JPH02242564A - Solid electrolyte fuel cell - Google Patents

Solid electrolyte fuel cell

Info

Publication number
JPH02242564A
JPH02242564A JP1064401A JP6440189A JPH02242564A JP H02242564 A JPH02242564 A JP H02242564A JP 1064401 A JP1064401 A JP 1064401A JP 6440189 A JP6440189 A JP 6440189A JP H02242564 A JPH02242564 A JP H02242564A
Authority
JP
Japan
Prior art keywords
solid electrolyte
gas
fuel cell
cell
porous sheet
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
JP1064401A
Other languages
Japanese (ja)
Inventor
Yasuo Miyake
泰夫 三宅
Toshihiko Saito
俊彦 齋藤
Yukinori Akiyama
幸徳 秋山
Shuzo Murakami
修三 村上
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric Co 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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP1064401A priority Critical patent/JPH02242564A/en
Publication of JPH02242564A publication Critical patent/JPH02242564A/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
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0271Sealing or supporting means around electrodes, matrices or membranes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/10Fuel cells with solid electrolytes
    • H01M8/12Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
    • H01M2008/1293Fuel cells with solid oxide electrolytes
    • 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
    • H01M2300/0065Solid electrolytes
    • H01M2300/0068Solid electrolytes inorganic
    • H01M2300/0071Oxides
    • H01M2300/0074Ion conductive at high temperature
    • 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)

Abstract

PURPOSE:To prevent any damage of a cell due to a heat cycle and retain an excellent sealing property by composing a gas sealing part with a heat resisting porous sheet, in which a seal material is impregnatorily retained, interposed in a contact surface between a gas separation plate and a solid electrolyte. CONSTITUTION:A plate state cell 1 is composed of: a solid electrolyte 2 composed of an elaborate baked body of zirconia stabilized with 8% yttria, an anode electrode 3 composed of Ni-ZrO2 thermet, and a cathode electrode 4 composed of a perovskite type oxide such as LaCoO3, etc. A solid electrolyte fuel cell is formed with the cell 1 and a gas separation plate 5, in which each reaction gas supply path 3' and 4' is formed in a complexity direction each other on the back of each electrode 3 and 4, laminated each other, and a pas seal part is composed with a heat resisting porous sheet 6, in which a seal material becoming a high viscosity fusing body at a battery operation temperature is impregnated and retained, interposed in the contact surface between the plate 5 and the electrolyte 2. This enables any damage of a cell due to a heat cycle to be prevented, and an excellent seal property to be maintained.

Description

【発明の詳細な説明】 (イ)産業上の利用分野 本発明は固体電解質燃料電池のガスシール構成に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to a gas seal structure for a solid electrolyte fuel cell.

(ロ)従来の技術 固体電解質型燃料電池(以下5OFCという)は、リン
酸型及び溶融炭酸塩型に続く完全固体化した第三世代の
燃料電池として注目されている。
(B) Prior Art Solid oxide fuel cells (hereinafter referred to as 5OFC) are attracting attention as a completely solid-state third generation fuel cell following the phosphoric acid type and molten carbonate type.

この5OFCは酸化物固体(一般にY 20 sで安定
化したZrO,)内の酸素イオン伝導性を利用している
ため電解質損失の問題は全て解消されると共に、作動温
度が約1000℃の高温のため発電効率も高いという特
性を有する。
This 5OFC utilizes the oxygen ion conductivity within the oxide solid (generally ZrO stabilized with Y 20 s), which eliminates all problems of electrolyte loss and allows for high operating temperatures of approximately 1000°C. Therefore, it has the characteristic of high power generation efficiency.

5OFCの形状には円筒型と平板型とがあり、円筒型は
ガスシール面で優れているが、電極の作成にプラズマ溶
射法やEVD法など特殊な技術が必要であり、またその
構成上単セルの大型化が困難で体積当りの出力密度が小
さいなどの欠点がある。一方平板型は電極を塗布法によ
り作成可能で量産性に優れると共に多数のセルを積層し
たスタック構造として体積当りの出力密度を大きくてき
るという利点がある反面、ガス分離板と固体電解質間の
ガスシールがむつかしいという問題をか)えている。
There are two types of 5OFC shapes: cylindrical and flat. The cylindrical shape is superior in terms of gas sealing, but it requires special techniques such as plasma spraying and EVD to create electrodes, and its structure makes it difficult to use. It has drawbacks such as difficulty in increasing the size of the cell and low output density per volume. On the other hand, the flat plate type has the advantage of being superior in mass production as the electrodes can be created by a coating method, and has the advantage of having a stacked structure in which many cells are stacked, increasing the output density per volume. The problem is that the seal is difficult.

平板型S OF Cのガスシール法として従来よりセラ
ミックスセメントの使用が検討されているが、セラミッ
クスセメントは固体シールであり電池各構成材と熱膨張
率が異なるため熱サイクルによってヒビ割れし、シール
性の不良によりガスのリークもしくはクロスリークを生
じるという問題があった。
The use of ceramic cement has been considered as a gas sealing method for flat-plate SOF Cs, but since ceramic cement is a solid seal and has a different coefficient of thermal expansion than each component of the battery, it can crack due to thermal cycles, resulting in poor sealing performance. There has been a problem in that gas leaks or cross leaks occur due to defects in the gas.

(ハ)発明が解決しようとする課題 本発明は平板型5OFCのシール構成を改善して前記問
題点を解消するものである。
(c) Problems to be Solved by the Invention The present invention solves the above-mentioned problems by improving the seal structure of a flat plate type 5OFC.

(ニ)問題点を解決するための手段 本発明はアノード極・固体電解質・カソード極からなる
平板状セルと、前記各極背面に互に交錯方向の各反応ガ
ス供給路を形成したガス分離板とを交互に積重してなる
固体電解質燃料電池において、前記ガス分離板と固体電
解質との接触面に、電池作動温度で高粘度の融体となる
シール材が含浸保持さツアーだ耐熱性多孔質シートを介
在させてガスシール部を構成したものである。
(d) Means for Solving the Problems The present invention comprises a flat cell consisting of an anode, a solid electrolyte, and a cathode, and a gas separation plate in which reaction gas supply channels in intersecting directions are formed on the back surface of each of the electrodes. In a solid electrolyte fuel cell, the contact surface between the gas separation plate and the solid electrolyte is impregnated with a sealing material that becomes a highly viscous melt at the cell operating temperature. The gas seal part is constructed by interposing a quality sheet.

(ホ)作用 本発明ではシール用融体が耐熱性多孔質シートに含浸保
持されているため、スタックの振動や傾きに対して融体
のがたよりがなくなると共に、シール材がセラミックス
セメントのような固体でないため熱サイクルによるセル
の損傷を防止し良好なシール性を維持する。
(E) Function In the present invention, the sealing melt is impregnated and retained in the heat-resistant porous sheet, so the melt does not wobble due to vibration or tilt of the stack, and the sealing material is similar to ceramic cement. Since it is not solid, it prevents cell damage due to thermal cycles and maintains good sealing performance.

(へ)実施例 第1図は本発明5OFCスタツクの要部分解斜面図、第
2図は同上の要部拡大断面図を示す。
(f) Example FIG. 1 is an exploded perspective view of the essential parts of the 5 OFC stack of the present invention, and FIG. 2 is an enlarged sectional view of the essential parts of the same.

平板状セル(1)は、8%イツトリアで安定化したジル
コニアの緻密な焼成体からなる固体電解質(2)と、N
i−ZrO2サーメットからなるアノード極(3)と、
L a Co Osなどのペロブスカイト型酸化物から
なるカソード極(41)とで構成さメする。
The flat cell (1) consists of a solid electrolyte (2) consisting of a dense sintered body of zirconia stabilized with 8% ittria, and a N
an anode pole (3) made of i-ZrO2 cermet;
It is composed of a cathode electrode (41) made of a perovskite type oxide such as L a Co Os.

固体電解質(2)は外寸10 QmmX 10 Qmm
、’厚さQ 、 3 mmで、この固体電解質には、表
裏互に交錯する方向において対向する二辺に夫々中5m
mのマスク(厚みQ 、 2mm )を予め配し、アノ
ード極(3)及びカソード極(4)を電解質の表裏各面
に夫々Q 、 2mm厚で塗布して後マスクを取除く。
Solid electrolyte (2) has an outer dimension of 10 Qmm x 10 Qmm
, 'Thickness Q is 3 mm, and this solid electrolyte has a thickness of 5 m on each side facing each other in the direction in which the front and back intersect with each other.
A mask (thickness Q, 2 mm) is placed in advance, and an anode electrode (3) and a cathode electrode (4) are applied to each of the front and back surfaces of the electrolyte to a thickness of Q, 2 mm, and then the mask is removed.

かくて各tfi(3)(4)の塗布面は90mn+X 
100Inmテあり、対向二辺に夫々5mmX100m
mの非塗布面を残して焼付けられる。
Thus, the coating surface of each tfi(3)(4) is 90m+X
100Inm tape, 5mm x 100m on two opposing sides
It is baked leaving a non-coated surface of m.

これらセル(1)間に介在するガス分離板(5)は、ニ
ッケルクロム合金などの耐熱性金属がらなり、その表裏
各面に互に交錯方向のアノードガス供給路(3)“及び
カソードガス供給路(4)゛を有する。
The gas separation plate (5) interposed between these cells (1) is made of a heat-resistant metal such as a nickel-chromium alloy, and has an anode gas supply path (3) and a cathode gas supply path on each of its front and back surfaces in intersecting directions. It has a path (4).

電池組立時ガス分離板(5)と固体電解質(2)の接触
面一電極(3)(4)の非塗布面一には、電池作動温度
で高粘度の融体となるシール材が含浸保持された耐熱性
多孔質シー) (6)(6)を配置する。
When assembling the battery, the contact surface between the gas separation plate (5) and the solid electrolyte (2) and the uncoated surface of the electrodes (3) and (4) are impregnated with a sealing material that becomes a highly viscous melt at the battery operating temperature. heat-resistant porous sheet) (6) (6) is placed.

この多孔質シー) (G )(6)は、アルミナ・シリ
カの混合体よりなるセラミックスファイバーを加工した
テープ状フェルトて、寸法5mmX1.00mm、厚h
 0 、3 mmである。このシート上に低膨張ホーケ
イ酸ガラス(商品名パイレックスガラス)の粉末を30
 mg/cm2配して1200”Cで溶融含浸し、冷却
後前記のように電池に組込まれる。
This porous sheet (G) (6) is a tape-shaped felt made of ceramic fiber made of a mixture of alumina and silica, and has dimensions of 5 mm x 1.00 mm and a thickness of h.
0.3 mm. On this sheet, powder of low expansion borosilicate glass (trade name: Pyrex glass) is applied for 30 minutes.
It is melt impregnated at 1200''C at a concentration of mg/cm2, and after cooling is assembled into a battery as described above.

尚図示しないが電池の対向周面には夫々アノードガス給
排マニホルド及びカソードガス給排マニホルドが取付け
られる。
Although not shown, an anode gas supply/discharge manifold and a cathode gas supply/discharge manifold are attached to opposing peripheral surfaces of the battery, respectively.

電池は起動に際し所定条件で1000℃まで■−温され
、この昇温により多孔質シート(6)中の含浸ガラスが
高粘度の融体となってガスシール部を構成する。ついで
アノードガスに水素を、カソードガスに空気を夫々用い
、300 mA/cm’で放電した。
When the battery is started, it is heated to 1000 DEG C. under predetermined conditions, and as a result of this temperature increase, the impregnated glass in the porous sheet (6) turns into a highly viscous melt, forming a gas seal section. Then, hydrogen was used as the anode gas and air was used as the cathode gas, and discharge was performed at 300 mA/cm'.

第3図は電池の運転(作動温度1.000’C)と停止
(保存温度常温)を繰返したサイクルテストの結果を示
す特性図で、初期特性は本発明電池(実線)と従来のセ
ラミックスセメントでシールした従来電池(点線)とは
同等であったが、熱サイクルに対する特性劣化率は本発
明電池が約10mV/回程度であるに対し、従来電池で
は約1.20m\77回であった。
Figure 3 is a characteristic diagram showing the results of a cycle test in which the battery was repeatedly operated (operating temperature: 1.000'C) and stopped (storage temperature: room temperature). However, the rate of characteristic deterioration due to heat cycling was about 10 mV/time for the battery of the present invention, while it was about 1.20 m\77 times for the conventional battery. .

このように本発明により熱サイクルに対する劣化が著し
く改善されるが、その理由は本発明シ・−ル材が゛電池
作動時融体となって可熱性多孔質シートに保持さh、良
好なガスシール性を維持すると共に電池停止時固体とな
って多孔質シートにより補強され、いづhの場合も熱膨
張の差を吸収するのでひび割れを生ずることがないため
と考えられる。
As described above, the present invention significantly improves deterioration due to thermal cycles. This is thought to be because it maintains sealing performance, becomes solid when the battery is stopped, is reinforced by the porous sheet, and absorbs the difference in thermal expansion even when the battery is stopped, so no cracks occur.

本実施例では、耐熱性多孔質シー [・とじてアルミナ
とシリカの混合ファイバーを用いたが、多孔質ジルコニ
アフェルトを使用してらよく、又シール材としてガラス
の他にKCl・λ・1g c Il、などの塩化物もし
くはP1〕0・Bi、0.などの酸化物も使用可能であ
る。
In this example, a heat-resistant porous sheet was used, but a mixed fiber of alumina and silica was used, but porous zirconia felt may also be used, and as a sealing material, in addition to glass, KCl. , etc. or P1]0.Bi, 0. Oxides such as can also be used.

(l・)発明の効果 上述の如く本発明によれば、固体電解質とガス分離板と
の接触面に介在するシール材が耐熱性多孔質シートに含
浸保持された融体てあり、従来のセラミ・lクスセメン
トのような固体でないため熱サイクルによるセルの損傷
を防ローすると共に振動や傾きに対しても融体のかたよ
りがなく、長期に亘り良好なシール性を保持してガスの
リークやクロスリークを防止することができる。
(l.) Effects of the Invention As described above, according to the present invention, the sealing material interposed at the contact surface between the solid electrolyte and the gas separation plate is a molten material impregnated and held in a heat-resistant porous sheet, which is different from the conventional ceramic material.・As it is not a solid like lxcement, it prevents cell damage due to heat cycles, and the melt does not shift even when subjected to vibrations or tilting, and maintains good sealing performance over a long period of time, preventing gas leaks. Cross leaks can be prevented.

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

第1図は本発明固体電解質燃料電池の要部分解斜面図、
第2図は同トの要部拡大断面図、第3図は電池の熱サイ
クルによる特性劣化率を比較して示す特性図である。 ]゛セル、2:固体電解質、3、アノード極、−1′カ
ソード極、5:ガス分離板、6゛耐熱性多孔質シート。
FIG. 1 is an exploded perspective view of the main parts of the solid electrolyte fuel cell of the present invention.
FIG. 2 is an enlarged sectional view of the main part of the battery, and FIG. 3 is a characteristic diagram comparing and showing the rate of characteristic deterioration due to thermal cycles of the battery. ]゛Cell, 2: Solid electrolyte, 3: Anode electrode, -1' cathode electrode, 5: Gas separation plate, 6゛Heat-resistant porous sheet.

Claims (3)

【特許請求の範囲】[Claims] (1)アノード極・固体電解質・カソード極からなる平
板状セルと、前記各極背面に互に交錯方向の各ガス供給
路を形成したガス分離板とを交互に積重してなり、前記
ガス分離板と固体電解質との接触面に、電池作動温度で
高粘度の融体となるシール材が含浸保持された耐熱性多
孔質シートを介在させてガスシール部を構成したことを
特徴とする固体電解質燃料電池。
(1) A flat cell consisting of an anode, a solid electrolyte, and a cathode, and a gas separation plate in which gas supply channels in intersecting directions are formed on the back surface of each electrode are stacked alternately, and the gas A solid body characterized in that a gas sealing portion is formed by interposing a heat-resistant porous sheet impregnated with a sealing material that becomes a highly viscous molten material at battery operating temperatures on the contact surface between the separator plate and the solid electrolyte. Electrolyte fuel cell.
(2)前記高粘度の融体となるシール材は、ホーケイ酸
ガラスであることを特徴とする請求項1記載の固体電解
質燃料電池。
(2) The solid electrolyte fuel cell according to claim 1, wherein the sealing material that becomes a high-viscosity melt is porsilicate glass.
(3)前記耐熱性多孔質シートはジルコニア・アルミナ
・シリカ・マグネシアの少くとも1種を含むセラミック
スファイバーのフェルトであることを特徴とする請求項
1記載の固体電解質燃料電池。
(3) The solid electrolyte fuel cell according to claim 1, wherein the heat-resistant porous sheet is a ceramic fiber felt containing at least one of zirconia, alumina, silica, and magnesia.
JP1064401A 1989-03-15 1989-03-15 Solid electrolyte fuel cell Pending JPH02242564A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1064401A JPH02242564A (en) 1989-03-15 1989-03-15 Solid electrolyte fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1064401A JPH02242564A (en) 1989-03-15 1989-03-15 Solid electrolyte fuel cell

Publications (1)

Publication Number Publication Date
JPH02242564A true JPH02242564A (en) 1990-09-26

Family

ID=13257259

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1064401A Pending JPH02242564A (en) 1989-03-15 1989-03-15 Solid electrolyte fuel cell

Country Status (1)

Country Link
JP (1) JPH02242564A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0620608A1 (en) * 1993-04-13 1994-10-19 Murata Manufacturing Co., Ltd. Solid oxide fuel cell and manufacturing process thereof
EP0675557A1 (en) * 1994-03-03 1995-10-04 Murata Manufacturing Co., Ltd. Method of producing a solid oxide fuel cell
KR100701758B1 (en) * 2004-09-03 2007-03-29 마쯔시다덴기산교 가부시키가이샤 Lithium ion secondary battery
JP2009511743A (en) * 2005-10-11 2009-03-19 コミッサリア タ レネルジー アトミーク Stable joint formed by thermal spraying
WO2018155112A1 (en) * 2017-02-27 2018-08-30 日本特殊陶業株式会社 Electrochemical reaction unit and electrochemical reaction cell stack
WO2018155111A1 (en) * 2017-02-27 2018-08-30 日本特殊陶業株式会社 Electrochemical reaction unit, electrochemical reaction cell stack, and production method for electrochemical reaction unit

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63128561A (en) * 1986-11-17 1988-06-01 Mitsubishi Heavy Ind Ltd Gas sealing device
JPS63133457A (en) * 1986-11-25 1988-06-06 Toshiba Corp Fuel cell of molten carbonate

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63128561A (en) * 1986-11-17 1988-06-01 Mitsubishi Heavy Ind Ltd Gas sealing device
JPS63133457A (en) * 1986-11-25 1988-06-06 Toshiba Corp Fuel cell of molten carbonate

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0620608A1 (en) * 1993-04-13 1994-10-19 Murata Manufacturing Co., Ltd. Solid oxide fuel cell and manufacturing process thereof
EP0675557A1 (en) * 1994-03-03 1995-10-04 Murata Manufacturing Co., Ltd. Method of producing a solid oxide fuel cell
KR100701758B1 (en) * 2004-09-03 2007-03-29 마쯔시다덴기산교 가부시키가이샤 Lithium ion secondary battery
JP2009511743A (en) * 2005-10-11 2009-03-19 コミッサリア タ レネルジー アトミーク Stable joint formed by thermal spraying
WO2018155112A1 (en) * 2017-02-27 2018-08-30 日本特殊陶業株式会社 Electrochemical reaction unit and electrochemical reaction cell stack
WO2018155111A1 (en) * 2017-02-27 2018-08-30 日本特殊陶業株式会社 Electrochemical reaction unit, electrochemical reaction cell stack, and production method for electrochemical reaction unit
JPWO2018155112A1 (en) * 2017-02-27 2019-02-28 日本特殊陶業株式会社 Electrochemical reaction unit and electrochemical reaction cell stack
JPWO2018155111A1 (en) * 2017-02-27 2019-02-28 日本特殊陶業株式会社 Electrochemical reaction unit, electrochemical reaction cell stack, and method for producing electrochemical reaction unit
US11289727B2 (en) 2017-02-27 2022-03-29 Morimura Sofc Technology Co., Ltd. Electrochemical reaction unit, electrochemical reaction cell stack, and production method for electrochemical reaction unit

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