JPH03219564A - Fuel cell power generator device - Google Patents

Fuel cell power generator device

Info

Publication number
JPH03219564A
JPH03219564A JP2035317A JP3531790A JPH03219564A JP H03219564 A JPH03219564 A JP H03219564A JP 2035317 A JP2035317 A JP 2035317A JP 3531790 A JP3531790 A JP 3531790A JP H03219564 A JPH03219564 A JP H03219564A
Authority
JP
Japan
Prior art keywords
electrode
fuel
fuel cell
gas
hydrogen
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
JP2035317A
Other languages
Japanese (ja)
Inventor
Akitoshi Seya
瀬谷 彰利
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 JP2035317A priority Critical patent/JPH03219564A/en
Publication of JPH03219564A publication Critical patent/JPH03219564A/en
Pending 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
    • H01M8/04Auxiliary 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
    • 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
    • H01M8/24Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/241Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/24Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2457Grouping of fuel cells, e.g. stacking of fuel cells with both reactants being gaseous or vaporised
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/24Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2465Details of groupings of fuel cells
    • H01M8/2483Details of groupings of fuel cells characterised by internal manifolds
    • 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
    • H01M8/0656Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants by electrochemical means
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

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  • 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 stop the generating operation of a fuel cell in the state where the deterioration of a formed oxidizing agent electrode catalyst is suppressed by connecting a water electrolytic device, utilizing electrode potential difference to electrolyze water, mixing the formed hydrogen with nitrogen, and supplying it to a fuel electrode. CONSTITUTION:The inert gas replacement of a fuel cell 1 is conducted, and a pair of electrodes of a water electrolytic device are electrically connected to the cell 1. At that time, the fuel electrode and oxidizing agent electrode 4A of the cell 1 generate potentials corresponding to the adsorption quantities of hydrogen and oxygen, and a potential difference exceeding the potential necessary for the electrolysis of water is applied between the electrodes of the water electrolytic device 11. Consequently, hydrogen and oxygen of the quantities corresponding to the remaining adsorbed gas quantities are formed by the electrolysis of water. As the quantity of hydrogen formed thereby is regularly larger than the remaining adsorbed oxygen on the oxidizing agent electrode 4A by a stoichiometric ratio or more, the formed hydrogen is mixed with nitrogen for inert gas replacement and supplied to a fuel electrode 3A through a fuel gas chamber 3, whereby the remaining adsorbed oxygen of the oxidizing agent electrode is consumed and removed on the bases of the electrostatic reaction of the fuel cell.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は主としてマトリックス形燃料電池発電装置、
ことに発電運転を停止する際酸化剤電極1 上に残留する残留吸着酸素を積極的に消費する停止装置
を備えた燃料電池発電装置に関する。
[Detailed Description of the Invention] [Industrial Application Field] This invention mainly relates to a matrix type fuel cell power generation device,
In particular, the present invention relates to a fuel cell power generation device equipped with a stop device that actively consumes residual adsorbed oxygen remaining on the oxidizer electrode 1 when power generation operation is stopped.

〔従来の技術〕[Conventional technology]

周知のように、燃料電池は電解液を保持したマトリック
スを一対の燃料電極と酸化剤電極で挟んだ単電池複数個
を積層面にガス不透過板を介装して積層したセルスタッ
クとし、燃料電極とガス不透過板との間に画成された燃
料ガス室に水素リンチな燃料ガスを供給し、酸化剤電極
とガス不透過板との間に画成された酸化剤室に酸化剤と
しての空気または酸素を供給することによって発電を行
うちのである。また、燃料電池は発電反応によって酸化
剤電極側に生成水を生ずるので、電解液としての吸湿性
の高いリン酸を用いる電池ではその運転温度を130℃
から190℃、一般には190℃程度の高温に保って生
成水の排出を容易化するとともに、電極触媒の活性を保
持して発電運転が行われる。
As is well known, a fuel cell is a cell stack consisting of multiple single cells in which a matrix holding an electrolyte is sandwiched between a pair of fuel electrodes and an oxidizer electrode, with a gas-impermeable plate interposed between the stacked surfaces. A hydrogen-rich fuel gas is supplied to the fuel gas chamber defined between the electrode and the gas impermeable plate, and a hydrogen-rich fuel gas is supplied as an oxidizer to the oxidizer chamber defined between the oxidizer electrode and the gas impermeable plate. It generates electricity by supplying air or oxygen. In addition, since fuel cells generate water on the oxidizer electrode side due to the power generation reaction, the operating temperature of batteries that use highly hygroscopic phosphoric acid as the electrolyte is 130°C.
to 190° C., generally about 190° C., to facilitate discharge of generated water, and to maintain the activity of the electrode catalyst for power generation operation.

このようにして運転される燃料電池の運転を停止または
休止するために外部負荷回路に流れる電流を遮断すると
、各単電池には高い値の高温開回路電圧が発生し、電極
触媒粒子が粗大化して電極表面積が低下する劣化現象(
シンタリングと呼ぶ)が発生し、発電性能の低下や寿命
低下をまねくこと、電池温度の低下とともに反応ガス中
の水分を吸着してリン酸が希釈され、体積膨張したリン
酸液がマトリックスから電極側に過度にしみ出して反応
ガスの供給障害を起こすこと、さらには、リン酸液の漏
出したマトリックスのガス区分機能が低下して反応ガス
としての空気と燃料ガスが混触し、爆鳴気を発生する危
険性が高まること、など種々の障害が発生する。
When the current flowing to the external load circuit is cut off in order to stop or suspend the operation of a fuel cell operated in this way, a high temperature open circuit voltage is generated in each unit cell, and the electrode catalyst particles become coarse. A deterioration phenomenon in which the electrode surface area decreases (
(called sintering) occurs, leading to a decrease in power generation performance and shortened lifespan.As the battery temperature decreases, the phosphoric acid adsorbs moisture in the reaction gas, diluting the phosphoric acid, and the phosphoric acid solution expands in volume and is transferred from the matrix to the electrode. In addition, the gas separation function of the matrix from which the phosphoric acid solution leaked may deteriorate, causing the air as a reaction gas to mix with the fuel gas, resulting in explosion gas. Various obstacles occur, such as an increased risk of occurrence.

そこでこれらの障害を回避して燃料電池の発電を停止す
るために、外部負荷回路を遮断するとともに、燃料ガス
および酸化剤ガスの供給を停止し、燃料ガス通路および
その給排マニホールドからなる燃料ガス室および酸化剤
通路および給排マニホールドからなる酸化剤室それぞれ
に乾燥した窒素などの不活性ガスを供給して残存反応ガ
ス (燃料ガスまたは酸化剤)をパージしながら燃料電
池を降温する方法が知られている。
Therefore, in order to avoid these failures and stop the power generation of the fuel cell, the external load circuit is cut off, and the supply of fuel gas and oxidizing gas is stopped. A method is known to lower the temperature of a fuel cell while purging residual reaction gas (fuel gas or oxidizer) by supplying an inert gas such as dry nitrogen to each of the oxidizer chambers, oxidizer passages, and supply/discharge manifolds. It is being

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

上述の従来方法においては、外部から窒素ガスを供給す
ることによって両ガス室内の反応ガスを早期にパージす
ることができるので、高温開回路電圧による障害やリン
酸の吸湿に起因する障害、ならびに反応ガスが混触する
危険性を回避することができるものと考えられてきた。
In the conventional method described above, by supplying nitrogen gas from the outside, the reaction gas in both gas chambers can be purged at an early stage. It has been thought that the danger of gas mixture can be avoided.

しかしながら酸化剤電極側には電極触媒粒子の表面に化
学吸着している残存吸着酸素が存在しており、窒素ガス
によるパージだけではこの残存吸着酸素を脱着できず、
これが原因で酸化剤電極は高い電位を保持していること
が最近の研究で明らかになり、酸化剤電極が冷えるまで
の高温状態で高い電位にさらされることにより、触媒層
に悪影響が現われることを回避できない欠点がある。
However, on the oxidizer electrode side, there is residual adsorbed oxygen that is chemically adsorbed on the surface of the electrode catalyst particles, and this residual adsorbed oxygen cannot be desorbed only by purging with nitrogen gas.
Recent research has revealed that this is the reason why the oxidizer electrode maintains a high potential, and that exposing the oxidizer electrode to a high potential at high temperatures until it cools down can have an adverse effect on the catalyst layer. There are drawbacks that cannot be avoided.

この発明の目的は、残存吸着酸素を積極的に消費する停
止装置を付加することにより、燃料電池の電極触媒層に
与える悪影響を排除することにある。
An object of the present invention is to eliminate the adverse effects on the electrode catalyst layer of a fuel cell by adding a stop device that actively consumes residual adsorbed oxygen.

〔課題を解決するための手段〕[Means to solve the problem]

上記目的はこの発明によれば、燃料電極および酸化剤電
極を有する単電池の積層体からなり、燃料ガス室および
酸化剤ガス室を介して前記燃料電極および酸化剤電極に
反応ガスとしての燃料ガスおよび酸化剤を供給して発電
を行い、その発電電力を電力変換装置を介して外部負荷
に供給するとともに、発電運転の停止時には前記燃料ガ
スおよび酸化剤を不活性ガスに切り換えてガス置換を行
うものにおいて、 前記燃料電極と酸化剤電極にスイッチを介して電気接続
されるとともに、燃料電池の起電力を用い水電解により
発生した水素を前記不活性ガスに混合して前記燃料ガス
室に供給する水電気分解装置を備えることにより達成さ
れる。
According to the present invention, the above object is made of a stack of unit cells having a fuel electrode and an oxidizer electrode, and a fuel gas as a reaction gas is supplied to the fuel electrode and the oxidizer electrode via a fuel gas chamber and an oxidizer gas chamber. and an oxidizer to generate power, and supply the generated power to an external load via a power converter, and when power generation operation is stopped, the fuel gas and oxidizer are switched to an inert gas for gas replacement. The hydrogen electrode is electrically connected to the fuel electrode and the oxidizer electrode via a switch, and hydrogen generated by water electrolysis using the electromotive force of the fuel cell is mixed with the inert gas and supplied to the fuel gas chamber. This is achieved by providing a water electrolyzer.

〔作用〕[Effect]

上記手段において、燃料電池のガス置換を行うとともに
燃料電池に水電気分解装置の一対の電極を導電接続する
。このとき、燃料電池の燃料電極および酸化剤電極は吸
着水素量および吸着酸素量に相応する電位を発生してお
り、水電気分解装置の電極間には水の電気分解に必要な
電位を超える電位差が印加されるので、水の電気分解に
よって残存吸着ガス量に見合う量の水素および酸素が生
成される。生成した水素量は酸化剤電極側の残存吸着酸
素より化学量論比以上に常に大きいので、この生成水素
をガス置換用の窒素に混合して燃料ガス室を介して燃料
電極に供給することにより、燃料電池の起電反応に基づ
いて酸化剤電極の残存吸着酸素を消費して除去すること
ができる。なお、必要に応じて燃料電池に放電抵抗を接
続されば、吸着酸素の消費を促進することができる。
In the above means, gas is replaced in the fuel cell, and a pair of electrodes of a water electrolyzer are electrically connected to the fuel cell. At this time, the fuel electrode and oxidizer electrode of the fuel cell generate a potential corresponding to the amount of adsorbed hydrogen and oxygen, and the potential difference between the electrodes of the water electrolyzer exceeds the potential required for water electrolysis. is applied, hydrogen and oxygen are generated by electrolysis of water in an amount commensurate with the amount of residual adsorbed gas. Since the amount of generated hydrogen is always greater than the stoichiometric ratio than the residual adsorbed oxygen on the oxidizer electrode side, by mixing this generated hydrogen with nitrogen for gas replacement and supplying it to the fuel electrode via the fuel gas chamber. , the residual adsorbed oxygen of the oxidizer electrode can be consumed and removed based on the electromotive reaction of the fuel cell. Note that if a discharge resistor is connected to the fuel cell as necessary, consumption of adsorbed oxygen can be promoted.

〔実施例〕〔Example〕

以下この発明を実施例に基いて説明する。 This invention will be explained below based on examples.

第1図はこの発明の燃料電池発電装置の実施例を示す概
略構成図である。図において、3Aは略示的に表わした
リン酸型燃料電池本体1の燃料電極、2はマトリックス
、4Aは酸化剤電極である。かかる燃料電池本体1の両
極には水電気分解装置のスイッチ7を介して水電気分解
装置11の一対の電極13A、 14Aが電気的に接続
されている。水電気分解装置11の水素発生室13はバ
ルブ8を介して燃料供給ラインに接続されており、一方
酸素発生室14は発電システム外へ開放される。燃料ガ
ス室3.酸化剤ガス室4の各々の入口には一方を窒素ガ
ス側に接続された三方バルブ5および三方バルブ6が接
続されている。
FIG. 1 is a schematic configuration diagram showing an embodiment of the fuel cell power generation apparatus of the present invention. In the figure, 3A is a fuel electrode of the phosphoric acid fuel cell main body 1, 2 is a matrix, and 4A is an oxidizer electrode. A pair of electrodes 13A and 14A of a water electrolyzer 11 are electrically connected to both poles of the fuel cell main body 1 via a switch 7 of the water electrolyzer. The hydrogen generation chamber 13 of the water electrolyzer 11 is connected to the fuel supply line via the valve 8, while the oxygen generation chamber 14 is opened to the outside of the power generation system. Fuel gas chamber 3. A three-way valve 5 and a three-way valve 6, each having one end connected to the nitrogen gas side, are connected to each inlet of the oxidant gas chamber 4.

燃料電池本体の停止時には、燃料電池本体1の電気負荷
を遮断し、三方バルブ5および三方バルブ6を窒素側に
切り換え窒素を両ガス室3.4に所定流量流す。同時に
水電気分解装置のスイッチ7を閉にし、一対の電極13
A、 14Aを燃料電極3Aと酸化剤電極4Aとに各々
電気的に接続する。一般に、燃料電池は燃料電極、マト
リックス、酸化剤電極からなる単セルを複数個直列に接
続しているため、各種に吸着している残存水素、残存酸
素により水の電気分解に必要な電位以上の電位差が得ら
れ、電解液室12の水が電気分解され、水素および酸素
が各々残存吸着ガス量に見合った量生成される。
When the fuel cell main body is stopped, the electrical load on the fuel cell main body 1 is cut off, the three-way valve 5 and the three-way valve 6 are switched to the nitrogen side, and nitrogen is allowed to flow into both gas chambers 3.4 at a predetermined flow rate. At the same time, the switch 7 of the water electrolyzer is closed, and the pair of electrodes 13
A and 14A are electrically connected to the fuel electrode 3A and the oxidizer electrode 4A, respectively. In general, fuel cells consist of multiple single cells connected in series, each consisting of a fuel electrode, a matrix, and an oxidizer electrode, so the residual hydrogen and oxygen adsorbed on each cell generate a potential higher than that required for water electrolysis. A potential difference is obtained, water in the electrolyte chamber 12 is electrolyzed, and hydrogen and oxygen are each produced in amounts commensurate with the amount of residual adsorbed gas.

ある時間をおき、水電気分解装置の水素発生室13に接
続されているバルブ8を開にし、燃料電極3Aに流れて
いる窒素に発生した水素を混合する。−方、酸素発生室
14で発生した酸素は燃料電池本体外へ排出される。こ
のため、燃料電極側の吸着水素量は酸化剤電極側の残存
吸着酸素より化学量論比以上に常に過剰となり、効率的
に酸化剤電極側の残存吸着酸素が除去される。さらに完
全に酸化剤電極側の残存吸着酸素を除去するためには、
放電抵抗21をスイッチ22を介して両極間に接続し、
燃料電池の電位があるレベル以下に低下したことを電圧
センサ23で検知して放電抵抗を投入する。
After a certain period of time, the valve 8 connected to the hydrogen generation chamber 13 of the water electrolyzer is opened, and the generated hydrogen is mixed with the nitrogen flowing to the fuel electrode 3A. On the other hand, oxygen generated in the oxygen generation chamber 14 is discharged to the outside of the fuel cell main body. Therefore, the amount of hydrogen adsorbed on the fuel electrode side is always in excess of the residual adsorbed oxygen on the oxidizer electrode side by more than the stoichiometric ratio, and the residual adsorbed oxygen on the oxidizer electrode side is efficiently removed. In order to further completely remove the residual adsorbed oxygen on the oxidizer electrode side,
A discharge resistor 21 is connected between the two poles via a switch 22,
When the voltage sensor 23 detects that the potential of the fuel cell has fallen below a certain level, a discharge resistor is turned on.

この放電抵抗21を介して燃料電池1に放電電流が流れ
、残存吸着酸素を起電反応により完全かつ早期に消費し
、電極電位を低下させることができる。
A discharge current flows through the fuel cell 1 through the discharge resistor 21, and the remaining adsorbed oxygen is completely and quickly consumed by an electromotive reaction, thereby making it possible to lower the electrode potential.

残存吸着酸素が消費され、これに伴って燃料電池の電極
電位が低下すると、水電気分解装置11の水素発生量も
減少し、遂には零に近づくので、これを電圧センサ23
によっ・て検知して燃料ガス室3および酸化剤ガス室4
の出口側に配された図示しない弁を閉じれば、両ガス室
を窒素ガス置換した状態で停止状態とすることができる
When the remaining adsorbed oxygen is consumed and the electrode potential of the fuel cell decreases accordingly, the amount of hydrogen generated by the water electrolyzer 11 also decreases and eventually approaches zero, which is detected by the voltage sensor 23.
The fuel gas chamber 3 and oxidizer gas chamber 4 are detected by
By closing a valve (not shown) disposed on the outlet side of the gas chamber, both gas chambers can be brought to a stopped state while being replaced with nitrogen gas.

〔発明の効果〕〔Effect of the invention〕

この発明は前述のように、発電運転の停止に際して外部
負荷を遮断し、燃料電池の反応ガス室に窒素を供給して
ガス置換するとともに、燃料電池に水電気分解装置を接
続し、残存吸着酸素による電極電位差を利用して水を電
気分解し、生成した水素を前記窒素に混合して燃料極に
供給するよう構成した。その結果、吸着酸素量に見合う
生成水素と吸着酸素を燃料電池の起電反応を利用して消
費することが可能となり、従来ガス置換だけでは除去で
きなかった酸化剤電極の残存吸着酸素を消費して電極電
位を低下できるので、電極が高電位にさらされることに
よって生ずる酸化剤電極触媒の劣化を抑制した状態で燃
料電池の発電運転を停止できる利点が得られる。また、
燃料電池の出力回路に負荷抵抗を接続して放電電流を流
すよう構成すれば、吸着酸素の消費が促進され、より早
く吸着酸素を消費することができる。
As described above, this invention cuts off the external load when power generation operation is stopped, supplies nitrogen to the reaction gas chamber of the fuel cell to replace the gas, and connects a water electrolyzer to the fuel cell to remove any remaining adsorbed oxygen. Water is electrolyzed using the electrode potential difference caused by the above, and the generated hydrogen is mixed with the nitrogen and supplied to the fuel electrode. As a result, it becomes possible to consume the generated hydrogen and adsorbed oxygen corresponding to the amount of adsorbed oxygen using the electromotive reaction of the fuel cell, and the remaining adsorbed oxygen of the oxidizer electrode, which could not be removed by conventional gas replacement alone, is consumed. Since the electrode potential can be lowered by the electrode being exposed to a high potential, it is possible to stop the power generation operation of the fuel cell while suppressing deterioration of the oxidizer electrode catalyst caused by exposing the electrode to a high potential. Also,
If a load resistor is connected to the output circuit of the fuel cell to cause a discharge current to flow, the consumption of adsorbed oxygen is promoted and the adsorbed oxygen can be consumed more quickly.

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

第1図はこの発明の燃料電池発電装置の実施例を示す概
略構成図である。 1:燃料電池、2:マトリックス、3:燃料ガス室、4
:酸化剤ガス室、5,6:三方弁、7:スイッチ、8:
バルブ、11:水電気分解装置、21:放電抵抗、3A
:燃料電極、4A二酸化剤電極。 0 第1図
FIG. 1 is a schematic configuration diagram showing an embodiment of the fuel cell power generation apparatus of the present invention. 1: Fuel cell, 2: Matrix, 3: Fuel gas chamber, 4
: Oxidizing gas chamber, 5, 6: Three-way valve, 7: Switch, 8:
Valve, 11: Water electrolyzer, 21: Discharge resistance, 3A
:Fuel electrode, 4A dioxide electrode. 0 Figure 1

Claims (1)

【特許請求の範囲】 1)燃料電極および酸化剤電極を有する単電池の積層体
からなり、燃料ガス室および酸化剤ガス室を介して前記
燃料電極および酸化剤電極に反応ガスとしての燃料ガス
および酸化剤を供給して発電を行い、その発電電力を電
力変換装置を介して外部負荷に供給するとともに、発電
運転の停止時には前記燃料ガスおよび酸化剤を不活性ガ
スに切り換えてガス置換を行うものにおいて、 前記燃料電極と酸化剤電極にスイッチを介して電気接続
されるとともに、燃料電池の起電力を用い水電解により
発生した水素を前記不活性ガスに混合して前記燃料ガス
室に供給する水電気分解装置を備えることを特徴とする
燃料電池発電装置。
[Scope of Claims] 1) Consisting of a stack of single cells having a fuel electrode and an oxidizer electrode, fuel gas as a reaction gas and A device that supplies an oxidizing agent to generate electricity, supplies the generated power to an external load via a power conversion device, and when power generation operation is stopped, switches the fuel gas and oxidizing agent to an inert gas for gas replacement. Water is electrically connected to the fuel electrode and the oxidizer electrode via a switch, and is supplied to the fuel gas chamber by mixing hydrogen generated by water electrolysis using the electromotive force of the fuel cell with the inert gas. A fuel cell power generation device comprising an electrolyzer.
JP2035317A 1989-11-22 1990-02-16 Fuel cell power generator device Pending JPH03219564A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2035317A JPH03219564A (en) 1989-11-22 1990-02-16 Fuel cell power generator device

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP1-304095 1989-11-22
JP30409589 1989-11-22
JP2035317A JPH03219564A (en) 1989-11-22 1990-02-16 Fuel cell power generator device

Publications (1)

Publication Number Publication Date
JPH03219564A true JPH03219564A (en) 1991-09-26

Family

ID=26374294

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2035317A Pending JPH03219564A (en) 1989-11-22 1990-02-16 Fuel cell power generator device

Country Status (1)

Country Link
JP (1) JPH03219564A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003536232A (en) * 2000-06-22 2003-12-02 ユーティーシー フューエル セルズ,エルエルシー Method and apparatus for regenerating PEM fuel cell performance
KR20050054125A (en) * 2003-12-04 2005-06-10 김학수 An oxygen and nitrogen generating apparatus using an electrolysis device and a fuel cell
JP2007149574A (en) * 2005-11-30 2007-06-14 Toyota Motor Corp Fuel cell system
JP2007273300A (en) * 2006-03-31 2007-10-18 Daido Metal Co Ltd Air intake type fuel cell

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003536232A (en) * 2000-06-22 2003-12-02 ユーティーシー フューエル セルズ,エルエルシー Method and apparatus for regenerating PEM fuel cell performance
KR20050054125A (en) * 2003-12-04 2005-06-10 김학수 An oxygen and nitrogen generating apparatus using an electrolysis device and a fuel cell
JP2007149574A (en) * 2005-11-30 2007-06-14 Toyota Motor Corp Fuel cell system
US8110311B2 (en) 2005-11-30 2012-02-07 Toyota Jidosha Kabushiki Kaisha Fuel cell system
JP2007273300A (en) * 2006-03-31 2007-10-18 Daido Metal Co Ltd Air intake type fuel cell

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