JP2957404B2 - Single cell manufacturing method of solid oxide fuel cell - Google Patents

Single cell manufacturing method of solid oxide fuel cell

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Publication number
JP2957404B2
JP2957404B2 JP5336789A JP33678993A JP2957404B2 JP 2957404 B2 JP2957404 B2 JP 2957404B2 JP 5336789 A JP5336789 A JP 5336789A JP 33678993 A JP33678993 A JP 33678993A JP 2957404 B2 JP2957404 B2 JP 2957404B2
Authority
JP
Japan
Prior art keywords
solid electrolyte
electrolyte membrane
electrode
fuel cell
porous
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
JP5336789A
Other languages
Japanese (ja)
Other versions
JPH07201342A (en
Inventor
直之 西村
隆章 槙野
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.)
Mitsui Zosen KK
Original Assignee
Mitsui Zosen KK
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 Mitsui Zosen KK filed Critical Mitsui Zosen KK
Priority to JP5336789A priority Critical patent/JP2957404B2/en
Publication of JPH07201342A publication Critical patent/JPH07201342A/en
Application granted granted Critical
Publication of JP2957404B2 publication Critical patent/JP2957404B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • 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

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  • Fuel Cell (AREA)

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、固体電解質型燃料電池
の単電池製造法に係り、特に、製造コストを低減し、機
械的強度を大きくすることができる固体電解質型燃料電
池の単電池製造法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing a single cell of a solid oxide fuel cell, and more particularly, to a method of manufacturing a single cell of a solid oxide fuel cell capable of reducing the manufacturing cost and increasing the mechanical strength. About the law.

【0002】[0002]

【従来の技術】低公害のエネルギー源として注目を集め
ている燃料電池の中でも、特に固体電解質型燃料電池は
電解質の漏洩がなく、反応速度が大きい電池として期待
されている。固体電解質型燃料電池は、電池の最小単位
である単電池(以下、単セルともいう)を多数積層し、
これを電気的に直列または並列に接続したものであり、
前記単セルの両電極面には電池の内部抵抗を低減するた
めに集電体が組込まれている。
2. Description of the Related Art Among fuel cells that have been attracting attention as low-pollution energy sources, solid electrolyte fuel cells, in particular, are expected to have a high reaction rate without electrolyte leakage. A solid oxide fuel cell stacks a number of single cells (hereinafter, also referred to as single cells), which are the minimum unit of the battery,
This is electrically connected in series or parallel,
Current collectors are incorporated on both electrode surfaces of the single cell in order to reduce the internal resistance of the battery.

【0003】ところで、単電池を構成する固体電解質膜
には緻密度が要求される一方、電極膜には多孔質性が要
求される。緻密構造の固体電解質膜上に多孔質構造の電
極膜を積層することは非常に困難であり、従来は、固体
電解質膜の構成材料からなる固体電解質膜のグリーン体
と、電極材料からなる電極膜グリーン体とを接合し、こ
れを一体として焼成する共焼結法が広く採用されてい
た。
Meanwhile, a solid electrolyte membrane constituting a unit cell is required to have a high density, while an electrode membrane is required to be porous. It is very difficult to laminate a porous electrode membrane on a dense solid electrolyte membrane. Conventionally, a green solid electrolyte membrane composed of the constituent materials of the solid electrolyte membrane and an electrode membrane composed of the electrode material A co-sintering method of bonding a green body and firing the green body integrally has been widely adopted.

【0004】しかしながら上記従来技術は、集電体(電
極)材料と電解質材料との焼結時の収縮過程が異なるた
めに、共焼結する前にセラミックス原料粉末をあらかじ
め仮焼したり構成材料の粒径を制御するなどして収縮過
程を厳密に制御する必要があった。従って、材料の歩留
まりが低下し、製作コストが高くつくという問題があ
り、特に大面積の単セルを製造する場合の材料の歩留ま
りは極めて低く、その改善が望まれていた。
[0004] However, in the above prior art, since the current collector (electrode) material and the electrolyte material have different shrinkage processes during sintering, the ceramic raw material powder is calcined in advance before co-sintering or the constituent materials are It was necessary to strictly control the shrinkage process by controlling the particle size. Therefore, there is a problem that the yield of the material is reduced and the production cost is high. In particular, the yield of the material when a large-area single cell is manufactured is extremely low, and improvement thereof has been desired.

【0005】[0005]

【発明が解決しようとする課題】本発明の目的は、上記
従来技術の問題点を解決し、特別な前処理が不要で、材
料の歩留まり率が高く、製作コストを低減することがで
きる固体電解質型燃料電池の単電池製造法を提供するこ
とにある。
SUMMARY OF THE INVENTION An object of the present invention is to solve the above-mentioned problems of the prior art, and to eliminate the need for a special pretreatment, to increase the material yield rate and to reduce the manufacturing cost. The object of the present invention is to provide a method for manufacturing a unit cell of a fuel cell.

【0006】[0006]

【課題を解決するための手段】上記目的を達成するた
め、本発明は、固体電解質型燃料電池の単電池製造法で
あって、多孔質な電極および集電体の骨格を、これが積
層される緻密質である固体電解質膜と同一材料で構成
し、一度の焼成によって前記固体電解質膜と、電極材料
および集電体材料が含有された多孔質部とが積層した焼
成体を得ようとするものである。
In order to achieve the above object, the present invention relates to a method for manufacturing a single cell of a solid oxide fuel cell, wherein a porous electrode and a skeleton of a current collector are laminated. A solid body composed of the same material as a dense solid electrolyte membrane, which is intended to obtain a fired body in which the solid electrolyte membrane and a porous portion containing an electrode material and a current collector material are laminated by one firing. It is.

【0007】すなわち、本願で特許請求する発明は以下
のとおりである。 (1)固体電解質膜の表面に電極膜を形成する固体電解
質型燃料電池の単電池製造法において、固体電解質膜の
構成材料スラリと、電極材料および集電体材料がコート
された多孔化材粒子とを混合し、該混合物をシート状に
成形し、乾燥した後、焼成することにより、固体電解質
膜としての緻密質部と、該緻密質部に積層された集電機
能を有する電極膜となる多孔質部とを形成し、次いで、
前記緻密質部の他方面に前記集電機能を有する電極膜と
対をなす電極膜を形成することを特徴とする固体電解質
型燃料電池の単電池製造法。
That is, the invention claimed in the present application is as follows. (1) In a method for manufacturing a single cell of a solid oxide fuel cell in which an electrode film is formed on the surface of a solid electrolyte membrane, a slurry of constituent materials of the solid electrolyte membrane and porous material particles coated with an electrode material and a current collector material And the mixture is formed into a sheet, dried, and fired to form a dense portion as a solid electrolyte membrane and an electrode film having a current collecting function laminated on the dense portion. Forming a porous part, and then
A method for manufacturing a single cell of a solid oxide fuel cell, comprising forming an electrode film paired with the electrode film having a current collecting function on the other surface of the dense portion.

【0008】[0008]

【作用】固体電解質膜の構成材料スラリと、電極材料お
よび集電体材料をコートした多孔化材粒子の混合物をシ
ート状に成形してグリーン体とし、その後、乾燥するこ
とにより、前記電極材料および集電体材料がコートされ
た多孔化材粒子(以下、コート多孔化材ともいう)は比
重が小さいために浮上し、前記グリーン体の表層部は主
としてコートされた多孔化材層となり、下層部は固体電
解質膜の構成材料スラリのみからなるスラリ層となる。
このグリーン体を焼成することにより、表層部は多孔化
材粒子が消失して電極材料および集電体材料を含有する
多孔質の、集電体機能を併せもつ電極膜となり、一方、
下層部は固体電解質膜の構成材料のみからなる緻密質の
固体電解質膜となる。この固体電解質膜の他方面に前記
電極膜と対をなす電極膜が形成されることによって単電
池となる。
The mixture of the material slurry of the solid electrolyte membrane and the porous material particles coated with the electrode material and the current collector material is formed into a sheet shape to form a green body, and then dried to obtain a green body. The porous material particles coated with the current collector material (hereinafter, also referred to as a coated porous material) float due to low specific gravity, and the surface layer portion of the green body mainly becomes a coated porous material layer, and the lower layer portion Becomes a slurry layer consisting only of the slurry of the constituent material of the solid electrolyte membrane.
By firing this green body, the surface layer becomes a porous electrode film containing both an electrode material and a current collector material, with the porous material particles disappearing, and an electrode film having both current collector functions.
The lower layer is a dense solid electrolyte membrane composed of only the constituent materials of the solid electrolyte membrane. By forming an electrode film paired with the electrode film on the other surface of the solid electrolyte film, a single cell is obtained.

【0009】本発明において、固体電解質膜の構成材料
としては、例えばZrO2 −Y2 3 (YSZ)、Ce
2 −CaO、CeO2 −Y2 3 系のものが使用され
る。また、空気側電極の構成材料としては、例えばラン
タン系のLaCoO3 、La 0.7 Sr0.3 MnO3 、L
0.7 Ca0.3 MnO3 、La0.6 Ba0.4 Co0.8
0.2 3 等が、燃料側電極の構成材料としては、例え
ばニッケル系のNiO−ZrO2 −Y2 3 等が、さら
に集電体の構成材料としては、例えば空気側には(L
a、Sr)MnO3 系のペロブスカイト、燃料側にはN
i−CeO2 、Ni−YSZ、Fe−YSZ等のサーメ
ット等が使用される。これらの構成材料は、例えば0.
1〜10μmに粉砕し、スラリとして使用される。スラ
リ調製時の溶媒としては、例えばエタノール、トルエン
またはエタノールとトルエンとの混合液等が使用され
る。固体電解質膜の構成材料スラリには成形性を確保す
るために、例えばポリビニルブチラール(PVB)、ジ
ブチルフタレート(DBP)等のバインダーを添加する
ことが好ましい。
In the present invention, the constituent material of the solid electrolyte membrane
Is, for example, ZrOTwo-YTwoO Three(YSZ), Ce
OTwo-CaO, CeOTwo-YTwoOThreeSystem is used
You. Further, as a constituent material of the air-side electrode, for example,
Tan-based LaCoOThree, La 0.7Sr0.3MnOThree, L
a0.7Ca0.3MnOThree, La0.6Ba0.4Co0.8C
u0.2OThreeFor example, as a constituent material of the fuel-side electrode,
Nickel-based NiO-ZrOTwo-YTwoOThreeEtc.
As a constituent material of the current collector, for example, (L
a, Sr) MnOThreeSystem perovskite, N on fuel side
i-CeOTwo, Ni-YSZ, Fe-YSZ, etc.
Or the like is used. These constituent materials are, for example, 0.1.
It is pulverized to 1 to 10 μm and used as a slurry. Sura
Solvents for re-preparation include, for example, ethanol, toluene
Or a mixture of ethanol and toluene is used.
You. Formability is ensured for the solid electrolyte membrane material slurry
For example, polyvinyl butyral (PVB),
Add a binder such as butyl phthalate (DBP)
Is preferred.

【0010】本発明において、多孔化材粒子とは、焼成
時にガス化する、固体電解質膜の構成材料スラリよりも
比重が小さく、該スラリ中で浮上するものをいう。この
ような多孔化材粒子としては、例えばカーボンビーズ、
メラニンシアヌレート、その他有機化合物等が用いられ
る。多孔化材粒子の粒径は、例えば20〜200μmで
ある。
In the present invention, the porous material particles are particles which are gasified at the time of firing, have a lower specific gravity than a constituent material slurry of the solid electrolyte membrane, and float in the slurry. Such porous material particles include, for example, carbon beads,
Melanin cyanurate and other organic compounds are used. The particle size of the porous material particles is, for example, 20 to 200 μm.

【0011】本発明において多孔化材粒子に電極材料お
よび集電体材料をコートする方法としては、例えばスラ
リコートまたはCVD法(化学蒸着法)等があげられ
る。固体電解質膜の構成材料スラリと、コート多孔化材
との混合比は、例えば100対10〜100対50であ
り、特に、100対25であることが好ましい。コート
多孔化材の混合割合を加減することにより、電極膜とな
る多孔質部の厚さが変化する。固体電解質膜の構成材料
スラリとコート多孔化材との混合物をシート状に成形す
る方法としては、例えばテープキャスト法等があげられ
る。シート状に成形されたグリーン体は裁断後、自然乾
燥される。固体電解質膜の構成材料スラリとコート多孔
化材との混合物をシート状に成形する代わりに、前記固
体電解質膜の構成材料スラリのみをシート化したグリー
ン体の表層に、該グリーン体が乾燥する前に、前記コー
ト多孔化材を撒布しても同様のグリーン体が得られる。
In the present invention, examples of a method of coating the porous material particles with the electrode material and the current collector material include slurry coating and CVD (chemical vapor deposition). The mixing ratio of the constituent material slurry of the solid electrolyte membrane and the coating porous material is, for example, 100: 10 to 100: 50, and particularly preferably 100: 25. By adjusting the mixing ratio of the coating porous material, the thickness of the porous portion serving as the electrode film changes. Examples of a method of forming a mixture of the slurry of the constituent material of the solid electrolyte membrane and the coating porous material into a sheet include a tape casting method. The green body formed into a sheet shape is cut and then naturally dried. Instead of forming the mixture of the material slurry of the solid electrolyte membrane and the coating porous material into a sheet, the surface of the green body in which only the material slurry of the solid electrolyte membrane is formed into a sheet, before the green body is dried Then, a similar green body can be obtained by spraying the coated porous material.

【0012】本発明において、乾燥後のグリーン体は、
例えば大気中1000〜1400℃で1〜10時間焼成
される。得られた焼成体の前記緻密質からなる固体電解
質膜の他方面への電極膜の形成は公知の方法で行われ
る。
In the present invention, the green body after drying is
For example, it is fired in the atmosphere at 1000 to 1400 ° C. for 1 to 10 hours. The formation of the electrode film on the other surface of the dense solid electrolyte film of the obtained fired body is performed by a known method.

【0013】[0013]

【実施例】次に本発明を実施例によってさらに詳細に説
明する。図1は、本発明の一実施例である固体電解質型
燃料電池の単電池製造法の製作フローを示す説明図であ
り、製作工程における単セルの模式図を併記したもので
ある。
Next, the present invention will be described in more detail with reference to examples. FIG. 1 is an explanatory diagram showing a manufacturing flow of a method for manufacturing a single cell of a solid oxide fuel cell according to one embodiment of the present invention, and also shows a schematic diagram of a single cell in a manufacturing process.

【0014】図において、まず(1)固体電解質膜の構
成材料である、例えば8mol%のイットリア安定化ジ
ルコニア(以下、YSZという)の0.1〜5μmの粉
末100gに、有機バインダーとして、例えばポリビニ
ルブチラール(PVB)を13.5g、可塑剤としてジ
ブチルフタレートを12g、溶媒として、例えばトルエ
ンとエタノールの3対2混合液150ccをそれぞれ加
えて混練してYSZスラリを調製する。(2)次いで、
電極材料として電極活性が大きい(La0.8 Sr0.2
0.9 MnO3 を、また集電体材料として高電気伝導性の
(La0.6 Sr 0.4 0.9 MnO3 をそれぞれ用い、こ
れをそれぞれ電解質の場合と同様の要領で混練し、スラ
リ化して、多孔化材である、例えば粒径30〜50μm
のカーボンビーズ(カーボン粒子)表面にコートし、電
極材料および集電体材料がコートされたカーボンビーズ
を調製する。図2は、電極材料および集電体材料がコー
トされたカーボンビーズの断面部である。図において、
断面円形のカーボンビーズ5の表面に電極材料および集
電体材料のコート層7および6が形成されている。コー
ト層の厚みは、例えば50〜100μmであり、電極材
料および集電体材料のカーボンビーズ表面への付着量
は、外側から30μm程度の厚さまでが電極材料、その
内側が集電体材料である。
In the figure, first, (1) the structure of the solid electrolyte membrane
8 mol% yttria stabilized di
0.1 to 5 μm powder of Luconia (hereinafter referred to as YSZ)
100 g of powder, as an organic binder, for example, polyvinyl
13.5 g of rubutyral (PVB)
12 g of butyl phthalate, for example, toluene
150 cc of a 3 to 2 mixture of ethanol and ethanol
To prepare a YSZ slurry. (2) Then,
High electrode activity as electrode material (La0.8Sr0.2)
0.9MnOThreeAs a current collector material with high electrical conductivity
(La0.6Sr 0.4)0.9MnOThreeUsing
Are kneaded in the same manner as for the electrolyte,
Into a porous material, for example, a particle size of 30 to 50 μm.
Coated on the surface of carbon beads (carbon particles)
Carbon beads coated with electrode material and current collector material
Is prepared. FIG. 2 shows that the electrode material and the current collector material are coated.
This is a cross-sectional portion of the carbon bead. In the figure,
Electrode material and collection are applied to the surface of the carbon beads 5 having a circular cross section.
The coating layers 7 and 6 of the electric conductor material are formed. Co
The thickness of the electrode layer is, for example, 50 to 100 μm, and the electrode material
Of adsorbent and current collector material on carbon bead surface
Is the electrode material up to a thickness of about 30 μm from the outside,
The inside is the current collector material.

【0015】次いで、(3)残留溶媒量を調節して粘度
を調整した前記YSZスラリと前記コート多孔化材とし
てのカーボンビーズとを100対25の混合比で混合
し、その後(4)この混合物をテープキャスト法によ
り、すなわち離型剤を塗布した樹脂製シート上に厚さを
制御しながら展開してシート状に成形してグリーン体と
した。(5)次いで、得られたグリーン体を所定形状に
裁断して乾燥した。このとき、前記コート多孔化材であ
るカーボンビーズは比重が小さいためにグリーン体の表
層部に浮上する。従って、グリーン体の表層部は主とし
てコート多孔化材としてのカーボンビーズの層となり、
下層部は固体電解質の構成材料(YSZスラリ)のみか
らなるスラリ層となる。(6)次いでこのグリーン体を
大気中1450度で5時間焼成すると、カーボンビーズ
が消失して固体電解質膜の構成材料からなる多孔質部に
電極材料および集電体材料が含有された、集電体機能を
有する空気側電極膜と、固体電解質膜の構成材料のみか
らなる緻密構造の固体電解質膜とが積層された焼成体と
なる。得られた焼成体を徐冷して常温まで冷却した後、
(7)前記空気側電極が設けられていない前記固体電解
質膜の他方面に、公知の方法で、30〜40vol%の
Ni−YSZ(ニッケルサーメット)を電解質とほぼ同
様の手法で調製した燃料側電極の構成材料スラリを厚さ
0.2mmに塗布し、その後、(8)大気中1400℃
で5時間焼成して燃料側電極を形成し、(9)単セルを
完成させた。得られた単セルをガスセパレータと積層し
て燃料電池スタックとし、該燃料電池スタックを所定の
箱体に収納して固体電解質型燃料電池を構成した。この
固体電解質型燃料電池を用いて、1000℃に加熱し、
燃料ガスとして水素を、酸化剤ガスとして空気を用いて
発電テストを行った。結果を図3に示す。
Next, (3) the YSZ slurry whose viscosity has been adjusted by adjusting the amount of the residual solvent and carbon beads as the coating porous material are mixed at a mixing ratio of 100: 25. Was spread on a resin sheet coated with a release agent, that is, while controlling the thickness, and molded into a sheet to obtain a green body. (5) Next, the obtained green body was cut into a predetermined shape and dried. At this time, the carbon beads as the coating porous material float on the surface layer portion of the green body because the specific gravity is small. Therefore, the surface layer of the green body is mainly a layer of carbon beads as a coating porous material,
The lower layer is a slurry layer composed of only the solid electrolyte constituent material (YSZ slurry). (6) Next, when this green body is fired at 1450 ° C. for 5 hours in the air, the carbon beads disappear and the porous material made of the constituent material of the solid electrolyte membrane contains the electrode material and the current collector material. A fired body is obtained by laminating an air-side electrode film having a body function and a solid electrolyte membrane having a dense structure composed only of the constituent materials of the solid electrolyte membrane. After gradually cooling the obtained fired body to room temperature,
(7) On the other surface of the solid electrolyte membrane on which the air-side electrode is not provided, 30-40 vol% Ni-YSZ (nickel cermet) is prepared on the other surface of the solid electrolyte membrane by a method substantially similar to that of the electrolyte. The material slurry of the electrode is applied to a thickness of 0.2 mm, and then (8) 1400 ° C. in the atmosphere.
For 5 hours to form a fuel-side electrode, thereby completing (9) a single cell. The obtained single cell was laminated with a gas separator to form a fuel cell stack, and the fuel cell stack was housed in a predetermined box to constitute a solid oxide fuel cell. Using this solid oxide fuel cell, heat to 1000 ° C.
A power generation test was performed using hydrogen as fuel gas and air as oxidant gas. The results are shown in FIG.

【0016】図3から、本実施例によって得られた単セ
ルを用いて構成した固体電解質型燃料電池は、電流密度
と電圧とが正比例関係にあり、発電効率が良好であるこ
とが分かる。本実施例によれば、固体電解質膜の構成材
料スラリと、電極材料および集電体材料がコートされた
カーボンビーズとの混合物をシート状に成形してグリー
ン体とし、これを乾燥した後、焼成することにより、一
段の焼成工程で、グリーン体の表層部に浮上した前記カ
ーボンビーズが消失し、電極材料および集電体材料を含
有した多孔質部からなる、集電体機能を有する電極膜
と、緻密質部からなる固体電解質膜とが一体化した積層
体が得られる。従って、製造工程数が減少し、材料の歩
留まり率が向上して製造コストが大幅に低減する。ま
た、前記グリーン体は、基本的に電解質材料を中心に構
成されているので、焼成時の収縮が均一となり、従来法
で必要であった仮焼等の前処理を行うことなく、機械強
度が大きい焼成体を得ることができる。従って固体電解
質膜を従来よりも薄くすることもできる。
From FIG. 3, it can be seen that the solid oxide fuel cell constituted by using the single cell obtained according to the present embodiment has a direct proportional relationship between the current density and the voltage, and has a good power generation efficiency. According to the present embodiment, a mixture of the material slurry of the solid electrolyte membrane and the carbon beads coated with the electrode material and the current collector material is formed into a sheet to form a green body, which is dried and then fired. By doing so, in one firing step, the carbon beads floating on the surface layer portion of the green body disappear, comprising an electrode material and a porous portion containing a current collector material, an electrode film having a current collector function and Thus, a laminate in which the solid electrolyte membrane composed of the dense portion is integrated is obtained. Therefore, the number of manufacturing steps is reduced, the yield rate of the material is improved, and the manufacturing cost is significantly reduced. Further, since the green body is basically composed mainly of an electrolyte material, the shrinkage during firing becomes uniform, and the mechanical strength is reduced without performing pre-treatment such as calcination required in the conventional method. A large fired body can be obtained. Therefore, the solid electrolyte membrane can be made thinner than before.

【0017】本実施例において、グリーン体とは、固体
電解質膜の構成材料をシート状に成形した、焼成前のも
のをいう。グリーン体における、主としてコート多孔化
材からなる上層部の厚さは、該コート多孔化材の混合量
およびYSZスラリの粘度を加減することにより調節す
ることができる。本実施例ではコート多孔化材層の厚み
を、例えばグリーン体状態で1.0mmとした。電極材
料と集電体材料の組成は、前者がより電極活性であり、
後者は高電気伝導性の組成である。
In this embodiment, the green body refers to a material obtained by molding the constituent material of the solid electrolyte membrane into a sheet shape before firing. In the green body, the thickness of the upper layer mainly composed of the coated porous material can be adjusted by adjusting the mixing amount of the coated porous material and the viscosity of the YSZ slurry. In this example, the thickness of the coated porous material layer was, for example, 1.0 mm in a green body state. For the composition of the electrode material and the current collector material, the former is more electrode active,
The latter is a composition having high electric conductivity.

【0018】本実施例において、固体電解質膜と同一材
料で作成された骨格と一体焼成する電極膜として空気側
電極を示したが、燃料側電極でも差し支えない。
In this embodiment, the air-side electrode is shown as an electrode film which is integrally fired with a skeleton made of the same material as the solid electrolyte membrane, but a fuel-side electrode may be used.

【0019】[0019]

【発明の効果】本発明によれば、固体電解質膜となる緻
密質部と、該緻密質部に積層される、電極および集電体
材料を含有する多孔質部とを同一材料で構成し、一体焼
成することにより、収縮工程が均一となるので、歪み等
のない強固な単電池構成体が得られる。また、材料の歩
留まり率が向上するので、製作コストを大幅に低減する
ことができる。
According to the present invention, the dense part to be the solid electrolyte membrane and the porous part containing the electrode and the current collector material laminated on the dense part are formed of the same material, By integrally firing, the shrinking step becomes uniform, so that a strong unit cell structure without distortion or the like can be obtained. Further, since the yield rate of the material is improved, the manufacturing cost can be significantly reduced.

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

【図1】本発明の一実施例を示す製作フロー図。FIG. 1 is a manufacturing flowchart showing one embodiment of the present invention.

【図2】本発明の一実施例におけるコート多孔化材の断
面図。
FIG. 2 is a sectional view of a coated porous material according to one embodiment of the present invention.

【図3】本発明の一実施例における燃料電池の発電効果
を示す図。
FIG. 3 is a diagram showing a power generation effect of a fuel cell according to one embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1…YSZグリーン、2…コート多孔化材、3…緻密質
部(固体電解質膜)、4…多孔質部(電極膜)、5…カ
ーボンビーズ、6…集電体材料層、7…電極材料層。
DESCRIPTION OF SYMBOLS 1 ... YSZ green, 2 ... Coat porous material, 3 ... Dense part (solid electrolyte membrane), 4 ... Porous part (electrode film), 5 ... Carbon beads, 6 ... Current collector material layer, 7 ... Electrode material layer.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 固体電解質膜の表面に電極膜を形成する
固体電解質型燃料電池の単電池製造法において、固体電
解質膜の構成材料スラリと、電極材料および集電体材料
がコートされた多孔化材粒子とを混合し、該混合物をシ
ート状に成形し、乾燥した後、焼成することにより、固
体電解質膜としての緻密質部と、該緻密質部に積層され
た集電機能を有する電極膜となる多孔質部とを形成し、
次いで、前記緻密質部の他方面に前記集電機能を有する
電極膜と対をなす電極膜を形成することを特徴とする固
体電解質型燃料電池の単電池製造法。
1. A method for producing a solid electrolyte fuel cell unit cell comprising forming an electrode film on the surface of a solid electrolyte membrane, comprising a slurry of constituent materials of the solid electrolyte membrane and a porous material coated with an electrode material and a current collector material. Material particles, the mixture is formed into a sheet, dried, and fired to form a dense portion as a solid electrolyte membrane, and an electrode film having a current collecting function laminated on the dense portion. To form a porous portion,
Next, an electrode film paired with the electrode film having a current collecting function is formed on the other surface of the dense portion, and a method for manufacturing a unit cell of a solid oxide fuel cell is provided.
JP5336789A 1993-12-28 1993-12-28 Single cell manufacturing method of solid oxide fuel cell Expired - Fee Related JP2957404B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5336789A JP2957404B2 (en) 1993-12-28 1993-12-28 Single cell manufacturing method of solid oxide fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5336789A JP2957404B2 (en) 1993-12-28 1993-12-28 Single cell manufacturing method of solid oxide fuel cell

Publications (2)

Publication Number Publication Date
JPH07201342A JPH07201342A (en) 1995-08-04
JP2957404B2 true JP2957404B2 (en) 1999-10-04

Family

ID=18302707

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5336789A Expired - Fee Related JP2957404B2 (en) 1993-12-28 1993-12-28 Single cell manufacturing method of solid oxide fuel cell

Country Status (1)

Country Link
JP (1) JP2957404B2 (en)

Also Published As

Publication number Publication date
JPH07201342A (en) 1995-08-04

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