JPH04218264A - Manufacturing method of solid electrolyte fuel cell - Google Patents

Manufacturing method of solid electrolyte fuel cell

Info

Publication number
JPH04218264A
JPH04218264A JP2410959A JP41095990A JPH04218264A JP H04218264 A JPH04218264 A JP H04218264A JP 2410959 A JP2410959 A JP 2410959A JP 41095990 A JP41095990 A JP 41095990A JP H04218264 A JPH04218264 A JP H04218264A
Authority
JP
Japan
Prior art keywords
solid electrolyte
fuel electrode
molded body
manufacturing
fuel cell
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
JP2410959A
Other languages
Japanese (ja)
Inventor
Ryoichi Okuyama
良一 奥山
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.)
Yuasa Corp
Original Assignee
Yuasa Corp
Yuasa Battery 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 Yuasa Corp, Yuasa Battery Corp filed Critical Yuasa Corp
Priority to JP2410959A priority Critical patent/JPH04218264A/en
Priority to PCT/JP1991/001701 priority patent/WO1992010862A1/en
Priority to EP92900502A priority patent/EP0514552B1/en
Priority to US07/915,699 priority patent/US5290323A/en
Priority to DE69132207T priority patent/DE69132207T2/en
Publication of JPH04218264A publication Critical patent/JPH04218264A/en
Pending 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
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90Selection of catalytic material
    • H01M4/9041Metals or alloys
    • H01M4/905Metals or alloys specially used in fuel cell operating at high temperature, e.g. SOFC
    • H01M4/9066Metals or alloys specially used in fuel cell operating at high temperature, e.g. SOFC of metal-ceramic composites or mixtures, e.g. cermets
    • 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
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Composite Materials (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Fuel Cell (AREA)

Abstract

PURPOSE:To control contraction in the case of baking a complex compact and porosity of a fuel electrode by constituting a complex compact having a fuel electrode compact on an electrolyte compact by means of metallic oxide or slurry formed by adding metal and carbonic powder together. CONSTITUTION:After an electrolyte compact 5 is formed by using slurry containing zirconia obtained by adding a stabilizing agent therein, metallic oxide or slurry containing metal and carbonic powder is poured onto the electrolyte compact 5 so as to constitute a fuel electrode compact 6 as a complex compact, and then by baking it, a solid electrolyte - fuel electrode complex having a fuel electrode 7 on one surface and a solid electrolyte film 8 on the other surface is formed. Since the solid electrolyte film 8 and the fuel electrode 7 can integrally be constituted in one body, its porosity and mechanical strength can be controlled optionally, so that a solid electrolyte fuel cell having high performance can be realized.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は、固体電解質燃料電池の
製造方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing solid electrolyte fuel cells.

【0002】0002

【従来の技術】固体電解質燃料電池としては、リン酸型
燃料電池、溶融炭酸塩型燃料電池と類似した構造の平板
型、米国のアルゴンヌ国立研究所によって提案されたモ
ノリシック型、日本の電子技術総合研究所によって開発
中の円筒多素子型、米国のウェスティングハウス社によ
って提案された円筒単素子型が知られているが、現在は
高温におけるガスシールの容易さ、スタック構成の容易
さの点でウェスティングハウス社の円筒単素子型が注目
されている。
[Prior Art] Solid electrolyte fuel cells include a phosphoric acid fuel cell, a flat plate type with a structure similar to a molten carbonate fuel cell, a monolithic type proposed by Argonne National Laboratory in the United States, and a Japanese electronics technology complex. The cylindrical multi-element type currently being developed by the Institute, and the cylindrical single element type proposed by Westinghouse Corporation in the United States, are well known, but currently Westing is currently developing a cylindrical multi-element type that is being developed by Westinghouse, Inc. in the United States. Guhaus' cylindrical single element type is attracting attention.

【0003】このような固体電解質燃料電池に用いられ
る固体電解質の製造方法としては、プラズマ溶射法、化
学蒸着法(CVD)、電気化学蒸着法(EVD)、有機
金属ジルコニウム塩の熱分解法などが知られているが、
緻密な固体電解質膜が得られる方法としては、プラズマ
溶射法、電気化学蒸着法(EVD)があるのみである。
Methods for manufacturing the solid electrolyte used in such solid electrolyte fuel cells include plasma spraying, chemical vapor deposition (CVD), electrochemical vapor deposition (EVD), and thermal decomposition of organometallic zirconium salts. Although it is known,
The only methods for obtaining a dense solid electrolyte membrane are plasma spraying and electrochemical vapor deposition (EVD).

【0004】さらに、上記のような緻密な固体電解質膜
を作成する方法としては、図5のように安定化ジルコニ
ア粉末3をスラリーにし、基材1上に塗布して焼成する
試みもなされている。
Furthermore, as a method for producing a dense solid electrolyte membrane as described above, an attempt has been made to make a slurry of stabilized zirconia powder 3, apply it onto a base material 1, and sinter it as shown in FIG. .

【0005】[0005]

【発明が解決しようとする課題】上記した前者の製造方
法では、高価な製造装置を必要とするうえに、固体電解
質膜を必要とする部分と必要としない部分とを構成する
マスキングに時間がかかるため、電池の量産性に問題が
あった。
[Problem to be Solved by the Invention] The former manufacturing method described above requires expensive manufacturing equipment and takes time to mask the parts that require a solid electrolyte membrane and the parts that do not. Therefore, there was a problem with the mass production of batteries.

【0006】また、後者の製造方法では、焼成時に安定
化ジルコニア粉末3が収縮するため、基材1の上に構成
された固体電解質膜8に割れ2を生じたり、固体電解質
膜8が剥離するという問題があった。
Furthermore, in the latter manufacturing method, since the stabilized zirconia powder 3 shrinks during firing, cracks 2 may occur in the solid electrolyte membrane 8 formed on the base material 1 or the solid electrolyte membrane 8 may peel off. There was a problem.

【0007】[0007]

【課題を解決するための手段】上記課題を解決するため
、本発明は、安定化剤を添加したジルコニアを含有する
スラリーを成形して電解質成形体とする工程と、前記電
解質成形体の一方の面に、金属もしくは金属酸化物と炭
素粉末とを含有するスラリーを成形して燃料極成形体を
構成し、電解質成形体を燃料極成形体とを一体化した複
合成形体を得る工程と、この複合成形体を焼成して固体
電解質−燃料極複合体を得る工程と、この固体電解質−
燃料極複合体の固体電解質側に空気極を形成することを
特徴とするものである。
[Means for Solving the Problems] In order to solve the above problems, the present invention provides a step of forming an electrolyte molded body by molding a slurry containing zirconia to which a stabilizer has been added, and a step of forming one of the electrolyte molded bodies. A step of forming a slurry containing metal or metal oxide and carbon powder on a surface to form a fuel electrode compact, and obtaining a composite compact in which the electrolyte compact and the fuel electrode compact are integrated; A step of firing a composite molded body to obtain a solid electrolyte-fuel electrode composite, and
This is characterized in that an air electrode is formed on the solid electrolyte side of the fuel electrode composite.

【0008】[0008]

【作用】上記のように、本発明は、燃料極成形体中に含
有させた炭素粉末により、電解質成形体と燃料極成形体
とを一体化した複合成形体を焼成して固体電解質−燃料
極複合体とする時、前記炭素粉末が酸化されて一酸化炭
素もしくは二酸化炭素として外部に放出されるので、含
有させる炭素粉末の量をコントロールすると、燃料極側
の収縮を固体電解質膜側の収縮に近似させることができ
る。
[Operation] As described above, the present invention provides a solid electrolyte-fuel electrode by firing a composite molded body in which an electrolyte molded body and a fuel electrode molded body are integrated using carbon powder contained in the fuel electrode molded body. When forming a composite, the carbon powder is oxidized and released to the outside as carbon monoxide or carbon dioxide. Therefore, by controlling the amount of carbon powder contained, the shrinkage on the fuel electrode side can be reduced to the shrinkage on the solid electrolyte membrane side. It can be approximated.

【0009】また、炭素粉末の粒度をコントロールする
ことにより、燃料極側の多孔度を変化させることができ
る。
Furthermore, by controlling the particle size of the carbon powder, the porosity on the fuel electrode side can be changed.

【0010】さらに、本発明は、複合成形体を焼成して
いるので、燃料極の強度が高まり基材としての作用もす
る。
Furthermore, in the present invention, since the composite molded body is fired, the strength of the fuel electrode is increased and it also functions as a base material.

【0011】[0011]

【実施例】図1は、本発明の固体電解質燃料電池の製造
方法によって形成した電解質成形体5の断面図で、石膏
のような吸水性を有する材料からなる型4に安定化剤と
してのイットリアを添加したジルコニア、水、分散材、
バインダー、消泡剤からなるスラリーを流し込んで一定
時間放置した後、余剰のスラリーを除去した状態を示す
[Example] Fig. 1 is a cross-sectional view of an electrolyte molded body 5 formed by the method for producing a solid electrolyte fuel cell of the present invention. zirconia, water, dispersion material,
The state is shown in which a slurry consisting of a binder and an antifoaming agent is poured in, left to stand for a certain period of time, and then the excess slurry is removed.

【0012】図2は、前記電解質成形体5の一方の面、
すなわち内側の面に燃料極成形体6を形成した状態の断
面図で、金属もしくは金属酸化物と炭素粉末とを含有す
るスラリーを電解質成形体5の内側の面に流し込んで一
定時間放置した後、余剰のスラリーを除去して電解質成
形体5と燃料極成形体6とを一体化した複合成形体を形
成した状態を示す。
FIG. 2 shows one side of the electrolyte molded body 5,
That is, this is a cross-sectional view of a state in which the fuel electrode molded body 6 is formed on the inner surface, and after pouring a slurry containing metal or metal oxide and carbon powder onto the inner surface of the electrolyte molded body 5 and leaving it for a certain period of time, The figure shows a state in which the excess slurry has been removed to form a composite molded body in which the electrolyte molded body 5 and the fuel electrode molded body 6 are integrated.

【0013】図3は、図2の複合成形体を乾燥させて型
4を除去した後焼成して得た固体電解質−燃料極複合体
の断面図で、内側に多孔性の燃料極7が、外側に緻密な
固体電解質膜8が形成される。
FIG. 3 is a cross-sectional view of a solid electrolyte-fuel electrode composite obtained by drying the composite molded body of FIG. 2, removing the mold 4, and then firing it. A dense solid electrolyte membrane 8 is formed on the outside.

【0014】前記複合成形体の焼成時、燃料極成形体6
中に含有させた炭素粉末は酸化されて一酸化炭素もしく
は二酸化炭素として外部に放出されるので、含有させる
炭素粉末の量を増加させると、燃料極7側の収縮率は大
きくなる。これに対して、固体電解質膜8側の収縮率は
ほぼ一定であるから、燃料極成形体6中に含有させる炭
素粉末の量をコントロールし、燃料極7側の収縮率を固
体電解質膜8側の収縮率に近似させると、多孔性の燃料
極7と緻密な固体電解質膜8とを同時に製造することが
できる。
[0014] When firing the composite molded body, the fuel electrode molded body 6
Since the carbon powder contained therein is oxidized and released to the outside as carbon monoxide or carbon dioxide, increasing the amount of carbon powder contained increases the shrinkage rate on the fuel electrode 7 side. On the other hand, since the shrinkage rate on the solid electrolyte membrane 8 side is almost constant, the amount of carbon powder contained in the fuel electrode molded body 6 is controlled, and the shrinkage rate on the fuel electrode 7 side is adjusted to the solid electrolyte membrane 8 side. By approximating the shrinkage rate to , it is possible to simultaneously manufacture the porous fuel electrode 7 and the dense solid electrolyte membrane 8.

【0015】一方、添加するイットリアの量に応じてジ
ルコニアを立方晶ジルコニア、正方晶ジルコニア、部分
安定化ジルコニアにすることができ、固体電解質膜8の
強度をコントロールすることができるので、前述した炭
素粉末の量のコントロールと併用することにより、複合
成形体の焼成時の割れや剥離を防止することができ、固
体電解質−燃料極複合体の性能を向上させることができ
る。
On the other hand, depending on the amount of yttria added, zirconia can be made into cubic zirconia, tetragonal zirconia, or partially stabilized zirconia, and the strength of the solid electrolyte membrane 8 can be controlled. By using it together with controlling the amount of powder, cracking and peeling of the composite molded body during firing can be prevented, and the performance of the solid electrolyte-fuel electrode composite can be improved.

【0016】図4は、前記固体電解質−燃料極複合体の
固体電解質膜8の外側に空気極9として、ストロンチウ
ムドープしたLaMnO3 をデイッピング法によって
形成した状態の断面図、すなわち本発明の製造方法によ
って得られた固体電解質燃料電池の断面図である。なお
、空気極9の形成方法としては、デイッピング法以外に
スラリー塗布法、溶射法等があり、特に限定するもので
ないことは言うまでもない。
FIG. 4 is a cross-sectional view of a state in which strontium-doped LaMnO3 is formed as an air electrode 9 on the outside of the solid electrolyte membrane 8 of the solid electrolyte-fuel electrode composite by the dipping method, that is, by the manufacturing method of the present invention. FIG. 3 is a cross-sectional view of the obtained solid electrolyte fuel cell. Note that methods for forming the air electrode 9 include, in addition to the dipping method, a slurry coating method, a thermal spraying method, and the like, and it goes without saying that the method is not particularly limited.

【0017】こうして得られた図4のような固体電解質
燃料電池を作動温度である700℃から1000℃に昇
温し、燃料極7側に燃料を、空気極9側に空気を供給す
ると、燃料によって燃料極7中の酸化ニッケルが還元さ
れる。
When the solid electrolyte fuel cell thus obtained as shown in FIG. 4 is heated from the operating temperature of 700° C. to 1000° C., and fuel is supplied to the fuel electrode 7 side and air to the air electrode 9 side, the fuel The nickel oxide in the fuel electrode 7 is reduced by this.

【0018】従って、図4の燃料極7と空気極9とを外
部回路に接続すると、空気極9から取り入れられた酸素
は外部回路から供給される電子を取り込んで酸素イオン
となり、この酸素イオンは固体電解質膜8を通って固体
電解質膜8と燃料極7との界面に到達する。
Therefore, when the fuel electrode 7 and the air electrode 9 in FIG. 4 are connected to an external circuit, the oxygen taken in from the air electrode 9 takes in the electrons supplied from the external circuit and becomes oxygen ions. It passes through the solid electrolyte membrane 8 and reaches the interface between the solid electrolyte membrane 8 and the fuel electrode 7 .

【0019】一方、この界面には燃料極7中を拡散して
きた水素もしくは一酸化炭素が存在し、この水素もしく
は一酸化炭素と前記酸素イオンとが反応して水蒸気およ
び二酸化炭素を生成するとともに、外部回路に電子を放
出するので、外部回路には空気極9を正極、燃料極7を
負極とした起電力が生じ、電池としての作用がなされる
ことになる。
On the other hand, hydrogen or carbon monoxide that has diffused through the fuel electrode 7 is present at this interface, and this hydrogen or carbon monoxide reacts with the oxygen ions to generate water vapor and carbon dioxide. Since electrons are emitted to the external circuit, an electromotive force is generated in the external circuit with the air electrode 9 as the positive electrode and the fuel electrode 7 as the negative electrode, and it functions as a battery.

【0020】以上の説明は、型4を用いて複合成形体を
形成しているが、カレンダーロール等を用いてスラリー
をテープ状に成形すれば平板型の複合成形体を形成でき
ることは言うまでもない。
In the above explanation, a composite molded body is formed using the mold 4, but it goes without saying that a flat plate-shaped composite molded body can be formed by molding the slurry into a tape shape using a calendar roll or the like.

【0021】[0021]

【発明の効果】上記した如く、本発明は緻密な固体電解
質膜8と多孔性の燃料極7とが容易に形成でき、その多
孔度は含有させる炭素粉末の粒度をコントロールするこ
とによって変化させることができ、その機械的強度は含
有させる炭素粉末の量をコントロールすることによって
変化させることができるので、高性能な固体電解質燃料
電池が得られる。
[Effects of the Invention] As described above, according to the present invention, a dense solid electrolyte membrane 8 and a porous fuel electrode 7 can be easily formed, and the porosity can be changed by controlling the particle size of the carbon powder contained therein. Since the mechanical strength can be changed by controlling the amount of carbon powder contained, a high-performance solid electrolyte fuel cell can be obtained.

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

【図1】型4にスラリーを流し込んで一定時間放置して
電解質成形体5とした後、余剰のスラリーを除去した状
態の断面図である。
FIG. 1 is a cross-sectional view of a state in which surplus slurry is removed after slurry is poured into a mold 4 and left for a certain period of time to form an electrolyte molded body 5. FIG.

【図2】図1の電解質成形体5の上にスラリーを流し込
んで一定時間放置して燃料極成形体6とした後、余剰の
スラリーを除去して複合成形体とした状態の断面図であ
る。
FIG. 2 is a cross-sectional view of a state in which a slurry is poured onto the electrolyte molded body 5 of FIG. 1 and left for a certain period of time to form a fuel electrode molded body 6, and then excess slurry is removed to form a composite molded body. .

【図3】図2の複合成形体から型4を除去した後焼成し
て得た固体電解質−燃料極複合体の断面図である。
3 is a cross-sectional view of a solid electrolyte-fuel electrode composite obtained by firing after removing the mold 4 from the composite molded body of FIG. 2. FIG.

【図4】固体電解質−燃料極複合体の外側に空気極9を
形成した状態の断面図である。
FIG. 4 is a cross-sectional view of a state in which an air electrode 9 is formed on the outside of the solid electrolyte-fuel electrode composite.

【図5】従来の固体電解質燃料電池の製造方法により製
造された固体電解質膜8の断面図である。
FIG. 5 is a cross-sectional view of a solid electrolyte membrane 8 manufactured by a conventional solid electrolyte fuel cell manufacturing method.

【符号の説明】[Explanation of symbols]

4  型 5  電解質成形体 6  燃料極成形体 7  燃料極 8  固体電解質膜 9  空気極 4 type 5 Electrolyte molded body 6 Fuel electrode molded body 7 Fuel electrode 8 Solid electrolyte membrane 9 Air electrode

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】  安定化剤を添加したジルコニアを含有
するスラリーを成形して電解質成形体とする工程と、前
記電解質成形体の一方の面に、金属もしくは金属酸化物
と炭素粉末とを含有するスラリーを成形して燃料極成形
体を構成し、電解質成形体と燃料極成形体とを一体化し
た複合成形体を得る工程と、この複合成形体を焼成して
固体電解質−燃料極複合体を得る工程と、この固体電解
質−燃料極複合体の固体電解質側に空気極を形成するこ
とを特徴とする固体電解質燃料電池の製造方法。
1. A step of forming an electrolyte molded body by molding a slurry containing zirconia to which a stabilizer has been added, and containing metal or metal oxide and carbon powder on one surface of the electrolyte molded body. A step of molding the slurry to form a fuel electrode molded body to obtain a composite molded body that integrates the electrolyte molded body and the fuel electrode molded body, and firing the composite molded body to form a solid electrolyte-fuel electrode composite body. 1. A method for manufacturing a solid electrolyte fuel cell, comprising: obtaining the solid electrolyte fuel electrode, and forming an air electrode on the solid electrolyte side of the solid electrolyte-fuel electrode composite.
【請求項2】  安定化剤を添加したジルコニアは立方
晶ジルコニア、正方晶ジルコニア、部分安定化ジルコニ
アの単独物もしくは複数種の混合物からなることを特徴
とする請求項第1項記載の固体電解質燃料電池の製造方
法。
2. The solid electrolyte fuel according to claim 1, wherein the zirconia added with a stabilizer is composed of cubic zirconia, tetragonal zirconia, partially stabilized zirconia alone or in a mixture of multiple types. How to manufacture batteries.
【請求項3】  安定化剤は、イットリウム、カルシウ
ム、スカンジウム、イッテルビウム、ネオジウム、カド
リニウムの酸化物であることを特徴とする請求項第1項
記載の固体電解質燃料電池の製造方法。
3. The method for manufacturing a solid electrolyte fuel cell according to claim 1, wherein the stabilizer is an oxide of yttrium, calcium, scandium, ytterbium, neodymium, or quadrinium.
【請求項4】  金属酸化物もしくは金属は、ニッケル
またはコバルトの酸化物もしくは金属ニッケルまたは金
属コバルトであることを特徴とする請求項第1項記載の
固体電解質燃料電池の製造方法。
4. The method for manufacturing a solid electrolyte fuel cell according to claim 1, wherein the metal oxide or metal is an oxide of nickel or cobalt, or metal nickel or metal cobalt.
【請求項5】  焼成は、不活性気流中または還元雰囲
気中で行うことを特徴とする請求項第1項記載の固体電
解質燃料電池の製造方法。
5. The method for manufacturing a solid oxide fuel cell according to claim 1, wherein the calcination is performed in an inert gas flow or a reducing atmosphere.
【請求項6】  空気極は、ストロンチウムもしくはカ
ルシウムをドープしたLaMnO3 、LaCoO3 
、CaMnO3 であることを特徴とする請求項第1項
記載の固体電解質燃料電池の製造方法。
6. The air electrode is made of LaMnO3 or LaCoO3 doped with strontium or calcium.
, CaMnO3, the method for manufacturing a solid electrolyte fuel cell according to claim 1.
JP2410959A 1990-12-10 1990-12-14 Manufacturing method of solid electrolyte fuel cell Pending JPH04218264A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP2410959A JPH04218264A (en) 1990-12-14 1990-12-14 Manufacturing method of solid electrolyte fuel cell
PCT/JP1991/001701 WO1992010862A1 (en) 1990-12-10 1991-12-09 Method for manufacturing solid-state electrolytic fuel cell
EP92900502A EP0514552B1 (en) 1990-12-10 1991-12-09 Method for manufacturing solid-state electrolytic fuel cell
US07/915,699 US5290323A (en) 1990-12-10 1991-12-09 Manufacturing method for solid-electrolyte fuel cell
DE69132207T DE69132207T2 (en) 1990-12-10 1991-12-09 METHOD FOR PRODUCING ELECTROLYTIC SOLID CELL

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2410959A JPH04218264A (en) 1990-12-14 1990-12-14 Manufacturing method of solid electrolyte fuel cell

Publications (1)

Publication Number Publication Date
JPH04218264A true JPH04218264A (en) 1992-08-07

Family

ID=18520039

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2410959A Pending JPH04218264A (en) 1990-12-10 1990-12-14 Manufacturing method of solid electrolyte fuel cell

Country Status (1)

Country Link
JP (1) JPH04218264A (en)

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