JPH088109B2 - Molten carbonate fuel cell - Google Patents

Molten carbonate fuel cell

Info

Publication number
JPH088109B2
JPH088109B2 JP63296182A JP29618288A JPH088109B2 JP H088109 B2 JPH088109 B2 JP H088109B2 JP 63296182 A JP63296182 A JP 63296182A JP 29618288 A JP29618288 A JP 29618288A JP H088109 B2 JPH088109 B2 JP H088109B2
Authority
JP
Japan
Prior art keywords
electrolyte
fuel cell
battery
control valve
carbonate
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 - Fee Related
Application number
JP63296182A
Other languages
Japanese (ja)
Other versions
JPH02144856A (en
Inventor
正義 伊勢
陽一 川田
俊樹 加原
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP63296182A priority Critical patent/JPH088109B2/en
Publication of JPH02144856A publication Critical patent/JPH02144856A/en
Publication of JPH088109B2 publication Critical patent/JPH088109B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • H01M8/04276Arrangements for managing the electrolyte stream, e.g. heat exchange
    • H01M8/04283Supply means of electrolyte to or in matrix-fuel cells
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/14Fuel cells with fused electrolytes
    • H01M2008/147Fuel cells with molten carbonates
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0017Non-aqueous electrolytes
    • H01M2300/0048Molten electrolytes used at high temperature
    • H01M2300/0051Carbonates
    • 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

  • Fuel Cell (AREA)
  • 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)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、溶融炭酸塩型燃料電池に係り、特に高積層
化された電解質板に発電を停止することなく、均一に適
量の電解質を供給するのに好適な溶融炭酸塩型燃料電池
に関する。
Description: TECHNICAL FIELD The present invention relates to a molten carbonate fuel cell, and in particular, supplies an appropriate amount of electrolyte to a highly laminated electrolyte plate without stopping power generation. The present invention relates to a molten carbonate fuel cell suitable for

〔従来の技術〕[Conventional technology]

従来の溶融炭酸塩型の燃料電池の寿命は、数千時間程
度であり、寿命延長の為には、発電を停止して電解質の
交換や、電解質板側面より電解質を注入する方法がとら
れているが、いずれも発電運転を停止して、ガスマニホ
ールド等の分解が要求されるという欠点があった。
The life of the conventional molten carbonate type fuel cell is about several thousand hours, and in order to extend the life, the method of stopping the power generation, replacing the electrolyte, or injecting the electrolyte from the side of the electrolyte plate has been adopted. However, all of them had a drawback that the power generation operation was stopped and the gas manifold and the like had to be disassembled.

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

本発明の目的は、電池の発電運転を停止してガスマニ
ホールド等の分解をすることなく、運転中に電解質板に
溶融炭酸塩電解質を効率的に補充できる、稼働率の高
い、長寿命の溶融炭酸塩型燃料電池を提供することにあ
る。また、運転中の溶融炭酸塩電解質の補充を自動化す
ることにある。
An object of the present invention is to efficiently replenish the molten carbonate electrolyte to the electrolyte plate during operation without stopping the power generation operation of the battery and disassembling the gas manifold etc., high operating rate, long-life melting It is to provide a carbonate fuel cell. Another object is to automate replenishment of molten carbonate electrolyte during operation.

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

上記目的は、陰電極、電解質板、陽電極、セパレータ
を上下に積層した電池本体を含む溶融炭酸塩型燃料電池
において、炭酸塩電解質を貯蔵する炭酸塩タンクと、チ
タン系あるいはステンレン系の耐熱、耐食性の金属管と
該金属管の外面に焼結した電気絶縁性の高いセラミック
ス層からなり電池本体の電極と接しない電解質板の四隅
に上下に貫通させて配置された側面に多数の細孔を有す
る複数個の絶縁管と、前記炭酸塩タンクと前記複数個の
絶縁管を接続する電解質供給配管と、前記電解質供給配
管に設けられた制御弁とを備え、運転中に前記制御弁を
開くことで前記絶縁管の細孔を経由して炭酸塩電解質を
電池本体の電解質板に補充する機能を有することにより
達成される。
The above-mentioned object is a molten carbonate fuel cell including a negative electrode, an electrolyte plate, a positive electrode, and a battery body in which separators are stacked one above the other, a carbonate tank for storing a carbonate electrolyte, and a titanium-based or stainless steel heat-resistant material. A large number of pores are formed on the side surfaces vertically arranged at the four corners of the electrolyte plate that is made of a corrosion-resistant metal tube and a ceramic layer with high electrical insulation that is sintered on the outer surface of the metal tube and that does not contact the electrodes of the battery body. A plurality of insulating pipes having, an electrolyte supply pipe connecting the carbonate tank and the plurality of insulating pipes, and a control valve provided in the electrolyte supply pipe, and opening the control valve during operation It is achieved by having the function of replenishing the carbonate electrolyte to the electrolyte plate of the battery main body through the pores of the insulating tube.

電解質供給配管には、電気あるいは燃料電池の反応熱
により加熱する加熱器を配備するのが好ましい。
It is preferable to provide a heater for heating the electrolyte supply pipe with electricity or reaction heat of the fuel cell.

また、上記運転中の溶融炭酸塩電解質の補充の自動化
は、電池本体の出力電圧を検知する電圧計と制御装置と
を更に備え、制御装置は電圧計によって検知された電池
出力電圧を電解質板の劣化を示す閾値と比較して閾値よ
り低いとき制御弁を開け、出力電圧が回復すれば制御弁
を閉じる制御を行うことにより達成される。
Further, the automation of the replenishment of the molten carbonate electrolyte during the operation is further provided with a voltmeter and a control device for detecting the output voltage of the battery body, and the control device controls the battery output voltage detected by the voltmeter to the electrolyte plate. This is achieved by performing control such that the control valve is opened when it is lower than the threshold value as compared with the threshold value indicating deterioration and the control valve is closed when the output voltage is restored.

〔作用〕[Action]

電池を運転中に、分解することなく電池性能低下に対
応して、電解質を外部より自動的に供給するために、電
池出力電圧を電圧計で検知し、所要の電圧以下になると
電池外部の電解質タンクより供給制御弁を自動開閉し、
電池への供給配管を通して電池内に電解質を供給できる
構造とし、電池内には、チタン系又はステンレス系の金
属管に電気絶縁性の高いセラミックスを外面を焼結し、
多数の細孔を有する電解質供給管を通して、電解質板へ
適量の電解質を補充することができる。それによって電
池性能が回復し、長時間に渡って、所要の性能で電池を
運転することができる。
The battery output voltage is detected by a voltmeter in order to automatically supply the electrolyte from the outside without disassembling it while the battery is operating, and the electrolyte outside the battery is detected when the voltage falls below the required voltage. Automatically open and close the supply control valve from the tank,
An electrolyte can be supplied into the battery through a supply pipe to the battery.In the battery, a titanium-based or stainless-based metal tube is sintered on the outer surface of highly electrically insulating ceramics,
The electrolyte plate can be replenished with an appropriate amount of electrolyte through an electrolyte supply pipe having a large number of pores. As a result, the battery performance is restored, and the battery can be operated with the required performance for a long time.

〔実施例〕〔Example〕

以下、本発明の実施例を第1図、2図により説明す
る。第1図の実施例においては、電池本体1は、陰電極
5、陽電極6、電解質板2、セパレータ3、電解質供給
管4で構成される。第2図は、第1図のA−A断面を示
し、電解質供給管4は、耐食管9と絶縁体8で構成さ
れ、電解質供給用の細孔部10を有している。これにより
電池の発電中においても、電池外部より電解質供給管4
に、炭酸塩電解質7を送給することにより、電解質7が
管の細孔部10より、電解質板2に供給される。
An embodiment of the present invention will be described below with reference to FIGS. In the embodiment shown in FIG. 1, the battery body 1 is composed of a negative electrode 5, a positive electrode 6, an electrolyte plate 2, a separator 3 and an electrolyte supply pipe 4. FIG. 2 shows a cross section taken along the line AA in FIG. 1. The electrolyte supply pipe 4 is composed of a corrosion resistant pipe 9 and an insulator 8, and has a pore portion 10 for electrolyte supply. This allows the electrolyte supply pipe 4 to be supplied from the outside of the battery even during power generation of the battery.
Then, by feeding the carbonate electrolyte 7, the electrolyte 7 is supplied to the electrolyte plate 2 through the pores 10 of the tube.

第3図は炭酸塩電解質の供給制御系統を示し、電池本
体1の出力電圧を電圧計12で計測し、出力電圧のしきい
値より低い電圧低下が検知された場合、制御装置11を介
し、制御弁13を開け、適量の電解質が炭酸塩タンク15よ
り供給配管14を通り、電池本体1の電解質板に供給され
ることを示している。又電圧値が回復すれば、制御装置
11よりの信号で、制御弁13が閉じ効率的な自動供給を行
うことができる。
FIG. 3 shows a carbonate electrolyte supply control system, in which the output voltage of the battery main body 1 is measured by the voltmeter 12, and when a voltage drop lower than the threshold value of the output voltage is detected, through the control device 11, The control valve 13 is opened to show that an appropriate amount of electrolyte is supplied from the carbonate tank 15 through the supply pipe 14 to the electrolyte plate of the battery body 1. If the voltage value recovers, the control device
With the signal from 11, the control valve 13 is closed and efficient automatic supply can be performed.

電解質板は、リチウムアルミネート系のセラミック基
板を用いており、電解質7は、炭酸リチウムと炭酸カリ
ウムの混合塩で、電池の運転温度650℃で、よく液化
し、多数の細孔部10よりの供給性もよい。電解質供給管
4は、電極と接しない電解質板2の四隅に各1本ずつ配
置する方が良いことを実験で確かめている。供給管4の
材質は、ステンレス又はチタン系の管外面に炭化ケイ素
又は、リチウムアルミネート系の電気絶縁性の高いセラ
ミックを焼結したものを用いた。多数の細孔部10は、レ
ーザ加工等で0.3〜2.0mmの径の孔を多数設けた。電解質
のタンク15及び配管14の材質はグラスファイバー系の樹
脂を用いた。電解質の供給は、重力を利用した自然落下
法や、チッ素又は二酸化炭素を利用したガス圧送法、又
はポンプによる機械式圧送法がある。尚、電解質7の移
送を容易にする為、配管系14の途中に電気又は、電池反
応熱による加熱器16を設け、液化を進行させた。なお1
個の電解質タンク15から多数の電池に並列供給を実施す
ることも可能である。
The electrolyte plate uses a lithium aluminate-based ceramic substrate, and the electrolyte 7 is a mixed salt of lithium carbonate and potassium carbonate, which is well liquefied at a battery operating temperature of 650 ° C. Good supply. Experiments have confirmed that it is better to dispose one electrolyte supply tube 4 at each of the four corners of the electrolyte plate 2 that is not in contact with the electrodes. As the material of the supply pipe 4, a material obtained by sintering silicon carbide or a lithium aluminate-based ceramic having a high electric insulation property on the outer surface of a stainless steel or titanium base was used. A large number of pores 10 having a diameter of 0.3 to 2.0 mm were provided by laser processing or the like. As the material of the electrolyte tank 15 and the pipe 14, a glass fiber resin was used. The electrolyte can be supplied by gravity dropping using gravity, gas pressure feeding using nitrogen or carbon dioxide, or mechanical pressure feeding using a pump. In order to facilitate transfer of the electrolyte 7, a heater 16 by electricity or the heat of battery reaction was provided in the middle of the piping system 14 to promote liquefaction. 1
It is also possible to carry out parallel supply from a single electrolyte tank 15 to a large number of batteries.

〔発明の効果〕〔The invention's effect〕

本発明によれば、電池寿命が従来の数千時間程度から
数万時間程度まで延長できる効果がある。又電解質の補
充も、発電を停止することなく、実施可能となり、発電
所の運用上の効果が得られる。又自動供給装置により、
電池本体の分解も不要となり、メンテナンス経済性も向
上する効果がある。
According to the present invention, there is an effect that the battery life can be extended from the conventional thousands of hours to tens of thousands hours. Further, the electrolyte can be replenished without stopping the power generation, and the operational effect of the power plant can be obtained. Also, with the automatic feeder,
There is no need to disassemble the battery body, and maintenance efficiency is improved.

又、電解質供給用の絶縁管自体が、電池本体の高積層
時のガイド棒となり、積層組立作業を容易に実施でき、
側面の凹凸もなくなり、燃料ガスマニホールド取付面の
気密性も向上する効果がある。
In addition, the insulation tube itself for supplying the electrolyte serves as a guide rod for high stacking of the battery main body, which facilitates stacking and assembling work.
The unevenness on the side surface is also eliminated, and the airtightness of the mounting surface of the fuel gas manifold is improved.

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

第1図は、燃料電池本体の外形図、第2図は、第1図の
A−A線断面図、第3図は、炭酸塩電解質供給制御系統
図である。 1……燃料電池本体、2……電解質板、3……セパレー
タ、4……電解質供給管、5……陰電極、6……陽電
極、7……炭酸塩電解質、8……絶縁体、9……耐触
管、10……多数の細孔部、11……制御装置、12……電圧
計、13……制御弁、14……炭酸塩の供給配管、15……炭
酸塩タンク、16……加熱器。
1 is an external view of the fuel cell main body, FIG. 2 is a sectional view taken along the line AA of FIG. 1, and FIG. 3 is a carbonate electrolyte supply control system diagram. 1 ... Fuel cell main body, 2 ... Electrolyte plate, 3 ... Separator, 4 ... Electrolyte supply tube, 5 ... Negative electrode, 6 ... Positive electrode, 7 ... Carbonate electrolyte, 8 ... Insulator, 9 ... Corrosion resistant tube, 10 ... Many pores, 11 ... Control device, 12 ... Voltmeter, 13 ... Control valve, 14 ... Carbonate supply pipe, 15 ... Carbonate tank, 16 ... Heater.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】陰電極、電解質板、陽電極、セパレータを
上下に積層した電池本体を含む溶融炭酸塩型燃料電池に
おいて、 炭酸塩電解質を貯蔵する炭酸塩タンクと、チタン系ある
いはステンレス系の金属管と該金属管の外面に焼結した
電気絶縁性の高いセラミックス層からなり電池本体の電
極と接しない電解質板の四隅に上下に貫通させて配置さ
れた側面に多数の細孔を有する複数個の絶縁管と、前記
炭酸塩タンクと前記複数個の絶縁管を接続する電解質供
給配管と、前記電解質供給配管に設けられた制御弁とを
備え、運転中に前記制御弁を開くことで前記絶縁管の細
孔を経由して炭酸塩電解質を電池本体の電解質板に補充
する機能を有することを特徴とする溶融炭酸塩型燃料電
池。
1. A molten carbonate fuel cell comprising a battery body in which a negative electrode, an electrolyte plate, a positive electrode, and a separator are stacked one above the other in a molten carbonate fuel cell, and a carbonate tank for storing a carbonate electrolyte and a titanium-based or stainless-based metal. A plurality of holes having a large number of pores on the side surfaces vertically arranged at the four corners of the electrolyte plate which is made of a ceramic tube and a ceramic layer having a high electrical insulation property which is sintered on the outer surface of the metal tube and which does not contact the electrodes of the battery body. Insulation pipe, an electrolyte supply pipe connecting the carbonate tank and the plurality of insulation pipes, and a control valve provided in the electrolyte supply pipe, and the insulation is provided by opening the control valve during operation. A molten carbonate fuel cell, which has a function of replenishing a carbonate electrolyte to an electrolyte plate of a battery main body through pores of a tube.
【請求項2】電池本体の出力電圧を検知する電圧計と制
御装置とを更に備え、前記制御装置は前記電圧計によっ
て検知された電池出力電圧が電解質板の劣化を示すしき
い値より低いとき前記制御弁を開け、しきい値より高い
とき前記制御弁を閉じる制御を行うものであることを特
徴とする請求項1記載の溶融炭酸塩型燃料電池。
2. A voltmeter for detecting the output voltage of the battery body and a control device, wherein the control device is provided when the battery output voltage detected by the voltmeter is lower than a threshold value indicating deterioration of the electrolyte plate. 2. The molten carbonate fuel cell according to claim 1, wherein the control valve is opened and the control valve is closed when the control valve is higher than a threshold value.
JP63296182A 1988-11-25 1988-11-25 Molten carbonate fuel cell Expired - Fee Related JPH088109B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63296182A JPH088109B2 (en) 1988-11-25 1988-11-25 Molten carbonate fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63296182A JPH088109B2 (en) 1988-11-25 1988-11-25 Molten carbonate fuel cell

Publications (2)

Publication Number Publication Date
JPH02144856A JPH02144856A (en) 1990-06-04
JPH088109B2 true JPH088109B2 (en) 1996-01-29

Family

ID=17830227

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63296182A Expired - Fee Related JPH088109B2 (en) 1988-11-25 1988-11-25 Molten carbonate fuel cell

Country Status (1)

Country Link
JP (1) JPH088109B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101256072B1 (en) * 2011-04-25 2013-04-18 삼성에스디아이 주식회사 Fuel cell stack

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5433473A (en) * 1991-04-26 1995-07-18 Toyoda Gosei Co., Ltd. Pad mounting structure for air bag device
US7939219B2 (en) 2005-05-27 2011-05-10 Fuelcell Energy, Inc. Carbonate fuel cell and components thereof for in-situ delayed addition of carbonate electrolyte

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61214367A (en) * 1985-03-19 1986-09-24 Ishikawajima Harima Heavy Ind Co Ltd Carbonate supply method for fuel cell
JPH0416378Y2 (en) * 1986-02-05 1992-04-13

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101256072B1 (en) * 2011-04-25 2013-04-18 삼성에스디아이 주식회사 Fuel cell stack
US9653741B2 (en) 2011-04-25 2017-05-16 Samsung Sdi Co., Ltd. Fuel cell stack

Also Published As

Publication number Publication date
JPH02144856A (en) 1990-06-04

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