whether the battery voltage V has reached the specified open circuit voltage V S ,
For example, if there is an abnormality in the device such as a blockage in the fuel system or oxidant system that reduces the flow rate of fuel or oxidant, the replacement operation continues endlessly, and power generation operation starts at time t 3 . However, there is a problem that the switching of is significantly delayed. Also, open circuit voltage itself of the battery shows a voltage value higher in nitrogen gas mixed state, might determine whether complete replacement by slight voltage difference between the open circuit voltage of the provisions, the replacement completion t 3 The drawback is that the decisions are likely to be inaccurate. Further, since it is considered that the output voltage of the fuel cell used for a long period of time gradually decreases, it may be difficult to determine the replacement completion time point t 3 for such an abnormal mode.

この発明の目的は、起動シーケンスに装置の異常を検
出する機能を持たせることにより、装置に異常のない場
合には起動から発電運転への移行が安定かつ迅速に行わ
れ、装置に異常がある場合には発電運転への移行を中断
してトラブルの発生を防止することにある。
An object of the present invention is to provide a function for detecting an abnormality of the device in the startup sequence, so that when there is no abnormality in the device, the transition from startup to power generation operation is performed stably and quickly, and the device has an abnormality. In some cases, the transition to power generation operation is interrupted to prevent the occurrence of trouble.

〔問題点を解決するための手段〕[Means for solving problems]

上記問題転を解決するために、この発明によれば、電
解液層を挟持する酸化剤電極および燃料電極と、その両
側に配された酸化剤室および燃料室とを有する単位電池
複数個の積層体からなる燃料電池本体と、それぞれ排出
弁を有する前記燃料室および酸化剤室それぞれに供給弁
および圧力調整器を介して燃料および酸化剤を供給する
燃料系および酸化剤系、ならびに両室に供給弁,圧力調
整器,および一対の逆止弁を介して置換ガスを供給する
置換ガス系と、前記各弁を起動シーケンスに基づいて制
御する自動起動制御装置と、前記燃料電池の起電圧検出
部とを具備した燃料電池の自動起動制御方法において、
燃料電池の起動信号に対応して置換ガス系の供給弁およ
び少くとも燃料室側排出弁を開いて、排出ガス中の酸素
濃度が十分に安全な低濃度に低下することを実験的に求
めてあらかじめ設定した所定時間ガス置換を行う第1の
ステップを実行し、ついで前記燃料系および酸化剤系の
供給弁および前記酸化剤室側排出弁を開いて,燃料電池
の開回路電圧が定常値となることを実験的に求めてあら
かじめ設定した所定時間燃料および酸化剤を供給し置換
した後排出弁を閉じる第2のステップを実行し、このス
テップの終了以降直ちに前記起電圧検出部の検出起電圧
を所定の基準電圧と比較して検出起電圧が前記基準電圧
以下であったとき燃料電池の異常と判断して報知信号を
発するとともに少くとも燃料系の供給弁を閉じる第3の
ステップを実施するよう前記起動シーケンスが組まれて
なることとする。
In order to solve the above problem, according to the present invention, a plurality of unit cells having an oxidant electrode and a fuel electrode sandwiching an electrolytic solution layer, and an oxidant chamber and a fuel chamber disposed on both sides of the electrode are stacked. A fuel cell body consisting of a body, a fuel system and an oxidant system for supplying fuel and an oxidant through a supply valve and a pressure regulator to the fuel chamber and the oxidant chamber, respectively, each having a discharge valve, and a supply to both chambers A replacement gas system that supplies replacement gas through a valve, a pressure regulator, and a pair of check valves, an automatic start control device that controls each of the valves based on a start sequence, and an electromotive voltage detection unit of the fuel cell. In an automatic start control method for a fuel cell comprising:
Experimentally sought to open the supply gas supply valve and at least the fuel chamber side discharge valve in response to the fuel cell start signal to lower the oxygen concentration in the exhaust gas to a sufficiently safe low concentration. The first step of performing gas replacement for a preset predetermined time is executed, and then the fuel system and oxidant system supply valves and the oxidant chamber side discharge valve are opened to set the open circuit voltage of the fuel cell to a steady value. The second step of closing the discharge valve after supplying and replacing the fuel and the oxidant for a predetermined time determined experimentally by performing the second step is performed, and immediately after the end of this step, the detected electromotive voltage of the electromotive voltage detector is detected. Is compared with a predetermined reference voltage, and when the detected electromotive voltage is less than or equal to the reference voltage, it is determined that the fuel cell is abnormal, a warning signal is issued, and at least the third valve for the fuel system is closed. The activation sequence is to be formed by braided as.

〔作用〕[Action]

上記手段において、燃料室を含む燃料系,酸化剤室を
含む酸化剤系の一方または両方を窒素置換する第1のス
テップと、両系それぞれを燃料ガス置換,酸化剤ガス置
換する第2のステップとにそれぞれ要する置換時間を正
常な状態の燃料電池装置について実験的にあらかじめ求
めた所定時間になるよう起動シーケンスが組まれるとと
もに、第2ステップの終了以降直ちに電池電圧が基準電
圧としての既定の開回路電圧に到達したか否かのチェッ
クを行う第3のステップを実行し、電池電圧が基準電圧
より低い場合には装置に異常が生じたものと判定して報
知信号を発するとともに、燃料ガスを遮断して起動を中
断するようにしたことにより、装置に異常がない場合に
はあらかじめ定まる所定時間で起動操作を終了して速や
かに発電運転を開始できるとともに、装置に異常が生じ
た場合には報知信号により異常が早期に検知され、かつ
圧力の高い窒素系から水素が消費されることにより圧力
の下がった燃料系および燃料室に逆止弁を介して窒素が
供給されるので、起動を中断することによって生ずる酸
化剤系との間の圧力差による電池電極の損傷や両ガスの
混触による危険性が回避される。
In the above means, a first step of substituting one or both of a fuel system including a fuel chamber and an oxidant system including an oxidant chamber with nitrogen, and a second step of substituting both of them with fuel gas and oxidant gas The start-up sequence is set so that the replacement time required for the fuel cell device and the replacement time for the fuel cell device in the normal state are set to the predetermined time experimentally obtained in advance. The third step of checking whether or not the circuit voltage is reached is executed, and when the battery voltage is lower than the reference voltage, it is determined that an abnormality has occurred in the device, a warning signal is issued, and fuel gas is emitted. By shutting off and interrupting the startup, if there is no abnormality in the device, the startup operation will be completed within a predetermined time and the power generation operation will start immediately. In addition, if an abnormality occurs in the device, an abnormality is detected early by a notification signal, and a check valve is installed in the fuel system and the fuel chamber where the pressure has dropped due to the consumption of hydrogen from the high pressure nitrogen system. Since nitrogen is supplied through, the risk of damage to the battery electrodes due to the pressure difference with the oxidant system caused by interrupting the start-up and the risk of contact with both gases is avoided.

〔実施例〕〔Example〕

以下この発明方法を実施例に基づいて説明する。 The method of the present invention will be described below based on examples.

第1図はこの発明方法を説明するための装置を示す制
御および配管系統図、第2図は装置に異常がない場合の
起動シーケンス図、第3図は装置に異常が生じた場合の
起動シーケンス図であり、いずれの場合も従来装置,従
来方法と同じ部分には同一参照符号を付すことにより詳
細な説明を省略する。第1図において、電池の起電圧検
出部23で検出された起電圧23Eはシーケンス制御部31の
出力信号31Eにより電圧比較のタイミングが制御される
判断回路34に入力されて基準電圧VSと比較される。すな
わち、第2図に示すパルスシーケンス図において、起動
信号に基づいて時刻t0で立ち上がるN2供給弁駆動電圧12
Eにより置換ガスとしての窒素が供給され、燃料室,酸
化剤室の圧力上昇した時刻t1で排出弁駆動電圧13E,14E
によって排出弁13および14が開き、燃料室2および酸化
剤室の空気を窒素に置換する第1のステップが実行され
るが、このステップの置換時間t2‐t0の決定は排出弁13
および14から放出される排出ガス中の酸素濃度などを測
定する実験により酸素濃度が十分に安全な低濃度に低下
する時間を求めることにより、あらかじめ定まる所定時
間に決められる。つぎに、時刻t2で燃料系および酸化剤
系の供給弁10および11を開き、窒素を燃料ガスおよび酸
化剤ガスに置換し、時刻t3で排出弁13および14を閉じ
て、燃料電池を発電運転可能状態とする第2のステップ
における置換時間t3‐t2の決定も電池起電圧の経時変化
を測定する実験によってあらかじめ定まる所定時間に設
定され、このようにして決められた時刻t3において排出
弁駆動電圧13E,14Eの出力が停止することによって排出
弁13,14が閉じ、燃料電池本体1は発電運転の待機状態
となる。ここでシーケンス制御部31から判断回路34での
電圧チェックを指令する信号31E(図示せず)が出力さ
れ、第2図の場合VS<Vなる条件が成立しているので判
断回路34からは異常信号34Eは出力されず、駆動回路32
から報知器35に向けて出力される報知信号35Eも零とな
り、燃料電池装置の異常の有無をその起電圧によってチ
ェックする第3のステップを含めた起動シーケンスが完
了する。
FIG. 1 is a control and piping system diagram showing an apparatus for explaining the method of the present invention, FIG. 2 is a start sequence diagram when there is no abnormality in the apparatus, and FIG. 3 is a start sequence when there is an abnormality in the apparatus. In each case, the same parts as those of the conventional apparatus and the conventional method are denoted by the same reference numerals, and detailed description thereof will be omitted. In FIG. 1, the electromotive voltage 23E detected by the electromotive voltage detection unit 23 of the battery is input to the determination circuit 34 whose voltage comparison timing is controlled by the output signal 31E of the sequence control unit 31 and compared with the reference voltage V S. To be done. That is, in the pulse sequence diagram shown in FIG. 2, the N 2 supply valve drive voltage 12 that rises at time t 0 based on the start signal
Nitrogen as a replacement gas is supplied by E, and at the time t 1 when the pressure in the fuel chamber and the oxidant chamber rises, the exhaust valve drive voltage 13E, 14E
Causes the exhaust valves 13 and 14 to open and the first step of replacing the air in the fuel chamber 2 and the oxidant chamber with nitrogen is carried out, the determination of the replacement time t 2 -t 0 in this step being determined by the exhaust valve 13
By determining the time for the oxygen concentration to drop to a sufficiently safe low concentration by an experiment to measure the oxygen concentration in the exhaust gas emitted from and 14, the predetermined time can be determined. Next, at time t 2 , the fuel system and oxidant system supply valves 10 and 11 are opened, nitrogen is replaced by the fuel gas and the oxidant gas, and at time t 3 , the discharge valves 13 and 14 are closed, and the fuel cell is closed. The replacement time t 3 -t 2 in the second step for making the power generation operation possible is also set to a predetermined time that is determined in advance by an experiment for measuring the change with time of the battery electromotive voltage, and the time t 3 thus determined is determined. When the output of the discharge valve drive voltages 13E and 14E is stopped at, the discharge valves 13 and 14 are closed and the fuel cell main body 1 is in the standby state for the power generation operation. Here voltage check (not shown) signal 31E to the command at decision circuit 34 from the sequence control unit 31 is output from the decision circuit 34 so if the second view V S <V following condition is satisfied The abnormal signal 34E is not output, and the drive circuit 32
The notification signal 35E output from the device to the alarm device 35 also becomes zero, and the start-up sequence including the third step of checking the presence / absence of abnormality in the fuel cell device by its electromotive voltage is completed.

燃料電池装置に異常があった場合には、第3図にその
状態を示すように、電池起電圧Vが基準電圧VSに達しな
いので、異常検出を行う第3のステップにおいてこれを
検知した判断回路34がt3時点またはそれ以後に立上がる
異常信号34Eを出力し、これを受けたシーケンス制御部3
1が燃料系供給弁駆動電圧10Eの停止と、異常報知信号35
Eの出力を駆動回路32に指令するので、駆動電圧10Eはt3
時点で零となり、供給弁10が閉じて燃料室2への燃料の
供給が遮断されるとともに、報知器35が異常の発生を報
知する。また、燃料の供給が遮断されたt3時点以後にお
いては燃料系および燃料室が包蔵する燃料ガス中の含有
水素が消費されるにしたがい電池起電圧およびガス圧が
徐々に低下し、燃料室2のガス圧低下を逆止弁18が感知
して窒素系から燃料系に向けて窒素が供給されるので、
燃料系および燃料室中の滞留ガスは不活性化されて安全
性が保持され、かつ燃料室2と酸化剤室3との間の差圧
が窒素系に対する圧力差(通常200mm水柱以下)に抑え
られ、電極5,6に損傷を与えたり、電解液が燃料室側に
吹き出すなどのトラブルが回避される。したがって異常
の発生原因の調査および修復を早期かつ安全に行うこと
が可能になる。なお、第2ステップ以降直ちにとは、起
動シーケンスの完了遅延が実用上大幅に遅れない範囲内
の速やかな時間を意味し、時間は短い程望ましく、t3
点と同時も含まれる。また、第2のステップにおける置
換時間(t3‐t2)の決定にあたっては、起動前の電池温
度の影響を受けるので、この点を考慮して複数段階の置
換時間を選択できるようにしておくことが好ましい。
When the fuel cell device has an abnormality, the cell electromotive voltage V does not reach the reference voltage V S , as shown in FIG. 3, and this is detected in the third step of abnormality detection. The decision circuit 34 outputs an abnormal signal 34E that rises at time t 3 or later, and the sequence control unit 3 which receives this outputs the abnormal signal 34E.
1 is the stop of the fuel system supply valve drive voltage 10E, and the abnormality notification signal 35
Since the output of E is commanded to the drive circuit 32, the drive voltage 10E is t 3
At the time point, it becomes zero, the supply valve 10 is closed, the supply of fuel to the fuel chamber 2 is cut off, and the alarm 35 notifies the occurrence of abnormality. Further, after the time point t 3 when the fuel supply is cut off, the cell electromotive voltage and the gas pressure gradually decrease as the hydrogen contained in the fuel gas contained in the fuel system and the fuel chamber is consumed, and the fuel chamber 2 Since the check valve 18 senses the decrease in the gas pressure of, nitrogen is supplied from the nitrogen system to the fuel system,
The retained gas in the fuel system and the fuel chamber is deactivated to maintain safety, and the pressure difference between the fuel chamber 2 and the oxidant chamber 3 is suppressed to the pressure difference with the nitrogen system (usually 200 mm water column or less). As a result, troubles such as damage to the electrodes 5 and 6 and ejection of the electrolytic solution toward the fuel chamber can be avoided. Therefore, it becomes possible to investigate and repair the cause of the abnormality early and safely. Immediately after the second step means a prompt time within a range in which the completion delay of the startup sequence is not significantly delayed in practice, the shorter the time is, the more preferable, and the time at the time t 3 is also included. Also, in determining the replacement time (t 3 −t 2 ) in the second step, it is affected by the battery temperature before startup, so it is possible to select multiple steps of replacement time in consideration of this point. It is preferable.

〔発明の効果〕〔The invention's effect〕

この発明方法は前述のように、自動起動制御装置を有
する燃料電池装置を起動するにあたり、少くとも燃料室
を含む燃料系の空気を不活性ガスに置換する第1のステ
ップと、この不活性ガスおよび酸化剤室を含む酸化剤系
の空気を燃料ガスおよび酸化剤に置換する第2のステッ
プとの置換時間をあらかじめ定まる所定時間に設定され
た起動シーケンスに基づいて実行して発電運転の待機状
態とし、ついで起電圧検出部の検出電圧が基準電圧より
低いとき燃料電池に異常が生じたものと判定して少くと
も燃料の供給を停止し、報知信号を発する第3のステッ
プを実行するよう構成した。その結果、第3のステップ
が燃料電池の異常の早期検出手段として機能し、燃料系
および酸化剤系の閉塞によるガス不足,燃料電池の老化
など起電圧低下要因が報知信号によって早期に検知さ
れ、かつ燃料供給の停止により安全性が保持されるで、
電池起電圧のレベルによって起動シーケンスの完了を決
める従来技術で問題となった装置の故障によって起動シ
ーケンスの完了が延々と伸びてしまうという欠点が排除
され、起動シーケンスの組み方の改良により大がかりな
故障監視装置を必要とせずに故障の早期発見,自動監視
機能を有する燃料電池の自動起動制御装置を提供するこ
とができる。
As described above, the method of the present invention, when starting the fuel cell device having the automatic start control device, replaces the air of the fuel system including at least the fuel chamber with the inert gas, and the inert gas. And a standby state for the power generation operation by executing the replacement time with the second step of replacing the air of the oxidant system including the oxidant chamber with the fuel gas and the oxidant based on the startup sequence set to a predetermined time set in advance. Then, when the detection voltage of the electromotive voltage detection unit is lower than the reference voltage, it is determined that an abnormality has occurred in the fuel cell, at least the supply of fuel is stopped, and the third step of issuing a notification signal is executed. did. As a result, the third step functions as a means for early detection of an abnormality in the fuel cell, and an alarm voltage causes early detection of factors such as gas shortage due to blockage of the fuel system and oxidant system and aging of the fuel cell. And because safety is maintained by stopping the fuel supply,
Determining the completion of the startup sequence based on the level of the battery electromotive voltage.The drawback of the conventional technology, which is a problem with the device, in which the completion of the startup sequence is lengthened, is eliminated. It is possible to provide an automatic start-up control device for a fuel cell which has an early detection of a failure and an automatic monitoring function without requiring a device.

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

第1図はこの発明の実施例方法を説明するための制御回
路を含む配管系統図、第2図および第3図は実施例方法
を示す起動シーケンス図、第4図は従来装置を示す配管
系統図、第5図は従来装置における起動シーケンス図で
ある。 1……燃料電池本体、2……燃料室、3……酸化剤室、
(7,10,15,2)……燃料系、(8,11,16,3)……酸化剤
系、(9,12,17,18,19)……置換ガス系、10,11,12……
供給弁、13,14……排出弁、23……起電圧検出部、21,31
……シーケンス制御部、22,32……駆動回路、35……報
知器、V……起電圧、VS……基準電圧、10E,11E,12E,13
E,14E……駆動電圧、35E……異常報知信号。
FIG. 1 is a piping system diagram including a control circuit for explaining an embodiment method of the present invention, FIGS. 2 and 3 are start-up sequence diagrams showing the embodiment method, and FIG. 4 is a piping system showing a conventional apparatus. 5 and 5 are start-up sequence diagrams in the conventional device. 1 ... Fuel cell main body, 2 ... Fuel chamber, 3 ... Oxidant chamber,
(7,10,15,2) …… Fuel system, (8,11,16,3) …… Oxidizer system, (9,12,17,18,19) …… Substitution gas system, 10,11, 12 ……
Supply valve, 13,14 …… Discharge valve, 23 …… Electromotive voltage detector, 21,31
...... Sequence control unit, 22,32 ...... Drive circuit, 35 …… Annotator, V …… Electromotive voltage, V S …… Reference voltage, 10E, 11E, 12E, 13
E, 14E: Drive voltage, 35E: Abnormality notification signal.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】電解液層を挟持する酸化剤電極および燃料
電極と、その両側に配された酸化剤室および燃料室とを
有する単位電池複数個の積層体からなる燃料電池本体
と、それぞれ排出弁を有する前記燃料室および酸化剤室
それぞれに供給弁および圧力調整器を介して燃料および
酸化剤を供給する燃料系および酸化剤系、ならびに両室
に供給弁,圧力調整器,および一対の逆止弁を介して置
換ガスを供給する置換ガス系と、前記各弁を起動シーケ
ンスに基づいて制御する自動起動制御装置と、前記燃料
電池の起電圧検出部とを具備した燃料電池の自動起動制
御方法において、燃料電池の起動信号に対応して置換ガ
ス系の供給弁および少くとも燃料室側排出弁を開いて,
排出ガス中の酸素濃度が十分に安全な低濃度に低下する
ことを実験的に求めてあらかじめ設定した所定時間ガス
置換を行う第1のステップを実行し、ついで前記燃料系
および酸化剤系の供給弁および前記酸化剤室側排出弁を
開いて,燃料電池の開回路電圧が定常値となることを実
験的に求めてあらかじめ設定した所定時間燃料および酸
化剤を供給し置換した後排出弁を閉じる第2のステップ
を実行し、このステップの終了以降直ちに前記起電圧検
出部の検出起電圧を所定の基準電圧と比較して検出起電
圧が前記基準電圧以下であったとき燃料電池の異常と判
断して報知信号を発するとともに少くとも燃料系の供給
弁を閉じる第3のステップを実施するよう前記起動シー
ケンスが組まれてなることを特徴とする燃料電池の自動
起動制御方法。
1. A fuel cell main body comprising a stack of a plurality of unit cells each having an oxidant electrode and a fuel electrode sandwiching an electrolyte solution layer, and an oxidant chamber and a fuel chamber disposed on both sides of the electrode, respectively. A fuel system and an oxidant system for supplying fuel and an oxidant to the fuel chamber and the oxidant chamber, respectively, each having a valve via a supply valve and a pressure regulator, and a supply valve, a pressure regulator, and a pair of reverse valves for both chambers. A replacement gas system for supplying a replacement gas through a stop valve, an automatic startup control device for controlling each valve based on a startup sequence, and an automatic startup control for a fuel cell, which includes an electromotive voltage detection unit for the fuel cell. In the method, opening a supply gas supply valve and at least a fuel chamber side discharge valve in response to a fuel cell start signal,
The first step of carrying out gas replacement for a predetermined time set in advance by experimentally obtaining that the oxygen concentration in the exhaust gas is lowered to a safe low concentration is executed, and then the supply of the fuel system and the oxidant system is performed. Valve and the oxidant chamber side discharge valve are opened to experimentally determine that the open circuit voltage of the fuel cell becomes a steady value, and after the fuel and the oxidizer have been supplied and replaced for a predetermined time, the discharge valve is closed. The second step is executed, and immediately after the end of this step, the detected electromotive voltage of the electromotive voltage detection unit is compared with a predetermined reference voltage, and when the detected electromotive voltage is less than or equal to the reference voltage, it is determined that the fuel cell is abnormal. The automatic start control method for the fuel cell is characterized in that the start sequence is assembled so as to perform the third step of closing the supply valve of the fuel system at least while issuing the notification signal.
JP62312571A 1987-12-10 1987-12-10 Fuel cell automatic start control method Expired - Lifetime JPH088111B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62312571A JPH088111B2 (en) 1987-12-10 1987-12-10 Fuel cell automatic start control method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62312571A JPH088111B2 (en) 1987-12-10 1987-12-10 Fuel cell automatic start control method

Publications (2)

Publication Number Publication Date
JPH01154469A JPH01154469A (en) 1989-06-16
JPH088111B2 true JPH088111B2 (en) 1996-01-29

Family

ID=18030819

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62312571A Expired - Lifetime JPH088111B2 (en) 1987-12-10 1987-12-10 Fuel cell automatic start control method

Country Status (1)

Country Link
JP (1) JPH088111B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009031444A1 (en) * 2007-09-03 2009-03-12 Toyota Jidosha Kabushiki Kaisha Fuel cell operation method
WO2009057534A1 (en) * 2007-10-30 2009-05-07 Toyota Jidosha Kabushiki Kaisha Fuel cell system and fuel cell system start control method

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4372235B2 (en) * 1996-08-29 2009-11-25 トヨタ自動車株式会社 Fuel cell system and electric vehicle
JP4892779B2 (en) * 2000-12-27 2012-03-07 トヨタ自動車株式会社 Start-up control device for fuel cell system
US6979503B2 (en) * 2003-04-04 2005-12-27 Texaco Inc. Method and apparatus for burst disk identification
JP2005044687A (en) * 2003-07-24 2005-02-17 Matsushita Electric Ind Co Ltd Control device for fuel cell system
JP2007018992A (en) * 2005-06-07 2007-01-25 Ricoh Co Ltd Fuel cell system and fuel cell system operation control method
EP1843422B1 (en) * 2006-04-06 2010-11-17 STMicroelectronics Srl Method and circuit for managing a start-up phase of at least a micro fuel cell to be connected to a load
JP4924910B2 (en) * 2010-02-26 2012-04-25 Toto株式会社 Fuel cell device
JP7499001B2 (en) * 2020-12-03 2024-06-13 ヤンマーホールディングス株式会社 Fuel Cell Ship

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5822864B2 (en) * 1973-09-29 1983-05-11 松下電器産業株式会社 Nenryodenchi Seigiyosouchi
JPS55154075A (en) * 1979-05-21 1980-12-01 Hitachi Ltd Automatic starting method for fuel battery
JPS58164167A (en) * 1982-03-25 1983-09-29 Kansai Electric Power Co Inc:The Stopping method of fuel cell power generating system during starting process
JPS6054176A (en) * 1983-09-01 1985-03-28 Fuji Electric Corp Res & Dev Ltd Safety protection of stacked fuel cell

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009031444A1 (en) * 2007-09-03 2009-03-12 Toyota Jidosha Kabushiki Kaisha Fuel cell operation method
JP2009059669A (en) * 2007-09-03 2009-03-19 Aisin Seiki Co Ltd Operation method of fuel cell
WO2009057534A1 (en) * 2007-10-30 2009-05-07 Toyota Jidosha Kabushiki Kaisha Fuel cell system and fuel cell system start control method
JP2009110806A (en) * 2007-10-30 2009-05-21 Toyota Motor Corp FUEL CELL SYSTEM AND FUEL CELL SYSTEM START-UP CONTROL METHOD

Also Published As

Publication number Publication date
JPH01154469A (en) 1989-06-16

Similar Documents

Publication Publication Date Title
JP4806989B2 (en) Fuel cell system
US7833670B2 (en) Fuel cell system and method of shutting down the same
US7581431B2 (en) Gas leak detection device and method for same
JP4852917B2 (en) Fuel cell system
JP4617675B2 (en) Fuel cell system
KR102614135B1 (en) Air supply control method and control system for fuel cell
JP2015097218A (en) How to stop operation of fuel cell stack
JPH088111B2 (en) Fuel cell automatic start control method
KR101886522B1 (en) Control device and method for starting of fuel cell system
JP2007035446A (en) Fuel cell system and gas leak detection device
JP7119716B2 (en) fuel cell system
JP2002313403A (en) Method of discharging generated water from fuel cell system
CN110534770B (en) Fuel cell system
US10978724B2 (en) Method and system for removing residual water in fuel cell stack
JP3879429B2 (en) Fuel cell system
JP2004179114A (en) Function maintenance method of fuel cell system
JP2003331889A (en) Fuel cell system
JP2006134647A (en) Fuel cell system
JP2005325950A (en) Gas supply device
JP2005197211A (en) Fuel cell system
JP2007109529A (en) Control method of fuel cell power generation system
JP4211000B2 (en) Gas leak judgment device
JP5418872B2 (en) Fuel cell system
JPS61116764A (en) Fuel cell system
JP2025133327A (en) fuel cell system