JPH0690930B2 - Start / stop control method for fuel cell power generation equipment - Google Patents

Start / stop control method for fuel cell power generation equipment

Info

Publication number
JPH0690930B2
JPH0690930B2 JP62145499A JP14549987A JPH0690930B2 JP H0690930 B2 JPH0690930 B2 JP H0690930B2 JP 62145499 A JP62145499 A JP 62145499A JP 14549987 A JP14549987 A JP 14549987A JP H0690930 B2 JPH0690930 B2 JP H0690930B2
Authority
JP
Japan
Prior art keywords
fuel gas
fuel
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
JP62145499A
Other languages
Japanese (ja)
Other versions
JPS63308876A (en
Inventor
敦智 大山
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 JP62145499A priority Critical patent/JPH0690930B2/en
Publication of JPS63308876A publication Critical patent/JPS63308876A/en
Publication of JPH0690930B2 publication Critical patent/JPH0690930B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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
    • H01M8/06Combination of fuel cells with means for production of reactants or for treatment of residues
    • H01M8/0606Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
    • H01M8/0612Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
    • 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
    • H01M8/04223Auxiliary 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
    • H01M8/04228Auxiliary 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 shut-down
    • 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
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/043Processes for controlling fuel cells or fuel cell systems applied during specific periods
    • H01M8/04303Processes for controlling fuel cells or fuel cell systems applied during specific periods applied during shut-down
    • 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、燃料電池と燃料改質器とを組合せた燃料電
池発電設備の起動,停止制御方法,特に起動,停止に対
応したガス切換え制御方法に関する。
Description: TECHNICAL FIELD The present invention relates to a start / stop control method for a fuel cell power generation facility in which a fuel cell and a fuel reformer are combined, and in particular, gas switching control corresponding to start / stop. Regarding the method.

〔従来の技術〕[Conventional technology]

まず第3図に頭記した燃料電池発電設備の系統図を示
す。図において、1は燃料電池、2は燃料改質器であ
り、前記燃料電池1は燃料電極1a,酸化剤電極1b,電解質
層1c,燃料ガス室1d,酸化剤室1eから成り、また燃料改質
器2は改質原料の気化器2a,改質反応器2bを内蔵した燃
焼炉2cにバーナ2dを装備して構成されている。ここで燃
料改質器2の気化器2aの入口にはポンプ3を介して改質
原料タンク4が配管接続され、バーナ2dには助燃料タン
ク5,空気ブロア6とともに燃料電池1の燃料ガス室1dの
出口側から引出した燃料ガス出口管7が配管接続されて
いる。なお8は燃焼炉2cの排気管である。また燃料電池
1の燃料ガス室1dに対し、その入口側には前記燃料改質
器2の改質反応器2bより引出した燃料ガス入口管9,およ
び不活性ガス源に通じる不活性ガス供給管10が接続され
ており、さらに前記の燃料ガス入口管9,出口管7,不活性
ガス供給管10,および燃料電池1をバイパスして燃料ガ
ス入口管9と出口管7との間を結ぶバイパス管11にはそ
れぞれ燃料ガス入口弁12,出口弁13,不活性ガス供給弁1
4,およびバイパス弁15が介装されている。なお16は燃料
電池1の酸化剤室1eに反応空気を送気するブロアであ
る。
First, a system diagram of the fuel cell power generation facility shown in Fig. 3 is shown. In the figure, 1 is a fuel cell, 2 is a fuel reformer, and the fuel cell 1 comprises a fuel electrode 1a, an oxidant electrode 1b, an electrolyte layer 1c, a fuel gas chamber 1d, and an oxidant chamber 1e. The quality device 2 is configured by equipping a burner 2d in a combustion furnace 2c containing a vaporizer 2a of a reforming raw material and a reforming reactor 2b. Here, a reforming raw material tank 4 is connected to the inlet of the carburetor 2a of the fuel reformer 2 via a pump 3, and a burner 2d, together with an auxiliary fuel tank 5 and an air blower 6, are connected to the fuel gas chamber of the fuel cell 1. A fuel gas outlet pipe 7 drawn from the outlet side of 1d is connected to the pipe. Reference numeral 8 is an exhaust pipe of the combustion furnace 2c. Further, with respect to the fuel gas chamber 1d of the fuel cell 1, a fuel gas inlet pipe 9 drawn out from the reforming reactor 2b of the fuel reformer 2 and an inert gas supply pipe leading to an inert gas source are provided on the inlet side thereof. A bypass connecting the fuel gas inlet pipe 9, the outlet pipe 7, the inert gas supply pipe 10, and the fuel cell 1 and connecting the fuel gas inlet pipe 9 and the outlet pipe 7 to each other. The pipe 11 has a fuel gas inlet valve 12, an outlet valve 13 and an inert gas supply valve 1 respectively.
4, and a bypass valve 15 are provided. Reference numeral 16 is a blower for supplying reaction air to the oxidant chamber 1e of the fuel cell 1.

かかる燃料電池発電設備において、まず燃料電池の起動
準備時には燃料改質器2に対しそのバーナ2dに助燃料,
燃焼空気を供給して燃焼し、この状態で気化器2aに改質
原料を供給する。これにより改質原料は気化器2aで気化
された後に改質反応器2bに入り、ここで改質触媒との接
触反応により水素リッチな燃料ガスに改質される。また
改質された燃料ガスはバイパス管11,開放状態にあるバ
イパス弁15を通じてバーナ2dに供給され、ここでの燃焼
により改質反応に必要な熱量を与えるようになる。一
方、この時点では燃料電池1の燃料ガス室1d内は不活性
ガスが充填されており、かつ燃料ガス入口弁12,出口弁1
3は閉じている。
In such a fuel cell power generation facility, at the time of preparation for starting the fuel cell, the burner 2d of the fuel reformer 2 is supplemented with auxiliary fuel
Combustion air is supplied and burned, and in this state, the reforming raw material is supplied to the vaporizer 2a. As a result, the reforming raw material is vaporized by the vaporizer 2a and then enters the reforming reactor 2b, where it is reformed into a hydrogen-rich fuel gas by a catalytic reaction with the reforming catalyst. Further, the reformed fuel gas is supplied to the burner 2d through the bypass pipe 11 and the bypass valve 15 which is in an open state, and the amount of heat required for the reforming reaction is given by the combustion here. On the other hand, at this time, the fuel gas chamber 1d of the fuel cell 1 is filled with an inert gas, and the fuel gas inlet valve 12 and the outlet valve 1
3 is closed.

次に起動準備の確立した前記状態から燃料電池1を起動
するには、燃料ガス室1dに対する燃料ガス入口弁12,出
口弁13を開き、バイパス弁15を閉じるとともに、酸化剤
室1eに接続した空気ブロア16により反応空気の供給を開
始する。これにより燃料改質器2で改質生成された燃料
ガスは入口弁12を通じて燃料電池の燃料ガス室1dに導入
され、ここでいままで燃料ガス室に封じ込められていた
不活性ガスを追い出してガス置換するとともに、燃料電
池1は起電反応により発電を開始する。また燃料ガス室
1dに供給された燃料ガスのうち起電反応に関与しない余
剰分はオフガスとして燃料ガス室1dより出口弁13を通じ
て燃料改質器2のバーナ2dに供給され、燃焼により改質
反応に必要な熱量を与える。
Next, in order to start the fuel cell 1 from the state where the preparation for starting is established, the fuel gas inlet valve 12 and the outlet valve 13 for the fuel gas chamber 1d are opened, the bypass valve 15 is closed, and the fuel gas chamber 1d is connected to the oxidant chamber 1e. The supply of reaction air is started by the air blower 16. As a result, the fuel gas reformed and produced in the fuel reformer 2 is introduced into the fuel gas chamber 1d of the fuel cell through the inlet valve 12, where the inert gas that has been contained in the fuel gas chamber is expelled. At the same time as the replacement, the fuel cell 1 starts power generation by an electromotive reaction. Also fuel gas chamber
The surplus of the fuel gas supplied to 1d that is not involved in the electromotive reaction is supplied as off-gas from the fuel gas chamber 1d through the outlet valve 13 to the burner 2d of the fuel reformer 2 and the amount of heat required for the reforming reaction by combustion. give.

一方、燃料電池を発電運転状態から停止する場合には、
燃料ガス入口弁12を閉じ,かつバイパス弁15を開いて燃
料電池への燃料ガス供給を停止するとともに、この過程
で不活性ガス供給弁14を開放して燃料ガス室内に不活性
ガスを供給して室内を燃料ガスから不活性ガスにガス置
換する。しかる後に燃料ガス出口弁13を閉じて燃料ガス
室1d内に不活性ガスを封じ込める。
On the other hand, when stopping the fuel cell from the power generation operating state,
The fuel gas inlet valve 12 is closed and the bypass valve 15 is opened to stop the fuel gas supply to the fuel cell, and in the process, the inert gas supply valve 14 is opened to supply the inert gas into the fuel gas chamber. The interior of the room is gas-replaced from the fuel gas with the inert gas. After that, the fuel gas outlet valve 13 is closed to contain the inert gas in the fuel gas chamber 1d.

ここで上記した燃料電池の起動,停止時における従来の
制御方法によるガス切換え制御のタイムチャートを示す
と第2図のごとくであり、起動,停止時には燃料ガス入
口弁12,出口弁13,およびバイパス弁15を同じタイミング
で同時に切換え操作する(但し、出口弁13の停止時の操
作は除く)ようにしていた。
A time chart of the gas switching control by the conventional control method at the time of starting and stopping the fuel cell described above is shown in FIG. 2. At the time of starting and stopping, the fuel gas inlet valve 12, the outlet valve 13, and the bypass are shown. The valves 15 were simultaneously switched at the same timing (however, the operation when the outlet valve 13 was stopped was excluded).

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

ところで、上記した従来の燃料電池の起動,停止制御方
法では次記のような問題点がある。すなわち燃料ガス入
口弁12,出口弁13およびバイパス弁15を同時に開閉動作
させると、各弁の開閉動作応答のずれ等も加わって燃料
電池側では燃料ガス室1dの内圧が瞬間的に大きく変動す
る。このために燃料ガス室1dと酸化剤室1eとの間に過大
な差圧が発生し、この結果として電解質層1cを通じて反
応ガスのクロスオーバーが生じたり、電極が過大な差圧
で破壊されたりする危険がある。また特に起動時にはい
ままでの停止期間中に燃料ガス室1d内に充填されていた
不活性ガスが燃料に追い出されて一気に燃料改質器2の
バーナ2dに戻されるために、燃料不足からバーナでの燃
焼が不測に失火してしまうおそれがある。
By the way, the above-mentioned conventional start / stop control method of the fuel cell has the following problems. That is, when the fuel gas inlet valve 12, the outlet valve 13 and the bypass valve 15 are simultaneously opened and closed, the internal pressure of the fuel gas chamber 1d on the fuel cell side momentarily fluctuates greatly due to the deviation of the opening / closing response of each valve and the like. . For this reason, an excessive differential pressure is generated between the fuel gas chamber 1d and the oxidant chamber 1e, and as a result, reaction gas crossover occurs through the electrolyte layer 1c, or the electrode is destroyed by the excessive differential pressure. There is a risk of Further, especially at the time of startup, the inert gas filled in the fuel gas chamber 1d during the previous stop period is expelled by the fuel and returned to the burner 2d of the fuel reformer 2 at once, so that the burner is insufficient due to lack of fuel. There is a risk that the combustion of will accidentally ignite.

この発明は上記の点にかんがみ成されたものであり、そ
の目的は燃料電池の起動,停止時におけるガス切換えに
際して燃料ガス室と酸化剤室との間の過大な差圧,改質
器バーナの不測な失火発生を未然に防止して安全性の向
上を図るとともに、併せて燃料ガス室の不活性ガスによ
るガス置換が円滑に行えるようにした燃料電池発電設備
の起動,停止制御方法を提供することにある。
The present invention has been conceived in view of the above points, and an object thereof is an excessive differential pressure between a fuel gas chamber and an oxidant chamber when switching gas at the time of starting and stopping a fuel cell, and a reformer burner. Provide a start-up / shutdown control method for a fuel cell power generation facility, which prevents accidental misfires in advance and improves safety, and also enables smooth gas replacement by an inert gas in a fuel gas chamber. Especially.

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

上記問題点を解決するために、この発明によれば、電解
質層を挟んで設けられた燃料電池および酸化剤電極と前
記各電極に対応してそれぞれ設けられた燃料ガス室およ
び酸化剤ガス室とを備えた燃料電池と、改質原料が供給
されて水素リッチな燃料ガスを生成する改質反応器と改
質反応熱を供給するためのバーナとを備えた燃料改質器
と、燃料電池の停止時に前記燃料ガス室内に不活性ガス
を充填するための不活性ガス供給系と、前記酸化剤ガス
室および前記バーナに空気を供給する空気供給手段と、
前記改質反応で生成された燃料ガスを前記燃料ガス室に
供給する燃料ガス入口管と、燃料電池における起電反応
で消費されずに前記燃料ガス室から排出されるオフ燃料
ガスを前記バーナに供給する燃料ガス出口管と、前記改
質反応で生成された燃料ガスを燃料電池をバイパスして
前記バーナへ供給するために前記燃料ガス入口管と燃料
ガス出口管との間を接続するバイパス管と、該バイパス
管接続部より燃料電池側であって前記燃料ガス入口管お
よび燃料ガス出口管のライン上にそれぞれ介装された燃
料ガス入口弁および燃料ガス出口弁と、前記バイパス管
のライン上に介装されたバイバス弁とを備えた燃料電池
発電設備の起動,停止制御方法において、燃料電池の起
動時にはまず前記燃料ガス出口弁を開き、次いで燃料ガ
ス入口弁を開いた後にバイパス弁を閉じ、停止時にはま
ずバイパス弁を開いた後に燃料ガス入口弁を閉じ、ここ
で前記不活性ガス供給系を通じて供給した不活性ガスで
燃料ガス室内をガス置換した後に燃料ガス出口弁を閉じ
るよう相互に時間差を与えて前記各弁を開閉操作するよ
うにしたものである。
In order to solve the above problems, according to the present invention, a fuel cell and an oxidant electrode provided with an electrolyte layer sandwiched between them, and a fuel gas chamber and an oxidant gas chamber provided corresponding to each of the electrodes are provided. Of the fuel cell, a fuel cell provided with a reforming reactor for supplying a reforming raw material to generate a hydrogen-rich fuel gas, and a burner for supplying heat of the reforming reaction, An inert gas supply system for filling the fuel gas chamber with an inert gas when stopped, and an air supply means for supplying air to the oxidant gas chamber and the burner,
A fuel gas inlet pipe for supplying the fuel gas generated by the reforming reaction to the fuel gas chamber, and an off fuel gas discharged from the fuel gas chamber without being consumed by the electromotive reaction in the fuel cell to the burner. A fuel gas outlet pipe for supplying and a bypass pipe connecting between the fuel gas inlet pipe and the fuel gas outlet pipe for supplying the fuel gas generated by the reforming reaction to the burner by bypassing the fuel cell. A fuel gas inlet valve and a fuel gas outlet valve, which are disposed on the fuel cell side of the bypass pipe connection portion and on the lines of the fuel gas inlet pipe and the fuel gas outlet pipe, respectively, and on the line of the bypass pipe. In a start-up / shutdown control method for a fuel cell power generation facility including a bypass valve interposed in a fuel cell, the fuel gas outlet valve is first opened when the fuel cell is started, and then the fuel gas inlet valve is opened. Closed the bypass valve, and at the time of stop, first opened the bypass valve and then closed the fuel gas inlet valve.Here, the fuel gas chamber was replaced with the inert gas supplied through the inert gas supply system, and then the fuel gas outlet valve was closed. The respective valves are opened and closed by giving a time difference to each other so as to close them.

〔作用〕[Action]

上記の制御方法を採用することにより、まず燃料電池の
起動時には燃料ガス出口弁を開いた後に入口弁を開くの
で、弁の機械的な開放応答時間の遅れ等の影響を受ける
ことなく燃料ガス室内への燃料ガス導入による急激な内
圧の上昇を確実に避けることができ、さらに入口弁の開
放後に時間差を置いてバイパス弁を閉じることにより、
燃料ガス室内に充填されていた不活性ガスを燃料改質器
のバーナに向けて追い出す過程でもバイパス弁を通じて
バーナへの燃料ガス供給が確保されており、したがって
バーナの不測な失火が防止できる。
By adopting the above control method, the fuel gas outlet valve is first opened and then the inlet valve is opened when the fuel cell is started, so the fuel gas chamber is not affected by the mechanical opening response time delay of the valve. It is possible to reliably avoid a sudden increase in internal pressure due to the introduction of fuel gas into the fuel cell, and by closing the bypass valve with a time lag after opening the inlet valve,
Even in the process of expelling the inert gas filled in the fuel gas chamber toward the burner of the fuel reformer, the supply of fuel gas to the burner is secured through the bypass valve, and therefore accidental misfire of the burner can be prevented.

また停止時にもバイパス弁の開放後、燃料ガス出口弁に
先立って入口弁を閉じ、かつこの状態で不活性ガスによ
る燃料ガス室のガス置換を行うことにより、起動時と同
様に酸化剤室との間の過大な差圧の発生,燃料改質器の
バーナ失火を避けつつガス置換が円滑に行われるように
なる。
Even when stopped, the bypass valve is opened, the inlet valve is closed prior to the fuel gas outlet valve, and the fuel gas chamber is replaced with an inert gas in this state, so that the oxidant chamber is replaced with the oxidant chamber. The gas replacement can be smoothly performed while avoiding the generation of excessive pressure difference between the two and burner misfire of the fuel reformer.

〔実施例〕〔Example〕

第1図はこの発明による燃料電池の起動,停止制御のタ
イムチャートを示すものであり、第3図とともに前記タ
イムチャートにしたがって燃料電池の起動,停止時にお
けるガス切換え動作を説明する。
FIG. 1 is a time chart of the start / stop control of the fuel cell according to the present invention. The gas switching operation at the time of start / stop of the fuel cell will be described with reference to FIG. 3 together with the time chart.

まず燃料電池の起動準備状態では、従来と同様に燃料改
質器2で改質原料が水素リッチな燃料ガスに改質された
上で開放状態にあるバイパス弁15を経て改質器のバーナ
2dに還流し、ここで燃焼して改質反応に必要な熱を与え
ている。一方、この時点では燃料電池1の燃料ガス入口
弁12,出口弁13は閉じていて燃料ガス室1dの内部に不活
性ガスが充填されており、かつ不活性ガス供給弁14も閉
じた状態にある。
First, when the fuel cell is ready to start up, the reforming raw material is reformed into the hydrogen-rich fuel gas in the fuel reformer 2 as in the conventional case, and then the burner of the reformer is passed through the bypass valve 15 which is in the open state.
Reflux to 2d, where it burns to provide the heat necessary for the reforming reaction. On the other hand, at this time, the fuel gas inlet valve 12 and the outlet valve 13 of the fuel cell 1 are closed, the inside of the fuel gas chamber 1d is filled with the inert gas, and the inert gas supply valve 14 is also closed. is there.

ここで燃料電池1を起動する際には、まず燃料ガス出口
弁13を開き、指定の時間差t1だけ遅れて入口偏12を開放
する。これにより改質器2で得た燃料ガスが燃料ガス室
1d内に導入されて不活性ガスを押し出してガス置換する
とともに、燃料電池1は酸化剤室1eに供給された反応空
気とによる起電反応で発電を開始する。なおこの時点で
はバイパス弁15が開いていて燃料ガスの一部はバイパス
弁15を通じて改質器のバーナ2dに供給継続されており、
前記のガス置換により燃料ガス室から追い出された不活
性ガスでバーナが不測に失火することはないし、また燃
料ガス室内部での急激な内圧上昇の発生もない。一方、
入口弁12の開放後に燃料ガス室1d内が完全にガス置換さ
れるに要する時間t2だけ遅れて次にバイパス弁15が閉
じ、改質器2で生成した燃料ガスの全量を燃料電池の燃
料ガス室1dに供給して定常発電に移行させるとともに、
そのオフガスを改質器2のバーナ2dに戻して改質動作を
継続させる。
When starting the fuel cell 1, the fuel gas outlet valve 13 is first opened, and the inlet bias 12 is opened with a delay of a designated time difference t1. As a result, the fuel gas obtained in the reformer 2 becomes the fuel gas chamber.
While being introduced into 1d to push out the inert gas to replace the gas, the fuel cell 1 starts power generation by an electromotive reaction with the reaction air supplied to the oxidant chamber 1e. At this time, the bypass valve 15 is open, and a part of the fuel gas is continuously supplied to the burner 2d of the reformer through the bypass valve 15.
The inert gas expelled from the fuel gas chamber due to the gas replacement does not accidentally cause the burner to misfire, and the internal pressure of the fuel gas chamber does not suddenly increase. on the other hand,
After the inlet valve 12 is opened, the bypass valve 15 is closed after a delay of time t2 required to completely replace the gas in the fuel gas chamber 1d, and the entire amount of the fuel gas generated in the reformer 2 is changed to the fuel gas of the fuel cell. While supplying to room 1d to shift to steady power generation,
The off gas is returned to the burner 2d of the reformer 2 to continue the reforming operation.

一方、燃料電池を停止する場合には、まずバイパス弁15
を開放し、改質器2で生成した燃料ガスの一部をバイパ
ス弁15を通じて改質器のバーナ2dにバイパス供給させ
る。次に時間差t3だけ遅れて燃料ガス入口弁12を閉じ、
この状態で不活性ガス供給弁14を開放して燃料ガス室1d
内を不活性ガスでガス置換する。さらにこのガス置換に
要する時間t4だけ遅れて燃料ガス出口弁13を閉じて燃料
ガス室1d内に不活性ガスを封じ込める。これによりガス
置換が円滑に行えるとともに、燃料ガス室1dの急激な内
圧変化,およびこれに起因する酸化剤室1eとの間の過大
な差圧発生、並びに改質器側での燃料ガス供給中断によ
るバーナ2dの不測な失火を確実に防止することができ
る。
On the other hand, when shutting down the fuel cell, first the bypass valve 15
Is opened, and a part of the fuel gas generated in the reformer 2 is bypass-supplied to the burner 2d of the reformer through the bypass valve 15. Next, the fuel gas inlet valve 12 is closed with a delay of time difference t3,
In this state, the inert gas supply valve 14 is opened to open the fuel gas chamber 1d.
The inside is replaced with an inert gas. Further, the fuel gas outlet valve 13 is closed with a delay of the time t4 required for this gas replacement to contain the inert gas in the fuel gas chamber 1d. As a result, gas replacement can be performed smoothly, a sudden change in the internal pressure of the fuel gas chamber 1d, an excessive pressure difference between the fuel gas chamber 1d and the oxidant chamber 1e, and a fuel gas supply interruption on the reformer side It is possible to reliably prevent accidental misfire of the burner 2d due to.

〔発明の効果〕〔The invention's effect〕

以上述べたようにこの発明によれば、燃料電池の起動時
にはまず燃料ガス出口弁を開き、次いで入口弁を開いた
後にバイパス弁を閉じ、停止時にはまずバイパス弁を開
いた後に入口弁を閉じ、ここで不活性ガス供給系を通じ
て供給した不活性ガスで燃料ガス室内をガス置換した後
に出口弁を閉じるように相互に時間差を与えて各弁を開
閉操作することにより、燃料電池の起動,停止に際して
燃料ガス室の内圧の急激な変動,およびこれに起因する
酸化剤室との間の過大な差圧の発生、並びに燃料改質器
のバーナでの不測な失火を防止して安全性の改善を図り
つつ、併せて燃料ガス室の燃料ガスと不活性ガスとの間
のガス置換を円滑に行うことができる。
As described above, according to the present invention, when the fuel cell is activated, the fuel gas outlet valve is first opened, then the inlet valve is opened and then the bypass valve is closed, and when stopped, the bypass valve is first opened and then the inlet valve is closed. At the time of starting and stopping the fuel cell, the fuel gas chamber is replaced with the inert gas supplied through the inert gas supply system, and then the valves are opened and closed by giving a time difference to each other so that the outlet valves are closed. Improving safety by preventing sudden changes in the internal pressure of the fuel gas chamber, generation of excessive differential pressure between it and the oxidant chamber, and accidental misfires in the burner of the fuel reformer. At the same time, the gas replacement between the fuel gas and the inert gas in the fuel gas chamber can be smoothly performed.

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

第1図は本発明の実施例による燃料電池の起動,停止時
におけるガス切換え制御のタイムチャート、第2図は第
1図に対応する従来の制御方法によるタイムチャート、
第3図は燃料電池発電設備の系統図である。図におい
て、 1:燃料電池、1d:燃料ガス室、2:燃料改質器、2d:燃焼バ
ーナ、4:改質原料タンク、10:不活性ガス供給管、12:燃
料ガス入口弁、13:燃料ガス出口弁、14:不活性ガス供給
弁、15:燃料ガスバイパス弁。
FIG. 1 is a time chart of gas switching control when starting and stopping a fuel cell according to an embodiment of the present invention, and FIG. 2 is a time chart of a conventional control method corresponding to FIG.
FIG. 3 is a system diagram of a fuel cell power generation facility. In the figure, 1: fuel cell, 1d: fuel gas chamber, 2: fuel reformer, 2d: combustion burner, 4: reforming raw material tank, 10: inert gas supply pipe, 12: fuel gas inlet valve, 13: Fuel gas outlet valve, 14: inert gas supply valve, 15: fuel gas bypass valve.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】電解質層を挟んで設けられた燃料電極およ
び酸化剤電極と前記各電極に対応してそれぞれ設けられ
た燃料ガス室および酸化剤ガス室とを備えた燃料電池
と、改質原料が供給されて水素リッチな燃料ガスを生成
する改質反応器と改質反応熱を供給するためのバーナと
を備えた燃料改質器と、燃料電池の停止時に前記燃料ガ
ス室内に不活性ガスを充填するための不活性ガス供給系
と、前記酸化剤ガス室および前記バーナに空気を供給す
る空気供給手段と、前記改質反応で生成された燃料ガス
を前記燃料ガス室に供給する燃料ガス入口管と、燃料電
池における起電反応で消費されずに前記燃料ガス室から
排出されるオフ燃料ガスを前記バーナに供給する燃料ガ
ス出口管と、前記改質反応で生成された燃料ガスを燃料
電池をバイパスして前記バーナへ供給するために前記燃
料ガス入口管と燃料ガス出口管との間を接続するバイパ
ス管と、該バイパス管接続部より燃料電池側であって前
記燃料ガス入口管および燃料ガス出口管のライン上にそ
れぞれ介装された燃料ガス入口弁および燃料ガス出口弁
と、前記バイパス管のライン上に介装されたバイバス弁
とを備えた燃料電池発電設備の起動,停止制御方法であ
って、燃料電池の起動時にはまず前記燃料ガス出口弁を
開き、次いで燃料ガス入口弁を開いた後にバイパス弁を
閉じ、停止時にはまずバイパス弁を開いた後に燃料ガス
入口弁を閉じ、ここで前記不活性ガス供給系を通じて供
給した不活性ガスで燃料ガス室内をガス置換した後に燃
料ガス出口弁を閉じるよう相互に時間差を与えて前記各
弁を開閉操作することを特徴とする燃料電池発電設備の
起動,停止制御方法。
1. A fuel cell provided with a fuel electrode and an oxidant electrode sandwiching an electrolyte layer, and a fuel gas chamber and an oxidant gas chamber provided corresponding to each of the electrodes, and a reforming raw material. Is supplied to produce a hydrogen-rich fuel gas and a fuel reformer having a burner for supplying heat of the reforming reaction, and an inert gas in the fuel gas chamber when the fuel cell is stopped. An inert gas supply system for filling the air, an air supply means for supplying air to the oxidant gas chamber and the burner, and a fuel gas for supplying the fuel gas generated by the reforming reaction to the fuel gas chamber. An inlet pipe, a fuel gas outlet pipe for supplying the burner with off-fuel gas exhausted from the fuel gas chamber without being consumed by an electromotive reaction in the fuel cell, and a fuel gas produced by the reforming reaction as fuel. Bypass the battery A bypass pipe connecting between the fuel gas inlet pipe and the fuel gas outlet pipe for supplying to the burner, and a fuel cell side of the bypass pipe connecting portion of the fuel gas inlet pipe and the fuel gas outlet pipe. A start and stop control method for a fuel cell power generation facility comprising a fuel gas inlet valve and a fuel gas outlet valve respectively installed on a line, and a bypass valve installed on the line of the bypass pipe, When the fuel cell is started, the fuel gas outlet valve is first opened, then the fuel gas inlet valve is opened and then the bypass valve is closed, and when the fuel cell is stopped, the bypass valve is first opened and then the fuel gas inlet valve is closed. A fuel characterized in that after the fuel gas chamber is replaced with an inert gas supplied through a supply system, the fuel gas outlet valve is closed and a time lag is applied to open and close each valve. Start-up of the cell power plant, stop control method.
JP62145499A 1987-06-11 1987-06-11 Start / stop control method for fuel cell power generation equipment Expired - Lifetime JPH0690930B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62145499A JPH0690930B2 (en) 1987-06-11 1987-06-11 Start / stop control method for fuel cell power generation equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62145499A JPH0690930B2 (en) 1987-06-11 1987-06-11 Start / stop control method for fuel cell power generation equipment

Publications (2)

Publication Number Publication Date
JPS63308876A JPS63308876A (en) 1988-12-16
JPH0690930B2 true JPH0690930B2 (en) 1994-11-14

Family

ID=15386672

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62145499A Expired - Lifetime JPH0690930B2 (en) 1987-06-11 1987-06-11 Start / stop control method for fuel cell power generation equipment

Country Status (1)

Country Link
JP (1) JPH0690930B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7402352B2 (en) * 2002-05-14 2008-07-22 Nissan Motor Co., Ltd. Fuel cell system and related startup method
JP4789505B2 (en) * 2005-05-11 2011-10-12 アイシン精機株式会社 Fuel cell system
JP5309799B2 (en) * 2008-08-29 2013-10-09 アイシン精機株式会社 Reformer and fuel cell system
JP2010135287A (en) * 2008-11-04 2010-06-17 Panasonic Corp Fuel cell system

Also Published As

Publication number Publication date
JPS63308876A (en) 1988-12-16

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