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JP2815690B2 - Startup control device for liquid electrolyte fuel cell - Google Patents

Startup control device for liquid electrolyte fuel cell

Info

Publication number
JP2815690B2
JP2815690B2 JP2235121A JP23512190A JP2815690B2 JP 2815690 B2 JP2815690 B2 JP 2815690B2 JP 2235121 A JP2235121 A JP 2235121A JP 23512190 A JP23512190 A JP 23512190A JP 2815690 B2 JP2815690 B2 JP 2815690B2
Authority
JP
Japan
Prior art keywords
fuel cell
amount
condenser
temperature
water
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
JP2235121A
Other languages
Japanese (ja)
Other versions
JPH04115468A (en
Inventor
義治 小林
守敏 長坂
晃 新田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fuji Electric Co Ltd
Daihen Corp
Original Assignee
Fuji Electric Co Ltd
Daihen Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fuji Electric Co Ltd, Daihen Corp filed Critical Fuji Electric Co Ltd
Priority to JP2235121A priority Critical patent/JP2815690B2/en
Publication of JPH04115468A publication Critical patent/JPH04115468A/en
Application granted granted Critical
Publication of JP2815690B2 publication Critical patent/JP2815690B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • 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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  • 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、液体電解質型燃料電池発電装置、ことに
燃料電池の起動時に保管温度から運転温度に昇温する起
動制御装置を備えた燃料電池発電装置に関する。
Description: BACKGROUND OF THE INVENTION The present invention relates to a liquid-electrolyte fuel cell power generator, and more particularly, to a fuel cell having a start-up control device that raises the temperature from a storage temperature to an operating temperature when the fuel cell is started. It relates to a power generator.

〔従来の技術〕[Conventional technology]

この種の燃料電池は、液体電解質として例えば水酸化
カリウム水溶液を満たした電解液室と、この電解液室を
挟んでその両側に対向するよう配された燃料電極,酸化
剤電極と、各電極に対応する反応ガス室とからなり、か
つ各反応ガス室を通じて各電極へ燃料ガス(水素)およ
び酸化剤ガス(空気)を供給することにより、電極内部
での起電反応で発電することは周知の通りである。ま
た、この起電反応は発熱反応であり、かつ水素と酸素が
反応して燃料電極側に水を生成する。
This type of fuel cell has an electrolyte chamber filled with, for example, a potassium hydroxide aqueous solution as a liquid electrolyte, and a fuel electrode and an oxidant electrode arranged on both sides of the electrolyte chamber so as to face each other. It is well known that power is generated by an electromotive reaction inside an electrode by supplying a fuel gas (hydrogen) and an oxidizing gas (air) to each electrode through each reaction gas chamber. It is on the street. Further, this electromotive reaction is an exothermic reaction, and hydrogen and oxygen react to generate water on the fuel electrode side.

上記の生成水がこのまま電池内部に溜まって液体電解
質中に溶け込むと、電解液が希釈され、起電反応が徐々
に低下する。このために、電解液濃度の適正維持を図る
管理方式として、反応ガスを適量循環送風させ、生成水
を水蒸気として燃料電池の外部に取り出し、燃料電池の
出口に設置した凝縮器により凝縮,分離する方法が知ら
れている。また前記反応ガスの循環量は、生成水量と凝
縮水量がほぼ一致するよう、演算制御部により適正値を
求め、制御する方法がとられている。
When the generated water accumulates inside the battery as it is and dissolves in the liquid electrolyte, the electrolyte is diluted, and the electromotive reaction gradually decreases. For this purpose, as a management method for maintaining an appropriate concentration of the electrolyte, a suitable amount of the reaction gas is circulated and blown, the generated water is taken out of the fuel cell as water vapor, and is condensed and separated by a condenser installed at the outlet of the fuel cell. Methods are known. The circulation amount of the reaction gas is determined and controlled by an arithmetic and control unit so that the generated water amount and the condensed water amount substantially match.

ところで、燃料電池は起電反応に適する運転温度(通
常100℃以下)があり、起動時には保管状態の温度から
前記運転温度に昇温する必要がある。従来、この方法と
しては、燃料電池が電気ヒータを内蔵し、起動時にバッ
テリーなどの電源より電流を供給して加熱する方法。ま
たは、燃料電池の電気出力側に負荷抵抗を接続して通電
させ、燃料電池自体の起電反応生成熱により昇温する方
法等がとられている。
By the way, a fuel cell has an operating temperature (usually 100 ° C. or lower) suitable for an electromotive reaction, and it is necessary to raise the temperature from a stored state to the operating temperature at the time of startup. Conventionally, as this method, a fuel cell has a built-in electric heater and is heated by supplying current from a power source such as a battery at the time of startup. Alternatively, a load resistance is connected to the electric output side of the fuel cell to energize the fuel cell, and the temperature is raised by the heat generated by the electromotive reaction of the fuel cell itself.

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

ところで、前述した従来の燃料電池の起動方法には次
のような問題点がある。
By the way, the conventional fuel cell starting method described above has the following problems.

(1)加熱手段としての電気ヒータ,補助バッテリー等
の付属装置が必要であり、これが原因で装置が大型化す
る。
(1) Attached devices such as an electric heater and an auxiliary battery are required as a heating means, and the size of the device is increased due to this.

(2)負荷抵抗による発電昇温時にも前記生成水が発生
しており、燃料電池温度が低い状態では飽和水蒸気圧も
低く、凝縮器で分離できる除去水量が少ないため、循環
送風量だけを増やしただけでは生成水を除去しきれず、
電解液の希釈を回避できない。
(2) The generated water is generated even when the power generation temperature rises due to the load resistance. When the temperature of the fuel cell is low, the saturated steam pressure is low, and the amount of removed water that can be separated by the condenser is small. Can not completely remove the generated water,
The dilution of the electrolyte cannot be avoided.

(3)上記問題点(2)を回避するため、抵抗負荷に流
す電流を極端に小さくして生成水の発生量を抑制する方
法も知られているが、この方法では起動に要する時間が
長くなり、発電装置そのものの使い勝手が悪くなる。
(3) In order to avoid the above problem (2), a method is also known in which the amount of generated water is suppressed by extremely reducing the current flowing to the resistance load. However, this method requires a long time for starting. As a result, the usability of the power generator itself becomes poor.

この発明の目的は、凝縮器や送風機の能力を十分活用
して電解液の希釈を生ずることなく燃料電池を速やかに
昇温できる起動制御装置を得ることにある。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a start-up control device capable of quickly raising the temperature of a fuel cell without causing dilution of an electrolyte by sufficiently utilizing the capacity of a condenser or a blower.

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

上記課題を解決するために、この発明によれば、液体
電解質を満たした電解液室と、この電解液室を挟んでそ
の両側に対向して配された多孔質の燃料電極および酸化
剤電極と、両電極に反応ガスとしての水素および酸化剤
を給排する反応ガス室とを有する単位セル複数層の積層
体からなり、前記燃料電極側に反応ガスの強制循環路
と、この強制循環路に設けられ反応ガス中に含まれる発
電生成水を分離する凝縮器とを備えたものにおいて、燃
料電池の出力側に設けられた電流センサ、および可変抵
抗器,開閉器を有する短絡回路と、前記凝縮器入口,出
口の反応ガス温度の検出センサと、前記電流センサの検
出電流を含む所定の算式に基づいて得られる発電生成水
量と,前記一対の温度センサの検出温度に対応して得ら
れる前記凝縮器の除去水量と,この除去水量と等量の生
成水を生ずる電流値とを求め、得られた電流値を前記短
絡回路に流すよう前記可変抵抗器を制御する信号を検出
する演算制御部とを備えてなるものとする。
In order to solve the above-described problems, according to the present invention, an electrolyte chamber filled with a liquid electrolyte, a porous fuel electrode and an oxidant electrode disposed opposite to each other with the electrolyte chamber interposed therebetween A stacked body of a plurality of unit cells each having a reaction gas chamber for supplying and discharging hydrogen and an oxidant as a reaction gas to both electrodes, and a forced circulation path of the reaction gas on the fuel electrode side; A short circuit having a current sensor, a variable resistor, and a switch provided on the output side of the fuel cell; and a condenser for separating the power generation water contained in the reaction gas. Sensors for detecting the reaction gas temperatures at the inlet and outlet of the reactor, the amount of generated water generated based on a predetermined formula including the current detected by the current sensor, and the condensation obtained based on the temperatures detected by the pair of temperature sensors Vessel removal An arithmetic control unit for determining an amount and a current value that generates an amount of generated water equal to the amount of the removed water, and detecting a signal for controlling the variable resistor so that the obtained current value flows through the short circuit. It shall be.

〔作用〕[Action]

この発明の構成において、演算制御部が出力電流に比
例する発電生成水量と、凝縮器入口,出口の温度差に対
応する生成水の除去水量と、両者が互いに等しくなる電
流値とを求め、この電流値に基づいて短絡回路に流れる
電流を制御するよう構成したことにより、短絡回路に配
された可変抵抗器の消費電力に対応して生ずる生成水を
凝縮器の除去水量とが常にバランスするとともに、燃料
電池の温度が上昇するに伴って生成水の除去量も増加
し、かつこれに伴って可変抵抗の消費電力を増加させら
れるので、凝縮器およびこれに反応ガスを環流する送風
器の能力をフルに活用して燃料電池をその保管温度から
運転温度まで効率よく昇温させる機能が得られると同時
に、生成水によって液状電解質が希釈され、かつこれが
原因で燃料電池の発電性能が低下する事態を未然に防止
することができる。
In the configuration of the present invention, the arithmetic and control unit determines the amount of generated water generated in proportion to the output current, the amount of generated water removed corresponding to the temperature difference between the inlet and outlet of the condenser, and the current value in which both are equal to each other. By controlling the current flowing in the short circuit based on the current value, the generated water corresponding to the power consumption of the variable resistor arranged in the short circuit is always balanced with the amount of water removed from the condenser. As the temperature of the fuel cell increases, the amount of generated water removed also increases, and the power consumption of the variable resistor can be increased accordingly. Thus, the capacity of the condenser and the blower that circulates the reaction gas to the condenser is increased. In addition to the function of efficiently raising the temperature of the fuel cell from its storage temperature to the operating temperature, the liquid electrolyte is diluted by the generated water, and this causes the fuel cell to generate power. Ability can be prevented a situation to decrease.

〔実施例〕〔Example〕

以下この発明を実施例に基づいて説明する。 Hereinafter, the present invention will be described based on examples.

第1図はこの発明の実施例になる燃料電池発電装置を
示すシステムフロー図である。図において、1は液体電
解質型燃料電池であり、液体電解質を満たした電解液室
2と、この電解液室2を挟んでその両側に対向する多孔
質の水素電極3,酸化剤電極4と、各電極3,4の両側に例
えばリブ付きセパレート板で画成した水素室5、酸化剤
室6とで構成される。水素室5の入口には、図示されて
いない水素ガスボンベなどのガス源から引き出した燃料
ガス供給管路10が接続配管され、さらに、水素室5の出
口と入口の間にまたがり送風機11を介装した燃料ガス循
環路12が配管されており、この循環路12の水素室出口側
には凝縮器13が設置してある。なお、18は酸化剤室6に
接続配管した酸化剤例えば空気の供給管路、9は燃料電
池の冷却ファン、20は凝縮器13の冷却ファンである。
FIG. 1 is a system flow diagram showing a fuel cell power generator according to an embodiment of the present invention. In the figure, reference numeral 1 denotes a liquid electrolyte fuel cell, which includes an electrolyte chamber 2 filled with a liquid electrolyte, a porous hydrogen electrode 3 and an oxidant electrode 4 opposed to both sides of the electrolyte chamber 2 with the electrolyte chamber 2 interposed therebetween. A hydrogen chamber 5 and an oxidant chamber 6 are formed on both sides of each of the electrodes 3 and 4 by, for example, a ribbed separate plate. At the inlet of the hydrogen chamber 5, a fuel gas supply pipe 10 drawn from a gas source such as a hydrogen gas cylinder (not shown) is connected and connected. Further, a blower 11 is provided between the outlet and the inlet of the hydrogen chamber 5. A fuel gas circulation path 12 is provided, and a condenser 13 is installed on the hydrogen chamber outlet side of the circulation path 12. Reference numeral 18 denotes an oxidant, for example, an air supply pipe connected to the oxidant chamber 6, 9 denotes a cooling fan of the fuel cell, and 20 denotes a cooling fan of the condenser 13.

一方、燃料電池の出力回路7,8の極間には遮断スイッ
チ29,可変抵抗器30を含む短絡回路19が設けられてお
り、また燃料電池の電気出力回路には出力検出用の電流
センサ24が、さらに燃料ガス循環路12における循環器13
の前後には反応ガス温度を検出する温度センサ25,26を
備え、電流センサ24,温度センサ25,26の検出信号は演算
制御部27に入力され、短絡回路19側に配された可変抵抗
器30の抵抗値を制御する信号27Sを得るための演算が行
われる。すなわち、電流センサ24で検出された燃料電池
1の出力電流をI、燃料電池1における単位セルの積層
数をNとした場合、運転時に燃料電池1で生ずる生成水
の発生量V1はファラデーの法則に基づき次式で求められ
る。
On the other hand, a short circuit 19 including a cutoff switch 29 and a variable resistor 30 is provided between the poles of the output circuits 7 and 8 of the fuel cell, and a current sensor 24 for output detection is provided in the electric output circuit of the fuel cell. Circulator 13 in the fuel gas circuit 12
Before and after, temperature sensors 25 and 26 for detecting the reaction gas temperature are provided, and the detection signals of the current sensor 24 and the temperature sensors 25 and 26 are input to the arithmetic and control unit 27, and the variable resistor disposed on the short circuit 19 side. An operation for obtaining a signal 27S for controlling the resistance value of 30 is performed. That is, the output current of the fuel cell 1 detected by the current sensor 24 I, if the number of stacked unit cells in the fuel cell 1 is N, the generation amount V 1 of the product water generated by the fuel cell 1 during operation of the Faraday It is obtained by the following equation based on the law.

V1=I×(60/96480)×(18.02/2)×N ……(1) 一方、送風機11による水素の循環量をQ、そのモル数
をm、1モルの完全ガスの体積をV0、凝縮器出口におけ
る水蒸気の飽和度をKとした場合、飽和状態にある循環
ガス中の水蒸気分圧比(水蒸気分圧/水素分圧)は循環
ガスの温度に依存するので、凝縮器13で分離される生成
水の除去量V2は次式によって算出される。
V 1 = I × (60/96480) × (18.02 / 2) × N (1) On the other hand, the amount of hydrogen circulated by the blower 11 is Q, the number of moles thereof is m, and the volume of one mole of complete gas is V 0 , when the saturation of steam at the condenser outlet is K, the steam partial pressure ratio (steam partial pressure / hydrogen partial pressure) in the circulating gas in a saturated state depends on the temperature of the circulating gas. removal amount V 2 of produced water that is separated is calculated from the following equation.

したがって、演算制御部27が電流センサ24の検出信号
を受けて上記(1)式に基づいて生成水量V1を求めると
同時に、温度センサ25,26の検出温度に基づいて上記
(2)式の演算を行って除去水量V2を求め、かつ生成水
量V1と除去水量V2とが互いに等しくなるような電流Iを
算出して、この電流Iを短絡回路19に流すよう可変抵抗
器30の抵抗値を制御する信号27Sを出力することによ
り、起動時に燃料電池1で生じた生成水量V1と凝縮器13
で凝縮,分離される除去水量V2とが常にバランスした状
態で起動することができる。また、上記演算を所定の時
間間隔で繰り返し行い、更新された制御信号に基づいて
可変抵抗器30を制御するよう構成すれば、燃料電池1の
温度上昇および循環ガスの温度上昇に伴って演算結果は
徐々に上昇し、これに基づいて短絡回路19に流す電流も
徐々に増加するので、送風機による循環ガス量Qと凝縮
器の凝縮性能をフルに活用して、燃料電池を自己発熱に
よってその保管温度から運転温度に向けて最短時間で昇
温できる起動制御装置を得ることができる。
Therefore, simultaneously with the operation control unit 27 receives the detection signal of the current sensor 24 obtains the amount of produced water V 1 on the basis of the above (1), based on the temperature detected by the temperature sensor 25 and 26 (2) formula calculating the calculated removal amount of water V 2 go, and with a water quantity V 1 and removing water V 2 is calculated equal such currents I together, in the variable resistor 30 to flow the current I to the short circuit 19 by outputting a signal 27S for controlling the resistance value, the amount of produced water V 1 generated in the fuel cell 1 during startup condenser 13
In the condensation, it can be started in a state where the amount of water removed V 2 to be separated is always balanced. Further, if the above calculation is repeatedly performed at predetermined time intervals and the variable resistor 30 is controlled based on the updated control signal, the calculation result is increased in accordance with the temperature rise of the fuel cell 1 and the temperature of the circulating gas. Gradually rises, and the current flowing through the short circuit 19 gradually increases based on this. Therefore, the fuel cell is stored by self-heating by making full use of the circulation gas amount Q by the blower and the condensation performance of the condenser. It is possible to obtain a startup control device capable of raising the temperature from the temperature to the operating temperature in the shortest time.

なお、短絡回路19の開閉器29は、演算制御部27が発す
る起動指令信号によって閉路し、燃料電池1が所定の運
転温度に到達した時点で発する起動の終了信号によって
開路するよう構成される。
The switch 29 of the short circuit 19 is configured to be closed by a start command signal generated by the arithmetic control unit 27 and to be opened by a start end signal generated when the fuel cell 1 reaches a predetermined operating temperature.

上述の実施例になる起動制御装置を設けたことによ
り、燃料電池の温度条件に対応して、生成水発生量と電
池外部に排出する生成水除去量とを常にバランスさせな
がら自己発熱により昇温するので、起動・停止回数に関
係なく、電解液濃度を一定に維持することが可能にな
り、したがって生成水が電解液を希釈することによって
生ずる燃料電池の発電性能の低下をほぼ完全に回避する
ことができる。
By providing the start-up control device according to the above-described embodiment, the temperature rises due to self-heating while always balancing the amount of generated water and the amount of generated water removed to the outside of the cell in accordance with the temperature condition of the fuel cell. Therefore, it is possible to maintain the concentration of the electrolyte constant regardless of the number of times of starting / stopping, and therefore, it is possible to almost completely avoid a decrease in the power generation performance of the fuel cell caused by diluting the electrolyte with the produced water. be able to.

また、燃料電池の生成水量と凝縮器の除去水量とがほ
ぼ一致するよう、ガス循環路の循環ガス量を制御する従
来方式とは異なり、短絡回路に流す電流を制御すること
によって生成水量そのものを除去水量に対応して制御す
るので、電解質溶液の濃度管理を精度よく行えるととも
に、(2)式において凝縮器出口側の水蒸気の飽和度K
の選択の仕方によって電解質溶液の濃度そのものを制御
することが可能になるという利点も得られる。
Also, unlike the conventional method of controlling the amount of circulating gas in the gas circulation path so that the amount of water generated by the fuel cell and the amount of water removed by the condenser substantially match, the amount of generated water itself is controlled by controlling the current flowing through the short circuit. Since the control is performed in accordance with the amount of water removed, the concentration of the electrolyte solution can be controlled with high accuracy.
There is also an advantage that it becomes possible to control the concentration of the electrolyte solution itself by the method of selecting.

〔発明の効果〕〔The invention's effect〕

この発明は前述のように、電流センサおよび温度セン
サの検出信号に基づき、演算制御部が凝縮器による除去
水量と等価な生成水を生ずる電流値を求め、短絡回路に
流す電流値を計算結果に基づいて制御する信号を可変抵
抗器に向けて出力するよう構成した。その結果、燃料電
池の起動時における生成水の発生量と凝縮器による除去
水量とを常にバランスさせながら自己発熱により燃料電
池をその保管温度から運転温度に向けて昇温できるとと
もに、温度上昇とともに増加する除去水量に見合って電
流値を増すよう制御することが可能になり、凝縮器およ
び循環送風機の能力をフルに活用して電池の昇温を効率
よく,かつ生成水により液体電解質の希釈を生ずること
なく行える起動制御装置を備えた液体電解質型燃料電池
を提供することができる。
According to the present invention, as described above, based on the detection signals of the current sensor and the temperature sensor, the arithmetic and control unit obtains a current value that generates water equivalent to the amount of water removed by the condenser, and calculates a current value flowing through the short circuit as a calculation result. A control signal is output to the variable resistor. As a result, it is possible to raise the temperature of the fuel cell from its storage temperature to the operating temperature by self-heating while always balancing the amount of generated water at the time of starting the fuel cell and the amount of water removed by the condenser, and increase as the temperature rises It is possible to control to increase the current value in accordance with the amount of water to be removed, to make full use of the capacity of the condenser and the circulating blower to efficiently raise the temperature of the battery, and to dilute the liquid electrolyte with the generated water. It is possible to provide a liquid electrolyte fuel cell provided with a start-up control device that can be performed without any problem.

また、生成水量と除去水量とがほぼ一致するよう、反
応ガスの循環量を制御する従来技術において問題となっ
た起動初期の低温時における生成水の悪影響も、生成と
除去を常にバランスさせるこの発明によってほぼ完全に
回避することができる。さらに、燃料電池に電気ヒータ
を埋設し、バッテリー電源から電力を供給して燃料電池
を加温する従来技術に比べ、この発明は自己発熱によっ
て加温を行うために内蔵電気ヒータやバッテリー電源な
どの機器を必要とせず、したがって装置の構成を簡素化
できるとともに、バッテリーの充電作業などを必要とし
ないので保守管理を容易化でき、かつ起動,停止の繰り
返しに関わりなく短時間で昇温できるので使い勝手がよ
いなどの利点が得られる。
In addition, the adverse effect of generated water at the time of low temperature at the beginning of start-up, which has been a problem in the prior art for controlling the circulation amount of the reaction gas so that the generated water amount and the removed water amount substantially match, always balances generation and removal. Can be avoided almost completely. Furthermore, in comparison with the conventional technology in which an electric heater is embedded in a fuel cell and power is supplied from a battery power source to heat the fuel cell, the present invention uses a built-in electric heater and a battery power source to perform heating by self-heating. No equipment is required, so the structure of the device can be simplified, and maintenance work can be simplified because there is no need to charge the battery, and the temperature can be raised in a short time regardless of the repeated start and stop operations. And other advantages.

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

第1図はこの発明の実施例になる液体電解質型燃料電池
の起動制御装置を簡略化して示すシステムフロー図であ
る。 1:燃料電池、2:電解液室、3,4:電極、5,6:反応ガス室、
7,8:出力回路、9,11,20:送風機、10,18:反応ガスの供給
系、12:ガス循環路、13:凝縮器、19:短絡回路、24:電流
センサ、25,26:温度センサ、27:演算制御部、29:開閉
器、30:可変抵抗器、27S:制御信号、I:出力電流。
FIG. 1 is a simplified system flow diagram showing a startup control device for a liquid electrolyte fuel cell according to an embodiment of the present invention. 1: fuel cell, 2: electrolyte chamber, 3, 4: electrode, 5, 6: reaction gas chamber,
7, 8: output circuit, 9, 11, 20: blower, 10, 18: reaction gas supply system, 12: gas circulation path, 13: condenser, 19: short circuit, 24: current sensor, 25, 26: Temperature sensor, 27: arithmetic control unit, 29: switch, 30: variable resistor, 27S: control signal, I: output current.

フロントページの続き (72)発明者 新田 晃 大阪府大阪市淀川区田川2丁目1番11号 株式会社ダイヘン内 (58)調査した分野(Int.Cl.6,DB名) H01M 8/00 - 8/24Continuation of the front page (72) Inventor Akira Nitta 2-1-1-11 Tagawa, Yodogawa-ku, Osaka-shi, Osaka Daihen Co., Ltd. (58) Field surveyed (Int. Cl. 6 , DB name) H01M 8/00- 8/24

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】液体電解質を満たした電解液室と、この電
解液室を挟んでその両側に対向して配された多孔質の燃
料電極および酸化剤電極と、両電極に反応ガスとしての
水素および酸化剤を給排する反応ガス室とを有する単位
セル複数層の積層体からなり、前記燃料電極側に反応ガ
スの強制循環路と、この強制循環路に設けられ反応ガス
中に含まれる発電生成水を分離する凝縮器とを備えたも
のにおいて、燃料電池の出力側に設けられた電流セン
サ、および可変抵抗器,開閉器を有する短絡回路と、前
記凝縮器入口,出口の反応ガス温度の検出センサと、前
記電流センサの検出電流を含む所定の算式に基づいて得
られる発電生成水量と,前記一対の温度センサの検出温
度に対応して得られる前記凝縮器の除去水量と,この除
去水量と等量の生成水を生ずる電流値とを求め、得られ
た電流値を前記短絡回路に流すよう前記可変抵抗器を制
御する信号を検出する演算制御部とを備えてなることを
特徴とする液体電解質型燃料電池の起動制御装置。
An electrolyte chamber filled with a liquid electrolyte, a porous fuel electrode and an oxidant electrode disposed on opposite sides of the electrolyte chamber, and hydrogen as a reaction gas And a reaction gas chamber for supplying and discharging an oxidant. The reaction cell chamber is composed of a plurality of unit cells each having a reaction gas chamber for supplying and discharging an oxidant. A condenser for separating generated water, a current sensor provided on the output side of the fuel cell, a short circuit having a variable resistor and a switch, and a reaction gas temperature at the inlet and outlet of the condenser. A detection sensor, an amount of generated water generated based on a predetermined formula including a current detected by the current sensor, an amount of water removed from the condenser obtained in accordance with a temperature detected by the pair of temperature sensors, and an amount of water removed from the condenser. Generating Equivalents And a calculation control unit for detecting a signal for controlling the variable resistor so that the obtained current value flows through the short circuit. Startup control device.
JP2235121A 1990-09-05 1990-09-05 Startup control device for liquid electrolyte fuel cell Expired - Lifetime JP2815690B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2235121A JP2815690B2 (en) 1990-09-05 1990-09-05 Startup control device for liquid electrolyte fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2235121A JP2815690B2 (en) 1990-09-05 1990-09-05 Startup control device for liquid electrolyte fuel cell

Publications (2)

Publication Number Publication Date
JPH04115468A JPH04115468A (en) 1992-04-16
JP2815690B2 true JP2815690B2 (en) 1998-10-27

Family

ID=16981366

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2235121A Expired - Lifetime JP2815690B2 (en) 1990-09-05 1990-09-05 Startup control device for liquid electrolyte fuel cell

Country Status (1)

Country Link
JP (1) JP2815690B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100813247B1 (en) 2006-10-17 2008-03-13 삼성에스디아이 주식회사 Fuel cell system and its operation method

Families Citing this family (4)

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Publication number Priority date Publication date Assignee Title
JP3772826B2 (en) * 2002-11-18 2006-05-10 日本電気株式会社 FUEL CELL SYSTEM, PORTABLE ELECTRIC DEVICE USING FUEL CELL, AND METHOD OF OPERATING FUEL CELL
JP4799827B2 (en) * 2004-03-30 2011-10-26 アイシン精機株式会社 Fuel cell system
JP5407235B2 (en) * 2008-09-11 2014-02-05 パナソニック株式会社 Fuel cell system and control method thereof
JP6969998B2 (en) * 2017-12-12 2021-11-24 株式会社東芝 Hydrogen power storage system and hydrogen power storage method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100813247B1 (en) 2006-10-17 2008-03-13 삼성에스디아이 주식회사 Fuel cell system and its operation method

Also Published As

Publication number Publication date
JPH04115468A (en) 1992-04-16

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