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JPH0565991B2 - - Google Patents
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JPH0565991B2 - - Google Patents

Info

Publication number
JPH0565991B2
JPH0565991B2 JP61135925A JP13592586A JPH0565991B2 JP H0565991 B2 JPH0565991 B2 JP H0565991B2 JP 61135925 A JP61135925 A JP 61135925A JP 13592586 A JP13592586 A JP 13592586A JP H0565991 B2 JPH0565991 B2 JP H0565991B2
Authority
JP
Japan
Prior art keywords
plate
electrolyte
separator
fuel cell
flange
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
JP61135925A
Other languages
Japanese (ja)
Other versions
JPS62295359A (en
Inventor
Hajime Toritani
Akio Soma
Keizo Ootsuka
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 JP61135925A priority Critical patent/JPS62295359A/en
Publication of JPS62295359A publication Critical patent/JPS62295359A/en
Publication of JPH0565991B2 publication Critical patent/JPH0565991B2/ja
Granted 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
    • H01M8/02Details
    • H01M8/0289Means for holding the electrolyte
    • H01M8/0295Matrices for immobilising electrolyte melts
    • 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〕 本発明は、燃料電池に係り、特に溶融炭酸塩型
燃料電池の電解質板の熱応力強度を向上させるこ
とのできる燃料電池に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a fuel cell, and more particularly to a fuel cell capable of improving the thermal stress strength of an electrolyte plate of a molten carbonate fuel cell.

〔発明の技術的背景および従来技術〕[Technical background of the invention and prior art]

従来の溶融炭酸塩型燃料電池は、特開昭57−
154766号に記載のものがあり、これを第2図乃至
第6図に示す。
The conventional molten carbonate fuel cell
There is one described in No. 154766, which is shown in FIGS. 2 to 6.

燃料電池の単位セルは、通常第2図に示すよう
な構成からなり、この単位セルが複数個積層され
て燃料電池を構成する。ここに示されている単位
セルは、電解質板1を境にして両側に多孔質体で
形成され触媒が付加されてなる電極板(アノード
2およびカソード3)が配置され、さらに両電極
板の背面にアノード2に燃料を供給する複数の平
行に設けられたリブによつて形成された流路溝5
およびカソード3に酸化剤ガスを供給する複数の
平行に設けられたリブによつて形成された酸化剤
流路溝6を有するセパレータ板4が積層され構成
されている。第3図には、第2図に示される単位
セルの断面図を示されている。図において、セパ
レータ4と電解質板1との間にウエツトシール7
が介挿されている。これは、セル内部に流れるガ
スをシールするためである。
A unit cell of a fuel cell usually has a structure as shown in FIG. 2, and a plurality of these unit cells are stacked to form a fuel cell. The unit cell shown here has electrode plates (anode 2 and cathode 3) made of a porous material and to which a catalyst is added on both sides of an electrolyte plate 1 as a boundary, and further has electrode plates (anode 2 and cathode 3) on both sides of the electrolyte plate 1 as a boundary, and a rear surface of both electrode plates. A channel groove 5 formed by a plurality of parallel ribs that supplies fuel to the anode 2.
A separator plate 4 having an oxidant passage groove 6 formed by a plurality of parallel ribs for supplying an oxidant gas to the cathode 3 is laminated. FIG. 3 shows a cross-sectional view of the unit cell shown in FIG. 2. In the figure, there is a wet seal 7 between the separator 4 and the electrolyte plate 1.
is inserted. This is to seal the gas flowing inside the cell.

上記構成よりなる装置において、電解質板1の
材料としてリチウムアルミネート粉末(LiAlO2
半分)に補強剤としてアルミナ繊維等を混入した
多孔質セラミツクス板等が用いられ、電解質とし
ては、Li2Co3,K2CO3,NaCO3等の炭酸塩の混
合物が使用され、これらを電解質板の内部に含浸
させている。この電解質は室温状態では固定であ
るが約490℃以上になると溶融し、電極とセパレ
ータ溝との境界面に流出して化学反応を起し発電
する。また、電極材として、アノード側にNi多
孔質燃結体、カソード側にNiO多孔質体を使用
し、セパレータ板の材質としては、オーステナイ
トステンレス鋼、例えばSUS316,SUS304,
SUS310,SUS446等の高温耐腐食材料が用いら
れていた。アノード側では水素による還元反応が
発生し、カソード側では空気中の酸素による酸化
反応がアルカリ雰囲気中で発生するため、耐食性
のあるオーステナイト鋼が適しているからであ
る。
In the device having the above configuration, lithium aluminate powder (LiAlO 2
A porous ceramic plate mixed with alumina fiber etc. is used as a reinforcing agent in the half), and a mixture of carbonates such as Li 2 Co 3 , K 2 CO 3 , NaCO 3 etc. is used as the electrolyte. It is impregnated inside the board. This electrolyte is fixed at room temperature, but when the temperature exceeds approximately 490°C, it melts and flows to the interface between the electrode and separator groove, causing a chemical reaction and generating electricity. In addition, as electrode materials, Ni porous combusted material is used on the anode side and NiO porous material is used on the cathode side, and the material of the separator plate is austenitic stainless steel, such as SUS316, SUS304,
High-temperature corrosion-resistant materials such as SUS310 and SUS446 were used. This is because a reduction reaction due to hydrogen occurs on the anode side, and an oxidation reaction due to oxygen in the air occurs on the cathode side in an alkaline atmosphere, so austenitic steel with corrosion resistance is suitable.

上記構成材料等からなる単位セルは、反応性能
向上および外部へのガスの流出を防止するため一
定荷重により圧縮された状態で積層されている。
さらにこの圧縮積層は、電極2において反応によ
る電気が発生するため、電極2とセパレータ4間
の電気抵抗の関係で密着性がよいほど性能がよく
なる。
The unit cells made of the above-mentioned constituent materials are stacked in a compressed state under a constant load in order to improve reaction performance and prevent gas from flowing out.
Furthermore, in this compressed lamination, since electricity is generated by a reaction at the electrode 2, the better the adhesion, the better the performance in terms of the electrical resistance between the electrode 2 and the separator 4.

第4図aには、電池の起動停止時における温度
特性が示されている。発電前にセルの温度は定格
温度まで上昇させられ、その後燃料および酸化剤
ガスを流入して発電させる。停止時にはガス停止
後セル温度を降下させるようにしている。
FIG. 4a shows the temperature characteristics when the battery starts and stops. Before power generation, the temperature of the cell is raised to the rated temperature, and then fuel and oxidizer gas are introduced to generate power. When the system is stopped, the cell temperature is lowered after the gas is stopped.

従来、燃料電池は火力発電設備の代替として有
望であり、国内においては原子力発電設備をベー
ス負荷運用とし、燃料電池は日負荷運用として用
いられることが予想される。
Conventionally, fuel cells have been promising as a replacement for thermal power generation equipment, and in Japan, it is expected that nuclear power generation equipment will be used for base load operation and fuel cells will be used for daily load operation.

したがつて、燃料電池は起動、停止の激しい運
転に耐え得るヒートサイクル性に優れていること
が必要条件となる。
Therefore, it is necessary for the fuel cell to have excellent heat cycle properties that can withstand operation with frequent startup and shutdown operations.

また、第4図bには燃料電池内部の起動、停止
時の各部の熱伸び変化が示されている。起動時の
温度上昇と共に電池のセパレータ板と、電解質板
は夫々伸びδSおよびδEを発生するが、セパレータ
板の伸び量δSは電解質板の伸び量δEよりも大きく
なることを示している。これは、第5図の線膨張
特性からもわかるように電解質板よりもセパレー
タ板の線膨張係数が大きいことに起因する。第6
図a,bは、電池本体の伸び状況を平面および側
面よりみた概略図である。
Further, FIG. 4b shows changes in thermal elongation of various parts inside the fuel cell during startup and shutdown. As the temperature rises during startup, the separator plate and electrolyte plate of the battery elongate δ S and δ E , respectively, but the amount of elongation δ S of the separator plate is larger than the amount of elongation δ E of the electrolyte plate. There is. This is due to the fact that the linear expansion coefficient of the separator plate is larger than that of the electrolyte plate, as can be seen from the linear expansion characteristics shown in FIG. 6th
Figures a and b are schematic views of the elongated state of the battery main body viewed from the top and side.

電池は温度が上昇すると中心から四方向に伸び
るがセパレータ板の伸び量δSが電解質板の伸び量
δEよりも大きく、かつ電池は圧縮荷重Fが図の矢
印方向より受けているため、セパレータ板4の伸
び量δSに引張られて電解質板1が伸びようとす
る。従つて、セパレータ板4よりも引張強度の弱
い電解質板1は電池の起動停止(昇温、降温)ご
とに引張、圧縮を受けることになる。
When the temperature rises, the battery stretches in four directions from the center, but the amount of elongation δ S of the separator plate is larger than the amount of elongation δ E of the electrolyte plate, and the battery receives a compressive load F from the direction of the arrow in the figure, so the separator plate The electrolyte plate 1 tries to stretch due to the amount of elongation δ S of the plate 4. Therefore, the electrolyte plate 1, which has a lower tensile strength than the separator plate 4, is subjected to tension and compression every time the battery is started or stopped (temperature rise or fall).

したがつて、電解質板として用いられるセラミ
ツク材は、圧縮強度は高いが引張強度が低いため
にヒートサイクル時の疲労強度が問題となること
がわかつた。
Therefore, it has been found that the ceramic material used as the electrolyte plate has high compressive strength but low tensile strength, so that fatigue strength during heat cycling becomes a problem.

そして、電解質板に疲労による割れが発生した
場合、アノード側の水素とカソードの空気が混合
することになり水が発生する酸化反応が起こる。
こうなると発電反応が著しく低下すると共に発熱
が生じ、セパレータ板や電極を腐食させて電池本
体の寿命を短くすることとなる。
When cracks occur in the electrolyte plate due to fatigue, hydrogen on the anode side mixes with air on the cathode, causing an oxidation reaction that generates water.
If this happens, the power generation reaction will be significantly reduced and heat will be generated, corroding the separator plates and electrodes and shortening the life of the battery body.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

このように従来の装置にあつてはセラミツクス
製よりなる電解質板をオーステナイト板よりなる
セパレータで挟持する構造となつており、熱伸び
に対する配慮がなされていなかつた。
As described above, the conventional apparatus has a structure in which an electrolyte plate made of ceramic is sandwiched between separators made of austenite plates, and no consideration is given to thermal expansion.

〔発明の目的〕[Purpose of the invention]

本発明の目的は、熱伸びすなわちヒートサイク
ル性に強いこの種燃料電池を提供することにあ
る。
An object of the present invention is to provide a fuel cell of this type that is resistant to thermal elongation or heat cycling.

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

すなわち本発明は電解質板が配置されている部
分に、この電解質板の底部および側部を覆いかつ
鍔部を有する金属材料からなる薄板を設けると共
に、該薄板の鍔部をセパレータ板で挟持し、更
に、この薄板の電解質板の底部に位置する部分に
は、多数の孔を設けると共に、前記鍔部とセパレ
ータ板の間には電気絶縁部材を介在させるように
なして所期の目的を達成するようにしたものであ
る。
That is, the present invention provides a thin plate made of a metal material that covers the bottom and sides of the electrolyte plate and has a flange in a portion where the electrolyte plate is arranged, and the flange of the thin plate is sandwiched between separator plates. Further, in order to achieve the desired purpose, a large number of holes are provided in the thin plate located at the bottom of the electrolyte plate, and an electrically insulating member is interposed between the flange and the separator plate. This is what I did.

〔実施例〕〔Example〕

以下に、本発明の実施例を説明する。 Examples of the present invention will be described below.

第1図には、本発明に係る燃料電池の一実施例
を示す縦断面図が示されている。従来例と同様の
構成のものは同一符号で示している。
FIG. 1 shows a longitudinal sectional view of an embodiment of a fuel cell according to the present invention. Components having the same configuration as the conventional example are designated by the same reference numerals.

図において、電解質板1が配置されている部分
に例えば鉄材の薄板8が設けられている。薄板8
は電解質板1の底部および側部を覆う部分を有
し、またセパレータ板4に挟持される鍔部8bを
有している。
In the figure, a thin plate 8 made of iron material, for example, is provided at a portion where the electrolyte plate 1 is arranged. thin plate 8
has a portion that covers the bottom and side portions of the electrolyte plate 1, and also has a flange portion 8b that is sandwiched between the separator plates 4.

薄板8がこのように形成されていると、薄板8
のシール部近傍には段差が形成され、セパレータ
板4と薄板8との熱伸び差に追従することができ
る。すなわちフレキシブル性を有する。
When the thin plate 8 is formed in this way, the thin plate 8
A step is formed in the vicinity of the sealing portion, and can follow the difference in thermal expansion between the separator plate 4 and the thin plate 8. In other words, it has flexibility.

電解質板1は、焼結してもしなくてもよく、こ
の電解質板1の両端に位置するセル端部には、炭
酸塩が外部に洩れるのを防ぐため電気絶縁部材9
が介挿されている。この部材9とセパレータ板4
とは、拡散接合、レーザ接合等により極部的に高
温にすることにより一体化されている。セパレー
タ板4と電極2および電極3は、高温還元条件下
で容易に一体化できるため、あらかじめ接合する
ようにしておく。また碁盤目状に配列されている
薄板8は、図に示す如くシール部8a以外のセル
内部のみに、すなわち電解質の底部に位置する部
分に、孔が穿設されている。孔の大きさは、板の
強度および電池反応速度によつて設計を変える。
そして、この薄板の材質としては、オーステナイ
トステンレス鋼等のようなセパレータ板4と同一
のものが適している。また、セル内部の性質はア
ルカリ性であるため、耐アルカリ腐食表面処理が
必要である。
The electrolyte plate 1 may be sintered or not, and electrically insulating members 9 are provided at the cell ends located at both ends of the electrolyte plate 1 to prevent carbonate from leaking to the outside.
is inserted. This member 9 and separator plate 4
are integrated by heating the parts to extremely high temperatures through diffusion bonding, laser bonding, etc. Since the separator plate 4, electrode 2, and electrode 3 can be easily integrated under high-temperature reduction conditions, they are bonded in advance. Further, as shown in the figure, the thin plates 8 arranged in a grid pattern are provided with holes only inside the cells other than the seal portion 8a, that is, in the portion located at the bottom of the electrolyte. The size of the holes varies depending on the strength of the plate and the reaction rate of the cell.
As for the material of this thin plate, the same material as the separator plate 4, such as austenitic stainless steel, is suitable. Furthermore, since the inside of the cell is alkaline in nature, alkali corrosion-resistant surface treatment is required.

このように形成された燃料電池であると、セパ
レータ板4の端部同志の間は、電気絶縁部材9と
薄板の鍔部8bとなり、電解質板1は挟持されて
いないし、また、薄板はフレキシブル性を有する
のでセパレータ板4が熱伸びしたとしても、電解
質板1には割れは生じないのである。
In the fuel cell formed in this way, the electrical insulating member 9 and the thin plate flange 8b are located between the ends of the separator plates 4, the electrolyte plate 1 is not sandwiched, and the thin plate is flexible. Therefore, even if the separator plate 4 is thermally expanded, the electrolyte plate 1 will not crack.

〔発明の効果〕〔Effect of the invention〕

本発明は以上説明してきたように、電解質板が
配置されている部分に、この電解質板の底部およ
び側部を覆い、かつ、鍔部を有する金属材料から
なる薄板を設けると共に、該薄板の鍔部をセパレ
ータ板で挟持し、更に、この薄板の電解質板の底
部に位置する部分には、多数の孔を設けると共
に、前記鍔部とセパレータ板の間には電気絶縁部
材を介在させるようにしたものであるから、セパ
レータ板と電解質板との間に熱伸び差が生じて
も、セパレータ板の熱伸びが電解質板に及ぼすこ
となく、したがつて熱伸びすなわちヒートサイク
ル性に強いこの種燃料電池を得ることができる。
As described above, the present invention provides a thin plate made of a metal material that covers the bottom and sides of the electrolyte plate and has a flange in a portion where the electrolyte plate is arranged, and the flange of the thin plate. The electrolyte plate is sandwiched between separator plates, and the thin plate is provided with a large number of holes in the bottom portion of the electrolyte plate, and an electrically insulating member is interposed between the flange and the separator plate. Therefore, even if a difference in thermal expansion occurs between the separator plate and the electrolyte plate, the thermal expansion of the separator plate will not affect the electrolyte plate, thus obtaining this type of fuel cell that is resistant to thermal expansion, that is, heat cycle property. be able to.

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

第1図は、本発明の一実施例を示す縦断面図、
第2図は、従来の電池傾斜図、第3図は、従来の
電池の縦断面図、第4図a,bは、電池の起動停
止パターン図、第5図および第6図a,bは、セ
パレータと電解質板の線膨張係数および伸び説明
図である。 1……電解質板、2……アノード、3……カソ
ード、4……セパレータ板、8……薄板、8b…
…鍔部、9……電気絶縁部材。
FIG. 1 is a longitudinal sectional view showing an embodiment of the present invention;
Fig. 2 is an inclined view of a conventional battery, Fig. 3 is a vertical cross-sectional view of a conventional battery, Fig. 4 a and b are illustrations of starting and stopping patterns of the battery, and Figs. 5 and 6 a and b are FIG. 2 is an explanatory diagram of linear expansion coefficient and elongation of a separator and an electrolyte plate. DESCRIPTION OF SYMBOLS 1... Electrolyte plate, 2... Anode, 3... Cathode, 4... Separator plate, 8... Thin plate, 8b...
...Brim portion, 9...Electrical insulating member.

Claims (1)

【特許請求の範囲】 1 補強剤が混入された多孔質板の内部に電解質
が含浸されてなる電解質板と、 該電解質板を介して配置された一対の電極と、
各々の電極に対向する面に互いに直交するような
向きに形成されたリブによつて流体燃料および流
体酸化剤の流通路が形成されてなるセパレータ板
と、 を備えてなる燃料電池において、 前記電解質板が配置されている部分に、該電解
質板の底部および側部を覆い、かつ、鍔部を有す
る金属材料からなる薄板を設けると共に、該薄板
の鍔部を前記セパレータ板で挟持し、 更に、前記薄板の電解質板の底部に位置する部
分には、多数の孔を設けると共に、前記鍔部とセ
パレータ板の間には電気絶縁部材を介在させるよ
うにしたことを特徴とする燃料電池。 2 特許請求の範囲第1項記載の燃料電池におい
て、上記金属材料からなる薄板は、オーステナイ
ト鋼からなることを特徴とする燃料電池。 3 特許請求の範囲第2項記載の燃料電池におい
て、上記金属材料からなる薄板は、耐アルカリ腐
食表面処理を施してなることを特徴とする燃料電
池。
[Scope of Claims] 1. An electrolyte plate formed by impregnating an electrolyte inside a porous plate mixed with a reinforcing agent; a pair of electrodes disposed through the electrolyte plate;
a separator plate in which flow paths for fluid fuel and fluid oxidizer are formed by ribs formed in a direction perpendicular to each other on a surface facing each electrode; and the electrolyte. A thin plate made of a metal material that covers the bottom and sides of the electrolyte plate and has a flange is provided in the portion where the plate is arranged, and the flange of the thin plate is sandwiched between the separator plates, and further, A fuel cell characterized in that a plurality of holes are provided in a bottom portion of the thin electrolyte plate, and an electrically insulating member is interposed between the flange and the separator plate. 2. The fuel cell according to claim 1, wherein the thin plate made of the metal material is made of austenitic steel. 3. The fuel cell according to claim 2, wherein the thin plate made of the metal material has been subjected to an alkali corrosion-resistant surface treatment.
JP61135925A 1986-06-13 1986-06-13 Fuel cell Granted JPS62295359A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61135925A JPS62295359A (en) 1986-06-13 1986-06-13 Fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61135925A JPS62295359A (en) 1986-06-13 1986-06-13 Fuel cell

Publications (2)

Publication Number Publication Date
JPS62295359A JPS62295359A (en) 1987-12-22
JPH0565991B2 true JPH0565991B2 (en) 1993-09-20

Family

ID=15163057

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61135925A Granted JPS62295359A (en) 1986-06-13 1986-06-13 Fuel cell

Country Status (1)

Country Link
JP (1) JPS62295359A (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58129775A (en) * 1982-01-29 1983-08-02 Hitachi Ltd Fuel battery
JPS6093760A (en) * 1983-10-27 1985-05-25 Matsushita Electric Ind Co Ltd Molten salt fuel cell

Also Published As

Publication number Publication date
JPS62295359A (en) 1987-12-22

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