JPH01267964A - Fuel battery with solid electrolyte - Google Patents
Fuel battery with solid electrolyteInfo
- Publication number
- JPH01267964A JPH01267964A JP63097656A JP9765688A JPH01267964A JP H01267964 A JPH01267964 A JP H01267964A JP 63097656 A JP63097656 A JP 63097656A JP 9765688 A JP9765688 A JP 9765688A JP H01267964 A JPH01267964 A JP H01267964A
- Authority
- JP
- Japan
- Prior art keywords
- fuel
- cell
- solid electrolyte
- unitary
- pipe
- 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
Links
- 239000000446 fuel Substances 0.000 title claims abstract description 68
- 239000007784 solid electrolyte Substances 0.000 title claims description 10
- 239000001301 oxygen Substances 0.000 claims abstract description 18
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 18
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000004020 conductor Substances 0.000 claims description 11
- 239000000758 substrate Substances 0.000 claims description 7
- 238000010248 power generation Methods 0.000 abstract description 9
- 239000000126 substance Substances 0.000 abstract 1
- 239000007787 solid Substances 0.000 description 9
- 238000005192 partition Methods 0.000 description 7
- 238000010586 diagram Methods 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 4
- 238000003411 electrode reaction Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- -1 oxygen ion Chemical class 0.000 description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007772 electrode material Substances 0.000 description 2
- 229910044991 metal oxide Inorganic materials 0.000 description 2
- 150000004706 metal oxides Chemical class 0.000 description 2
- 239000011149 active material Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000002800 charge carrier Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 239000011532 electronic conductor Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229910052746 lanthanum Inorganic materials 0.000 description 1
- FZLIPJUXYLNCLC-UHFFFAOYSA-N lanthanum atom Chemical compound [La] FZLIPJUXYLNCLC-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/241—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
- H01M8/2425—High-temperature cells with solid electrolytes
- H01M8/243—Grouping of unit cells of tubular or cylindrical configuration
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel 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
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、固体電解質型燃料電池に係り、特に発電出力
密度の高い固体電解質型燃料電池に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a solid oxide fuel cell, and particularly to a solid oxide fuel cell with a high power generation output density.
〔従来の技術]
最近、低公害のエネルギー源として注目を集めている燃
料電池は、起電反応の源となる、活物質としての燃料と
酸化剤とを外部がら連続的に供給して電気エネルギーと
して取り出すとともに、反応生成物を連続的に排出する
ことができる電池である。このような燃料電池のなかで
電解質の漏洩の恐れがなく、反応速度が大きいとして注
目されているのが固体電解質型燃料電池であり、基体管
の外表面に酸素極、固体電解質および燃料極が順次積層
された単セルを基板上に多数配列したものが知られてい
る。このような従来技術に関するものとして、例えば特
開昭61−101971号公報等があげられる。[Prior Art] Fuel cells, which have recently attracted attention as a low-pollution energy source, generate electrical energy by continuously supplying fuel as an active material and oxidizing agent from the outside, which are the sources of electromotive reactions. This is a battery that can take out the reaction products as well as continuously discharge the reaction products. Among these types of fuel cells, solid oxide fuel cells are attracting attention because they have no fear of electrolyte leakage and have a high reaction rate. It is known that a large number of sequentially stacked single cells are arranged on a substrate. Examples of such prior art include Japanese Patent Application Laid-Open No. 101971/1983.
しかしながら上記従来技術は、単セルを基板上に多数配
列し、各単セルの電極をインターコネクタ等で直列また
は並列に連結したものであり、単セルを配置するための
面積の広い基板が必要であるばかりでなく、単位面積当
たりの発電出力、すなわち発電出力密度が低いという問
題があった。However, in the above-mentioned conventional technology, a large number of single cells are arranged on a substrate, and the electrodes of each single cell are connected in series or parallel with interconnectors, etc., and a large substrate area is required for arranging the single cells. In addition, there was a problem that the power generation output per unit area, that is, the power generation output density was low.
本発明の目的は、上記従来技術の問題点を解決し、発電
出力密度が高い固体電解質型燃料電池を提供することに
ある。An object of the present invention is to solve the problems of the prior art described above and to provide a solid oxide fuel cell with high power generation output density.
上記目的を達成するため本発明は一電子導電体からなる
酸素極と、酸素イオン導電性の固体電解質と、電子導電
体からなる燃料極とをガス透過性の基体管に積層した単
セルを基板上に多数配列した固体電解質型燃料電池にお
いて、前記基体管を一端が閉塞された円筒状とし、その
直径および高さを段階的に変化させて単セルを構成し、
この単セルを同心円状に多数配列したことを特徴とする
ものである。In order to achieve the above object, the present invention provides a single cell substrate in which an oxygen electrode made of a one-electron conductor, an oxygen ion conductive solid electrolyte, and a fuel electrode made of an electron conductor are laminated on a gas-permeable base tube. In the solid oxide fuel cell arranged in large numbers on the top, the base tube is formed into a cylindrical shape with one end closed, and the diameter and height of the base tube are changed in stages to constitute a single cell,
It is characterized by having a large number of these single cells arranged concentrically.
−・端が閉塞された円筒状の基体管の直径および高さを
段階的に変化させて単セルを作成し、該単セルを基板上
に同心円状に配列して燃料電池スタックを形成したこと
により、基板単位面積当たりの単セル数が増加し、固体
電解質型燃料電池全体としての発電出力密度が高くなる
。−・Single cells were created by changing the diameter and height of a cylindrical base tube with a closed end in stages, and the single cells were arranged concentrically on a substrate to form a fuel cell stack. As a result, the number of single cells per unit area of the substrate increases, and the power generation output density of the solid oxide fuel cell as a whole increases.
本発明において電子導電性を有する固体電解質とは、例
えば4価の金属酸化物に2価または3価の金属酸化物を
固溶させた蛍石型酸化物等があげられ、代表的にはZr
0z Yz 03 (YSZ)、CeO□−CaO
等が知られている。また、酸素極または燃料極として使
用される電子導電体とは、1000°C前後の高温で化
学的に安定で、熱膨張率が前記固体電解質の熱膨張率に
近く、かつ電子導電性を有するものであり、酸素極とし
て例えば、高温の酸素雰囲気で安定なLaCo0=、L
aCr(h等の複合酸化物が、燃料極として例えば、高
温の還元雰囲気で安定なCoN i −Z ro□、N
+ −A1等があげられる。In the present invention, the solid electrolyte having electronic conductivity includes, for example, a fluorite-type oxide in which a divalent or trivalent metal oxide is dissolved in a tetravalent metal oxide, and a typical example is Zr.
0z Yz 03 (YSZ), CeO□-CaO
etc. are known. In addition, the electronic conductor used as the oxygen electrode or fuel electrode is chemically stable at high temperatures of around 1000°C, has a coefficient of thermal expansion close to that of the solid electrolyte, and has electronic conductivity. As an oxygen electrode, for example, LaCo0=, L, which is stable in a high temperature oxygen atmosphere.
Composite oxides such as aCr(h) can be used as fuel electrodes, such as CoN i -Z ro□, N
+ -A1 etc. are mentioned.
次に、本発明を実施例によりさらに詳細に説明する。 Next, the present invention will be explained in more detail with reference to Examples.
第1A図は、本発明の一実施例を示す固体電解質型燃料
電池を構成する単セルの断面図、第1B図は、第1A図
の開口部の詳細図である。この単セルは、底付き円筒状
の多孔質からなる基体管lと、該基体管lの外表面に順
次薄膜上に積層された、ランタン系の、例えばLaCo
Q、からなる酸素極(以下、酸素側電極という)3、B
i、0yYzox系の、例えば(Y−Ox )。、zs
(BizO,+)。、ヮ、からなる固体電解質2および
ニッケル系の、例えばN1p−YSZからなる燃料極(
以下、燃料側電極という)4とから主として構成されて
いる。単セルの開口部近傍には、発生した電気エネルギ
ーを効率よく取り出すために、基体管Iの表面が露出し
た、何も積層されていない部分と、横断面円形の円周の
半周に外表面に積層された電極材を、残り半周に内表面
に積層された電極材を延長してそれぞれ単独に積層した
部分が設けられている。単セルに積層される酸素側電極
3と燃料側電極4はその単セルの燃料電池スタックにお
ける配列位置により、その積層位置が異なり、単セルの
外側が空気流路となる場合は外表面に酸素側電極3、内
表面に燃料側電極4がそれぞれ積層され、単セルの外表
面が燃料流路となる場合は外表面に燃料側電極4、内表
面に酸素側電極3がそれぞれ積層される。このような単
セルが直径および高さの異なる基体管を用いて多数作成
され、これを組み合わせて燃料電池スタックが形成され
る。FIG. 1A is a sectional view of a single cell constituting a solid oxide fuel cell showing one embodiment of the present invention, and FIG. 1B is a detailed view of the opening shown in FIG. 1A. This single cell consists of a bottomed cylindrical porous base tube l, and a lanthanum-based material such as LaCo, which is sequentially laminated on the outer surface of the base tube l on a thin film.
Q, an oxygen electrode (hereinafter referred to as the oxygen side electrode) 3, B
i, 0yYzox system, for example (Y-Ox). ,zs
(BizO, +). , ヮ, and a nickel-based fuel electrode (for example, N1p-YSZ).
(hereinafter referred to as the fuel side electrode) 4. Near the opening of the single cell, in order to efficiently take out the generated electrical energy, there is a part where the surface of the base tube I is exposed and where nothing is laminated, and an outer surface half around the circumference of the circle with a circular cross section. In the remaining half of the laminated electrode material, a portion is provided in which the electrode material laminated on the inner surface is extended and individually laminated. The stacking positions of the oxygen-side electrode 3 and fuel-side electrode 4 that are stacked on a single cell differ depending on the arrangement position of the single cell in the fuel cell stack. A side electrode 3 and a fuel side electrode 4 are laminated on the inner surface, respectively, and when the outer surface of the unit cell becomes a fuel flow path, the fuel side electrode 4 is laminated on the outer surface and the oxygen side electrode 3 is laminated on the inner surface. A large number of such single cells are created using base tubes of different diameters and heights, and these are combined to form a fuel cell stack.
第2図は、単セルを多数組み合わせた、本発明の一実施
例を示す燃料電池スタックの説明図、第3A図および第
3B図は、それぞれ第2図の空気送給管7の管配列方向
の断面図およびこれと直交する面、すなわち燃料送給管
9の配列方向の断面図である。FIG. 2 is an explanatory diagram of a fuel cell stack showing one embodiment of the present invention in which a large number of single cells are combined, and FIGS. 3A and 3B are respectively the tube arrangement directions of the air supply pipes 7 in FIG. 2. FIG. 2 is a cross-sectional view of FIG.
第3A図および第3B図において、この燃料電池スタッ
クは、電気絶縁性のセラミックスからなるフランジvi
6と、該フランジ板6に同心円状に嵌挿された単セル5
a、5b、5Cおよび5dと、空気送給管7と、該空気
送給管7から分岐され前記フランジ板6を貫通して単セ
ル5aの基体管1内および単セル5bと50の間にそれ
ぞれ空気を送る空気管8と、燃料送給管9と、該燃料送
給管9から分岐され隔壁11および11■記フランジ仮
6を貫通して単セル5aと5bの間および単セル5Cと
5dの間にそれぞれ燃料を送る燃料管10とから主とし
て構成されている。空気管8および燃斜管10は共に空
気および燃料を前記単セルの先端部に送るためにその先
端は各単セルの先端部までのびており、燃料管IOの隔
壁I″lとフランジ板6との間は二重管で、内管が燃料
供給流路、外管が燃料戻り流路となっている。また、前
記隔壁11は、空気送給管7と燃料送給管9との間に設
けられ、空気層と燃料層とを隔離している。なお、12
は燃料管10の外管に設けられた燃料孔である。3A and 3B, this fuel cell stack has a flange vi made of electrically insulating ceramics.
6, and a single cell 5 fitted concentrically into the flange plate 6.
a, 5b, 5C and 5d, an air supply pipe 7, which is branched from the air supply pipe 7 and passes through the flange plate 6, into the base pipe 1 of the single cell 5a and between the single cells 5b and 50. An air pipe 8 that sends air, a fuel feed pipe 9, and a pipe branched from the fuel feed pipe 9 and passing through the partition wall 11 and temporary flange 6 marked 11) between the single cells 5a and 5b and between the single cells 5C. 5d, and a fuel pipe 10 that sends fuel during each period. Both the air pipe 8 and the fuel diagonal pipe 10 have their tips extending to the tips of each single cell in order to send air and fuel to the tips of the single cells, and the partition wall I″l of the fuel pipe IO and the flange plate 6 The space between the air supply pipe 7 and the fuel supply pipe 9 is a double pipe, with the inner pipe serving as a fuel supply passage and the outer pipe serving as a fuel return passage. The air layer and the fuel layer are separated from each other.
is a fuel hole provided in the outer tube of the fuel pipe 10.
このような構成において、空気送給管7および空気管8
を経て単セル5aの基体管1内および単セル5bと50
の間に供給された空気Aは、単セル5aの基体管1およ
び単セル5bと50の間の空間を満たした後、フランジ
板6と空気管8との隙間から単セル外へ流出する。一方
、燃料送給管9および燃料管10を経て単セル5aと5
bの間および単セル5cと5dの間に送給された燃料、
例えば水素Fは、それぞれの単セルの間の空間を満たし
た後、フランジ板6と燃料管100間を通り、二重管と
なっている燃料管1oの外管を流れ、隔壁11の燃料送
給管9側へ流出する。このようにして空気Aと水素Fが
供給された各単セルの電極間では電極反応が生じる。例
えば、空気Aの流路に面した単セル5bの外表面の酸素
側電極3では、空気A中の酸素が外部回路から電子を受
は取って酸素イオンとなり、その内側に積層された固体
電解質2に入って荷電担体となる。一方、この単セル5
bの基体管1内は燃料である水素Fの流路となり、水素
Fは前記基体管1を介してその外表面に積層さた燃料側
電極4へ流入し、ここで前記固体電解f2中の酸素イオ
ンと反応して水を生成し、外部へ電子を放出する。他の
単セルにおいても同様の電極反応が生じて電気エネルギ
ーが発生し、フランジ板6内の導電材に集電された後、
外部に取り出される。なお、単セル5dの外側は隔壁1
1により燃料層と隔離された空気層であり、前記単セル
5dの外表面の酸素側電極3へはこの空気層中の酸素が
取り入れられる。また、燃料管10の外管に設けられた
燃料孔12は、電極反応に使用されなかった余剰燃料の
一部が該燃料孔12から空気層中に漏洩して燃焼し、空
気温度を高温に維持するためのものである。In such a configuration, the air supply pipe 7 and the air pipe 8
through the base tube 1 of the single cell 5a and the single cells 5b and 50.
The air A supplied during this period fills the base tube 1 of the unit cell 5a and the space between the unit cells 5b and 50, and then flows out of the unit cell through the gap between the flange plate 6 and the air tube 8. On the other hand, the single cells 5a and 5
fuel fed between b and between single cells 5c and 5d,
For example, after hydrogen F fills the space between each single cell, it passes between the flange plate 6 and the fuel pipe 100, flows through the outer pipe of the double pipe fuel pipe 1o, and flows through the partition wall 11 for fuel delivery. It flows out to the supply pipe 9 side. An electrode reaction occurs between the electrodes of each single cell to which air A and hydrogen F are supplied in this manner. For example, at the oxygen side electrode 3 on the outer surface of the single cell 5b facing the flow path of air A, oxygen in the air A receives and takes electrons from an external circuit to become oxygen ions, and the solid electrolyte layered inside 2 and becomes a charge carrier. On the other hand, this single cell 5
The inside of the base tube 1 of b becomes a flow path for hydrogen F, which is a fuel, and the hydrogen F flows through the base tube 1 to the fuel-side electrode 4 laminated on its outer surface, where it is absorbed into the solid electrolyte f2. It reacts with oxygen ions to produce water and releases electrons to the outside. Similar electrode reactions occur in other single cells to generate electrical energy, which is collected by the conductive material in the flange plate 6, and then
taken outside. Note that the outer side of the single cell 5d is the partition wall 1.
This is an air layer separated from the fuel layer by 1, and oxygen in this air layer is taken into the oxygen side electrode 3 on the outer surface of the single cell 5d. Further, the fuel hole 12 provided in the outer tube of the fuel tube 10 allows a portion of surplus fuel that is not used for the electrode reaction to leak into the air layer from the fuel hole 12 and burn, raising the air temperature to a high temperature. It is intended to be maintained.
第4A図および第4B図は、フランジ板6における集電
用導電材料の配置およびその結線方法を示す説明図であ
る。集電用導電材料工3はそれぞれ同心円状に配置され
ており、第4A図は直列結線を、第4B図は並列結線を
示している。各単セルで発生した電気エネルギーは、単
セルを支持するフランジ板6に蒸着された集電用導電材
料13に集電された後、外部に取り出される。なお、集
電用導電材料13の結線方法は各々燃料電池スタック内
で任意に選択することができる。FIGS. 4A and 4B are explanatory diagrams showing the arrangement of the current collecting conductive material on the flange plate 6 and the method of connecting the conductive materials. The current collecting conductive materials 3 are arranged concentrically, and FIG. 4A shows a series connection, and FIG. 4B shows a parallel connection. The electrical energy generated in each unit cell is collected by a current collecting conductive material 13 deposited on the flange plate 6 that supports the unit cell, and then taken out to the outside. Note that the method of connecting the current collecting conductive material 13 can be arbitrarily selected within each fuel cell stack.
本実施例によれば、単セルの形状を一端が閉塞された円
筒状にし、その直径および高さを段階的に変化させたの
で、同心円状に多数組み合わせることができ、単位面積
当たりの単セル数が増加し、発電出力密度が高くなる。According to this example, the shape of the single cell is cylindrical with one end closed, and the diameter and height are changed in stages, so that a large number of single cells can be combined concentrically, and the single cell per unit area is The number increases, and the power generation output density increases.
また、隔壁11により燃料と空気との無用な接触を避け
るとともに、燃料孔I2から燃料の一部を空気側に洩ら
すようにしたので、この燃料が燃焼することにより空気
の温度を高温に維持することができ燃料の利用率が向上
する。In addition, unnecessary contact between the fuel and air is avoided by the partition wall 11, and a portion of the fuel leaks to the air side from the fuel hole I2, so that the temperature of the air is maintained at a high temperature by burning this fuel. It can improve fuel utilization.
本発明によれば、単セルを同心円状に多数配列して燃料
電池スタックを構成したので、単位面積当たりの単セル
数が増加し、発電出力密度が高(なる。According to the present invention, since a fuel cell stack is constructed by arranging a large number of single cells concentrically, the number of single cells per unit area increases, resulting in a high power generation output density.
第1A図は、本発明の一実施例を示す固体電解質型燃料
電池を構成する単セルの断面図、第1B図は、第1A図
の部分詳細図、第2図は、本発明の一実施例を示す固体
電解質型燃料電池の燃料電池スタックの説明図、第3A
図および第3B図は、それぞれ第2図の断面図、第4A
図および第4B図は、それぞれ燃料電池スタックのフラ
ンジ板に蒸着された集電用°導電材料の結線方法例を示
す図である。
5a〜5d・・・単セル、6・・・フランジ板、7・・
・空気送給管、9・・・燃料送給管、11・・・隔壁。
代理人 弁理士 川 北 武 長
2:固体電解質
3:酸素側電極
4:燃料側電極
5a〜5d:単セル
6:フランジ板
7:空気送給管
8:空気管
9:燃料送給管
10: fi料斜
管1:隔壁
12:燃料孔
ζ
り
ζ
/FIG. 1A is a sectional view of a single cell constituting a solid oxide fuel cell showing one embodiment of the present invention, FIG. 1B is a detailed view of a portion of FIG. 1A, and FIG. 2 is an embodiment of the present invention. Explanatory diagram of a fuel cell stack of a solid oxide fuel cell showing an example, No. 3A
Figure 3B is a sectional view of Figure 2 and Figure 4A, respectively.
4B and 4B are diagrams each showing an example of a method for connecting a conductive material for current collection deposited on a flange plate of a fuel cell stack. 5a to 5d... Single cell, 6... Flange plate, 7...
- Air supply pipe, 9... Fuel supply pipe, 11... Partition wall. Agent Patent Attorney Takeshi Kawakita 2: Solid electrolyte 3: Oxygen side electrode 4: Fuel side electrode 5a to 5d: Single cell 6: Flange plate 7: Air supply pipe 8: Air pipe 9: Fuel supply pipe 10: Fuel diagonal pipe 1: Partition wall 12: Fuel hole ζ /
Claims (1)
の固体電解質と、電子導電体からなる燃料極とをガス透
過性の基体管に積層した単セルを基板上に多数配列した
固体電解質型燃料電池において、前記基体管を一端が閉
塞された円筒状とし、その直径および高さを段階的に変
化させて単セルを構成し、この単セルを同心円状に多数
配列したことを特徴とする固体電解質型燃料電池。(1) A solid electrolyte in which a large number of single cells are arranged on a substrate, in which an oxygen electrode made of an electron conductor, an oxygen ion conductive solid electrolyte, and a fuel electrode made of an electron conductor are stacked on a gas-permeable base tube. type fuel cell, characterized in that the base tube has a cylindrical shape with one end closed, the diameter and height of the base tube are changed stepwise to constitute a single cell, and a large number of these single cells are arranged concentrically. Solid electrolyte fuel cell.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63097656A JPH01267964A (en) | 1988-04-20 | 1988-04-20 | Fuel battery with solid electrolyte |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63097656A JPH01267964A (en) | 1988-04-20 | 1988-04-20 | Fuel battery with solid electrolyte |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH01267964A true JPH01267964A (en) | 1989-10-25 |
Family
ID=14198116
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63097656A Pending JPH01267964A (en) | 1988-04-20 | 1988-04-20 | Fuel battery with solid electrolyte |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01267964A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2004093235A1 (en) * | 2003-04-10 | 2004-10-28 | University Of Connecticut | Solid state electrochemical devices |
| FR2877498A1 (en) * | 2004-11-02 | 2006-05-05 | Commissariat Energie Atomique | FUEL CELL MODULE, MANUFACTURING METHOD THEREOF, AND MULTIPLE CONTAINING UNIT. |
| EP1837943A1 (en) * | 2006-03-24 | 2007-09-26 | Institute of Nuclear Energy Research Atomic Energy Council, Executive Yuan | Solid oxide fuel cell of multiple tabular electrodes |
| JP2008519391A (en) * | 2004-11-02 | 2008-06-05 | コミツサリア タ レネルジー アトミーク | Fuel cell module with flexible interconnect |
| US7674543B2 (en) | 2005-11-08 | 2010-03-09 | Institute Of Nuclear Energy Research Atomic Energy Council | Solid oxide fuel cell of multiple tubular electrodes |
-
1988
- 1988-04-20 JP JP63097656A patent/JPH01267964A/en active Pending
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2004093235A1 (en) * | 2003-04-10 | 2004-10-28 | University Of Connecticut | Solid state electrochemical devices |
| FR2877498A1 (en) * | 2004-11-02 | 2006-05-05 | Commissariat Energie Atomique | FUEL CELL MODULE, MANUFACTURING METHOD THEREOF, AND MULTIPLE CONTAINING UNIT. |
| WO2006048574A1 (en) * | 2004-11-02 | 2006-05-11 | Commissariat A L'energie Atomique | Fuel cell module, method for the production thereof and a unit comprises a number thereof |
| JP2008519391A (en) * | 2004-11-02 | 2008-06-05 | コミツサリア タ レネルジー アトミーク | Fuel cell module with flexible interconnect |
| JP2008519392A (en) * | 2004-11-02 | 2008-06-05 | コミツサリア タ レネルジー アトミーク | FUEL CELL MODULE, MANUFACTURING METHOD THEREOF, AND UNIT INCLUDING MULTIPLE MODULES |
| US7887959B2 (en) | 2004-11-02 | 2011-02-15 | Commissariat A L'energie Atomique | Fuel cell module with flexible interconnects |
| US8709675B2 (en) | 2004-11-02 | 2014-04-29 | Commissariat A L'energie Atomique | Fuel cell module, manufacturing method thereof and unit containing several of the latter |
| US7674543B2 (en) | 2005-11-08 | 2010-03-09 | Institute Of Nuclear Energy Research Atomic Energy Council | Solid oxide fuel cell of multiple tubular electrodes |
| EP1837943A1 (en) * | 2006-03-24 | 2007-09-26 | Institute of Nuclear Energy Research Atomic Energy Council, Executive Yuan | Solid oxide fuel cell of multiple tabular electrodes |
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