JP2001102075A - Solid electrolyte fuel cell - Google Patents

Solid electrolyte fuel cell

Info

Publication number
JP2001102075A
JP2001102075A JP27686799A JP27686799A JP2001102075A JP 2001102075 A JP2001102075 A JP 2001102075A JP 27686799 A JP27686799 A JP 27686799A JP 27686799 A JP27686799 A JP 27686799A JP 2001102075 A JP2001102075 A JP 2001102075A
Authority
JP
Japan
Prior art keywords
fuel cell
solid oxide
oxide fuel
oxygen
containing gas
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.)
Granted
Application number
JP27686799A
Other languages
Japanese (ja)
Other versions
JP4817476B2 (en
Inventor
Takashi Shigehisa
高志 重久
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.)
Kyocera Corp
Original Assignee
Kyocera 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 Kyocera Corp filed Critical Kyocera Corp
Priority to JP27686799A priority Critical patent/JP4817476B2/en
Publication of JP2001102075A publication Critical patent/JP2001102075A/en
Application granted granted Critical
Publication of JP4817476B2 publication Critical patent/JP4817476B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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

Landscapes

  • Fuel Cell (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a solid electrolyte fuel cell which can remove an invalid energy consumption to keep a temperature of the solid electrolyte fuel cell with reducing a starting time in operation by raising a temperature of the solid electrolyte fuel cell in fast speed. SOLUTION: In a solid electrolyte fuel cell 7 constituted by inserting a pipe 9 for guiding gas including oxygen into it with plural accommodating a cylindrical solid electrolyte fuel battery cell 7 constituted by forming an air pole 21 into an inner surface of a solid electrolyte 22 and a fuel electrode 23 into an outer surface of it within a reacting vessel 11, the pipe 9 for guiding gas including oxygen and/or the solid electrolyte fuel cell 7 are arranged with heating elements 31, 41.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、固体電解質型燃料
電池に関し、特に、発熱体を有する固体電解質型燃料電
池に関する。
The present invention relates to a solid oxide fuel cell, and more particularly, to a solid oxide fuel cell having a heating element.

【0002】[0002]

【従来技術】固体電解質型燃料電池は、図1に示すよう
に、反応容器1内に、酸素含有ガス室仕切板2、燃焼室
仕切板3、燃料ガス室仕切板5を用いて酸素含有ガス室
A、燃焼室B、反応室C、燃料ガス室Dが形成されてい
る。
2. Description of the Related Art As shown in FIG. 1, a solid oxide fuel cell uses an oxygen-containing gas chamber partition plate 2, a combustion chamber partition plate 3, and a fuel gas chamber partition plate 5 in a reaction vessel 1. A chamber A, a combustion chamber B, a reaction chamber C, and a fuel gas chamber D are formed.

【0003】反応容器1内には、複数の有底筒状の固体
電解質型燃料電池セル7が収容されており、これらの固
体電解質型燃料電池セル7は、燃焼室仕切板3に形成さ
れたセル挿入孔に挿入固定されており、また、その内部
には酸素含有ガス室仕切板2に固定された酸素含有ガス
導入管9の一端が挿入されている。
A plurality of bottomed cylindrical solid oxide fuel cells 7 are accommodated in a reaction vessel 1, and these solid oxide fuel cells 7 are formed on a combustion chamber partition plate 3. One end of an oxygen-containing gas introducing pipe 9 fixed to the oxygen-containing gas chamber partition plate 2 is inserted and fixed in the cell insertion hole.

【0004】燃焼室仕切板3には、図示しないが、余剰
の燃料ガスを燃焼室Bに導入するための燃料ガス噴出孔
が形成されており、燃料ガス室仕切板5には、図示しな
いが、燃料ガスを反応室C内に供給するための供給孔が
形成されている。
[0004] Although not shown, the combustion chamber partition plate 3 is provided with a fuel gas ejection hole for introducing surplus fuel gas into the combustion chamber B, and the fuel gas chamber partition plate 5 is provided with a fuel gas ejection hole (not shown). A supply hole for supplying the fuel gas into the reaction chamber C is formed.

【0005】また、反応容器1には、例えば水素からな
る燃料ガスを導入する燃料ガス導入口13、酸素含有ガ
ス、例えば空気を導入する酸素含有ガス導入口17、燃
焼室B内で燃焼したガスを排出するための排気口19が
形成されている。
The reaction vessel 1 has a fuel gas inlet 13 for introducing a fuel gas composed of, for example, hydrogen, an oxygen-containing gas such as an oxygen-containing gas inlet 17 for introducing air, and a gas burned in the combustion chamber B. An exhaust port 19 for discharging air is formed.

【0006】このような固体電解質型燃料電池は、酸素
含有ガス室Aからの酸素含有ガス、例えば空気を、酸素
含有ガス導入管9を介して固体電解質型燃料電池セル7
内にそれぞれ供給し、かつ、燃料ガス室Dからの燃料ガ
スを複数の固体電解質型燃料電池セル7間に供給し、反
応室Cにて反応させ、余剰の空気と燃料ガスを燃焼室B
にて燃焼させ、燃焼したガスが排気口19から外部に排
出される。
In such a solid oxide fuel cell, the oxygen-containing gas, for example, air from the oxygen-containing gas chamber A is supplied to the solid oxide fuel cell 7 through the oxygen-containing gas introducing pipe 9.
And the fuel gas from the fuel gas chamber D is supplied between the plurality of solid oxide fuel cells 7 and reacted in the reaction chamber C, and the excess air and fuel gas are removed from the combustion chamber B.
The burned gas is exhausted from the exhaust port 19 to the outside.

【0007】ところで、固体電解質型燃料電池は、固体
電解質型燃料電池セル7を約1000℃という高温で動
作させるため、装置立ち上げの際は、酸素含有ガス、例
えば空気を外部でプレヒートした後、酸素含有ガス導入
口17より酸素含有ガス室A内に導入し、酸素含有ガス
室Aから酸素含有ガス導入管9を介して固体電解質型燃
料電池セル7内にそれぞれ供給され、このプレヒートさ
れた空気により固体電解質型燃料電池セル7を昇温して
いた。
In the solid oxide fuel cell, since the solid oxide fuel cell 7 is operated at a high temperature of about 1000 ° C., at the time of starting the apparatus, an oxygen-containing gas, for example, air is preheated outside. The preheated air is introduced into the oxygen-containing gas chamber A from the oxygen-containing gas inlet 17 and supplied from the oxygen-containing gas chamber A into the solid oxide fuel cell unit 7 via the oxygen-containing gas introduction pipe 9. As a result, the temperature of the solid oxide fuel cell unit 7 was raised.

【0008】さらに、燃料ガス室Dから複数の固体電解
質型燃料電池セル7間を通過し、燃焼室仕切板3の燃料
ガス噴出孔より噴出した余剰の燃料ガスと、固体電解質
型燃料電池セル7内を通過した空気が、燃焼室B内にて
燃焼し、この熱により酸素含有ガス導入管9を暖め、そ
の内部を通過する空気を暖めることによって固体電解質
型燃料電池セル7を昇温していた。
Further, surplus fuel gas passing from the fuel gas chamber D through the plurality of solid oxide fuel cells 7 and jetting from the fuel gas jet holes of the combustion chamber partition plate 3, and solid fuel cells 7. The air that has passed through the inside is burned in the combustion chamber B, and the heat heats the oxygen-containing gas introduction pipe 9 and the air that passes through the inside of the pipe, thereby raising the temperature of the solid oxide fuel cell 7. Was.

【0009】[0009]

【発明が解決しようとする課題】しかしながら、上記の
ような方法では、反応容器1内に導入する前に酸素含有
ガスを加熱し、この加熱した酸素含有ガスを反応容器1
内に導入することで固体電解質型燃料電池セル7を昇温
したり、余剰の燃料ガスと酸素含有ガスの燃焼により、
酸素含有ガス導入管9内の酸素含有ガスを加熱し、この
加熱した酸素含有ガスの循環により固体電解質型燃料電
池セル7を昇温していたため、加熱した酸素含有ガスと
反応容器1内に導入する経路が長くなり、酸素含有ガス
と固体電解質型燃料電池セル7間の熱交換効率が低く、
固体電解質型燃料電池セル7を加熱するのに時間がかか
り、固体電解質型燃料電池が作動するのに長時間を要す
という問題があった。
However, in the above-described method, the oxygen-containing gas is heated before being introduced into the reaction vessel 1, and the heated oxygen-containing gas is supplied to the reaction vessel 1.
The temperature of the solid oxide fuel cell 7 is increased by introducing it into the fuel cell, or combustion of surplus fuel gas and oxygen-containing gas causes
Since the oxygen-containing gas in the oxygen-containing gas introduction pipe 9 was heated, and the temperature of the solid oxide fuel cell 7 was increased by the circulation of the heated oxygen-containing gas, the heated oxygen-containing gas was introduced into the reaction vessel 1. And the heat exchange efficiency between the oxygen-containing gas and the solid oxide fuel cell 7 is low,
There is a problem that it takes time to heat the solid oxide fuel cell 7, and it takes a long time for the solid oxide fuel cell to operate.

【0010】さらに起動時間が長いため、電力を必要な
時に迅速に取り出せるように、常時固体電解質型燃料電
池セル7を加熱しておく必要があり、無駄なエネルギー
を消費するという問題も生じていた。
Further, since the start-up time is long, it is necessary to constantly heat the solid oxide fuel cell 7 so that electric power can be quickly taken out when needed, thus causing a problem that wasteful energy is consumed. .

【0011】本発明は、固体電解質型燃料電池セルを急
速に昇温でき、これにより動作開始時間を短縮できると
ともに、固体電解質型燃料電池セルの保温のための無駄
なエネルギー消費をなくすことができる固体電解質型燃
料電池を提供することを目的とする。
According to the present invention, the temperature of the solid oxide fuel cell can be rapidly raised, thereby shortening the operation start time and eliminating unnecessary energy consumption for keeping the solid oxide fuel cell warm. It is an object to provide a solid oxide fuel cell.

【0012】[0012]

【課題を解決するための手段】本発明の固体電解質型燃
料電池は、反応容器内に、固体電解質の内面に空気極
を、外面に燃料極を形成してなる円筒状の固体電解質型
燃料電池セルを複数収容するとともに、前記固体電解質
型燃料電池セル内に酸素含有ガス導入管を挿入してなる
固体電解質型燃料電池において、前記酸素含有ガス導入
管および/または前記固体電解質型燃料電池セルに発熱
体を設けたものである。
SUMMARY OF THE INVENTION A solid oxide fuel cell according to the present invention is a cylindrical solid oxide fuel cell comprising an air electrode formed on an inner surface of a solid electrolyte and a fuel electrode formed on an outer surface in a reaction vessel. A solid electrolyte fuel cell comprising a plurality of cells and inserting an oxygen-containing gas inlet tube into the solid oxide fuel cell, wherein the oxygen-containing gas inlet tube and / or the solid oxide fuel cell is A heating element is provided.

【0013】このような構成を採用することにより、固
体電解質型燃料電池セルを急速に昇温でき、迅速に発電
状態に立ち上げることができ、起動性に優れた固体電解
質型燃料電池を得ることができる。
By employing such a configuration, it is possible to rapidly raise the temperature of the solid oxide fuel cell, quickly start up the power generation state, and obtain a solid oxide fuel cell excellent in startability. Can be.

【0014】また、酸素含有ガス導入管の固体電解質型
燃料電池セル内における外側表面に発熱体が形成され、
該発熱体が絶縁層により被覆されていることが望まし
い。このような構成では、酸素含有ガス導入管により、
例えば、空気からなる酸素含有ガスが固体電解質型燃料
電池セル内に導入されるが、酸素含有ガス導入管の外側
表面に形成された発熱体により、酸素含有ガス導入管内
部を流れる空気や、酸素含有ガス導入管と固体電解質型
燃料電池セル間を流れる空気を加熱することができ、加
熱された空気によって固体電解質型燃料電池セルを昇温
できるとともに、固体電解質型燃料電池セルが発熱体の
近傍に配置されているため、輻射熱により固体電解質型
燃料電池セルを急速に昇温できる。
[0014] A heating element is formed on the outer surface of the oxygen-containing gas introduction pipe in the solid oxide fuel cell,
It is desirable that the heating element be covered with an insulating layer. In such a configuration, the oxygen-containing gas introduction pipe
For example, an oxygen-containing gas consisting of air is introduced into the solid oxide fuel cell, and a heating element formed on the outer surface of the oxygen-containing gas introduction tube causes air flowing inside the oxygen-containing gas introduction tube or oxygen. The air flowing between the gas introduction pipe and the solid oxide fuel cell can be heated, the solid electrolyte fuel cell can be heated by the heated air, and the solid oxide fuel cell is located near the heating element. , The temperature of the solid oxide fuel cell unit can be rapidly raised by radiant heat.

【0015】また、このような構成では、固体電解質型
燃料電池セル内面の空気極と、酸素含有ガス導入管の外
側表面との間隔が狭いため、酸素含有ガス導入管の外側
表面に形成された発熱体が空気極と接触する虞がある
が、絶縁層が発熱体を被覆しているため、固体電解質型
燃料電池セルの内面に酸素含有ガス導入管が接触して
も、発熱体を流れる電流が固体電解質型燃料電池セルに
流れることがなく、このため、確実に発熱体を加熱で
き、損失なく燃料電池セルを昇温できる。
Further, in such a configuration, since the distance between the air electrode on the inner surface of the solid oxide fuel cell and the outer surface of the oxygen-containing gas inlet tube is narrow, the air electrode is formed on the outer surface of the oxygen-containing gas inlet tube. Although the heating element may come into contact with the air electrode, since the insulating layer covers the heating element, even if the oxygen-containing gas introduction pipe contacts the inner surface of the solid oxide fuel cell, the current flowing through the heating element Does not flow to the solid oxide fuel cell, and therefore the heating element can be reliably heated, and the temperature of the fuel cell can be increased without loss.

【0016】さらに、発熱体を被覆する絶縁層は、Al
2 3 、MgOおよびZrO2 のうち少なくとも1種を
主成分とすることが望ましい。Al2 3 、MgO、Z
rO2 は耐熱性を有するため、1000℃での連続運転
に使用できる。中でもAl23 は熱伝導性が良好なた
め、固体電解質型燃料電池セルを急速に昇温させること
ができる。
Further, the insulating layer covering the heating element is made of Al
It is desirable that at least one of 2 O 3 , MgO and ZrO 2 be the main component. Al 2 O 3 , MgO, Z
Since rO 2 has heat resistance, it can be used for continuous operation at 1000 ° C. Above all, Al 2 O 3 has good thermal conductivity, so that the temperature of the solid oxide fuel cell can be rapidly raised.

【0017】また、固体電解質型燃料電池セルの空気極
に発熱体が内蔵されていることが望ましい。このような
構成を採用することにより、固体電解質型燃料電池セル
を直接加熱できるため、急速に加熱することができる。
It is desirable that a heating element is built in the air electrode of the solid oxide fuel cell. By employing such a configuration, the solid oxide fuel cell unit can be directly heated, and thus can be rapidly heated.

【0018】[0018]

【発明の実施の形態】本発明の固体電解質型燃料電池
は、固体電解質型燃料電池セルの空気極に発熱体を内蔵
した点、酸素含有ガス導入管に発熱体を形成した点を除
いて実質的に従来と同様の構造を有しているため、本発
明の固体電解質型燃料電池を、図1で説明する。
BEST MODE FOR CARRYING OUT THE INVENTION A solid oxide fuel cell according to the present invention is substantially the same as the solid oxide fuel cell except that a heating element is incorporated in an air electrode and a heating element is formed in an oxygen-containing gas introducing pipe. Since it has the same structure as the conventional one, the solid oxide fuel cell of the present invention will be described with reference to FIG.

【0019】即ち、固体電解質型燃料電池は、図1に示
すように、反応容器1内に、酸素含有ガス室仕切板2、
燃焼室仕切板3、燃料ガス室仕切板5を用いて酸素含有
ガス室A、燃焼室B、反応室C、燃料ガス室Dが形成さ
れている。
That is, as shown in FIG. 1, a solid oxide fuel cell comprises an oxygen-containing gas chamber partition plate 2,
An oxygen-containing gas chamber A, a combustion chamber B, a reaction chamber C, and a fuel gas chamber D are formed using the combustion chamber partition plate 3 and the fuel gas chamber partition plate 5.

【0020】反応容器1内には、複数の有底筒状の固体
電解質型燃料電池セル7が収容されており、これらの固
体電解質型燃料電池セル7は、燃焼室仕切板3に形成さ
れたセル挿入孔に挿入固定されており、また、その内部
には酸素含有ガス室仕切板2に固定された酸素含有ガス
導入管9の一端が挿入されている。
A plurality of bottomed cylindrical solid oxide fuel cells 7 are accommodated in the reaction vessel 1, and these solid oxide fuel cells 7 are formed on the combustion chamber partition plate 3. One end of an oxygen-containing gas introducing pipe 9 fixed to the oxygen-containing gas chamber partition plate 2 is inserted and fixed in the cell insertion hole.

【0021】燃焼室仕切板3には、図示しないが、余剰
の燃料ガスを燃焼室Bに導入するための燃料ガス噴出孔
が形成されており、燃料ガス室仕切板5には、図示しな
いが、燃料ガスを反応室C内に供給するための供給孔が
形成されている。
Although not shown, the combustion chamber partition plate 3 is provided with a fuel gas ejection hole for introducing excess fuel gas into the combustion chamber B, and the fuel gas chamber partition plate 5 is provided with a fuel gas discharge hole (not shown). A supply hole for supplying the fuel gas into the reaction chamber C is formed.

【0022】また、反応容器1には、例えば水素からな
る燃料ガスを導入する燃料ガス導入口13、酸素含有ガ
ス、例えば空気を導入する酸素含有ガス導入口17、燃
焼室B内で燃焼したガスを排出するための排気口19が
形成されている。
The reaction vessel 1 has a fuel gas inlet 13 for introducing a fuel gas composed of, for example, hydrogen, an oxygen-containing gas such as an oxygen-containing gas inlet 17 for introducing air, and a gas burned in the combustion chamber B. An exhaust port 19 for discharging air is formed.

【0023】固体電解質型燃料電池セル7は、図2に示
すように、例えば、支持管としてのLaMnO3 系空気
極21と、この空気極21の表面に形成されたY2 3
安定化ZrO2 からなる固体電解質22と、固体電解質
22の表面に形成されたNi一ジルコニア系の燃料極2
3と、空気極21と電気的に接続されるLaCrO3
よりなるインターコネクタ24とから構成されている。
As shown in FIG. 2, the solid oxide fuel cell 7 includes, for example, a LaMnO 3 -based air electrode 21 as a support tube, and Y 2 O 3 formed on the surface of the air electrode 21.
A solid electrolyte 22 made of stabilized ZrO 2, and a Ni-zirconia-based fuel electrode 2 formed on the surface of the solid electrolyte 22
3 and an interconnector 24 made of LaCrO 3 and electrically connected to the air electrode 21.

【0024】そして、図3に示すように、一方のセル7
のインターコネクタ24を、Ni金属繊維等の接続部材
25を介して他方のセル7の燃料極23に接続して、複
数のセル7が電気的に接続され、スタック27が構成さ
れており、このようなスタック27が、図1に示したよ
うに、反応容器1内に複数収容されて固体電解質型燃料
電池が構成されている。
Then, as shown in FIG.
Is connected to the fuel electrode 23 of the other cell 7 via a connecting member 25 such as Ni metal fiber, so that a plurality of cells 7 are electrically connected to form a stack 27. As shown in FIG. 1, a plurality of such stacks 27 are accommodated in the reaction vessel 1 to constitute a solid oxide fuel cell.

【0025】そして、本発明の固体電解質型燃料電池で
は、図4に示すように、セル7内部における酸素含有ガ
ス導入管9の外面に発熱体31が形成されており、この
発熱体31が、図4(b)に示すように、絶縁層33に
より被覆されている。この絶縁層33は、1000℃で
の高温でも耐久性を有するという点から、ZrO2 、M
gOおよびAl2 3 のうち少なくとも一種を主成分と
するものが望ましい。
Further, in the solid oxide fuel cell of the present invention, as shown in FIG. 4, a heating element 31 is formed on the outer surface of the oxygen-containing gas introducing pipe 9 inside the cell 7, and this heating element 31 As shown in FIG. 4B, it is covered with an insulating layer 33. This insulating layer 33 is made of ZrO 2 , M
It is desirable that at least one of gO and Al 2 O 3 be the main component.

【0026】特に、熱伝導が良好という観点からAl2
3 が望ましい。尚、図4(a)では絶縁層33は省略
した。
In particular, from the viewpoint of good heat conduction, Al 2
O 3 is preferred. In FIG. 4A, the insulating layer 33 is omitted.

【0027】発熱体31は、図4(a)の上方に向けて
引き出され、空気室Aで、直並列に接続され、燃料電池
の外部に取り出され、外部電源に接続されている。
The heating element 31 is drawn upward in FIG. 4A, connected in series and parallel in the air chamber A, taken out of the fuel cell, and connected to an external power supply.

【0028】以上のように構成された固体電解質型燃料
電池では、酸素含有ガス室Aからの酸素含有ガス、例え
ば空気を、酸素含有ガス導入管9を介して固体電解質型
燃料電池セル7内にそれぞれ供給し、かつ、燃料ガス室
Dからの燃料ガスを複数の固体電解質型燃料電池セル7
間に供給し、反応室Cにて反応させ、余剰の空気と燃料
ガスを燃焼室Bにて燃焼させ、燃焼したガスが排気口1
9から外部に排出される。
In the solid oxide fuel cell configured as described above, the oxygen-containing gas, for example, air from the oxygen-containing gas chamber A is introduced into the solid oxide fuel cell 7 through the oxygen-containing gas introducing pipe 9. Each of the plurality of solid oxide fuel cells 7 supplies fuel gas from the fuel gas chamber D and
And reacts in the reaction chamber C, and burns excess air and fuel gas in the combustion chamber B.
9 to the outside.

【0029】そして、本発明の固体電解質型燃料電池で
は、酸素含有ガス導入管9の外側表面に発熱体31が形
成されているので、酸素含有ガス導入管9内を流通する
空気や、酸素含有ガス導入管9の外面とセル7の内面と
の間を流通する空気が、酸素含有ガス導入管9の外側表
面の発熱体31により加熱され、この加熱された空気に
よりセル7を急速に昇温できる。また、同時に、セル7
が発熱体31の近傍に配置されているため、輻射熱によ
りセル7を動作温度である1000℃まで急速に昇温で
き、このため、固体電解質型燃料電池を迅速に発電状態
に立ち上げることができ、起動性に優れた固体電解質型
燃料電池を得ることができる。
In the solid oxide fuel cell according to the present invention, since the heating element 31 is formed on the outer surface of the oxygen-containing gas introduction pipe 9, air flowing through the oxygen-containing gas introduction pipe 9 and oxygen-containing gas The air flowing between the outer surface of the gas inlet tube 9 and the inner surface of the cell 7 is heated by the heating element 31 on the outer surface of the oxygen-containing gas inlet tube 9, and the heated air rapidly raises the temperature of the cell 7. it can. At the same time, cell 7
Is disposed near the heating element 31, the temperature of the cell 7 can be rapidly raised to the operating temperature of 1000 ° C. by radiant heat, and therefore, the solid oxide fuel cell can be quickly brought into the power generation state. Thus, a solid oxide fuel cell having excellent start-up properties can be obtained.

【0030】また、酸素含有ガス導入管9の外側表面に
形成された発熱体31が絶縁層33により被覆されてい
るため、セル7内面の空気極21に、酸素含有ガス導入
管9の外側表面が接触したとしても、空気極21と発熱
体31とが導通することがなく、発熱体31を流れる電
流がセル7に流れることがなく、このため損失なく昇温
できる。
Further, since the heating element 31 formed on the outer surface of the oxygen-containing gas introducing pipe 9 is covered with the insulating layer 33, the air electrode 21 on the inner surface of the cell 7 is attached to the outer surface of the oxygen-containing gas introducing pipe 9. Even if the contact occurs, the air electrode 21 and the heating element 31 do not conduct, and the current flowing through the heating element 31 does not flow through the cell 7, so that the temperature can be increased without loss.

【0031】さらに、発熱体31を被覆する絶縁層33
が、耐熱性を有するAl2 3 、MgOおよびZrO2
のうち少なくとも1種を主成分とするため、1000℃
での連続運転に使用できる。
Further, an insulating layer 33 covering the heating element 31
Are heat-resistant Al 2 O 3 , MgO and ZrO 2
1000 ° C. because at least one of them is a main component
Can be used for continuous operation at

【0032】図5は、本発明の他の固体電解質型燃料電
池のセルを示すもので、この固体電解質型燃料電池のセ
ル7の空気極21内には、Pt系材料からなる発熱体4
1が内蔵さられている。尚、発熱体41は、図示しない
が、電極がセル7の開放端に引き出され、燃焼室仕切板
3上に形成された電極を介して外部に引き出され、外部
電源に接続されている。
FIG. 5 shows a cell of another solid oxide fuel cell according to the present invention. A heating element 4 made of a Pt-based material is provided in an air electrode 21 of a cell 7 of the solid oxide fuel cell.
1 is built-in. Although not shown, the heating element 41 has an electrode drawn out to the open end of the cell 7, drawn out through an electrode formed on the combustion chamber partition plate 3, and connected to an external power supply.

【0033】このような固体電解質型燃料電池では、セ
ル7の空気極21に内蔵された発熱体41により、セル
7を直接加熱することができ、起動性に優れた固体電解
質型燃料電池を得ることができる。
In such a solid oxide fuel cell, the cell 7 can be directly heated by the heating element 41 incorporated in the air electrode 21 of the cell 7, and a solid oxide fuel cell excellent in start-up performance can be obtained. be able to.

【0034】[0034]

【発明の効果】本発明の固体電解質型燃料電池では、酸
素含有ガス導入管および/または固体電解質型燃料電池
セルに発熱体を設けたので、固体電解質型燃料電池セル
を効率良く急速に昇温できる。これにより動作開始時間
を短縮でき、保温のための無駄なエネルギー消費をなく
すことができる。
According to the solid oxide fuel cell of the present invention, since the heating element is provided in the oxygen-containing gas introducing pipe and / or the solid oxide fuel cell, the temperature of the solid oxide fuel cell can be raised quickly and efficiently. it can. As a result, the operation start time can be shortened, and unnecessary energy consumption for heat retention can be eliminated.

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

【図1】固体電解質型燃料電池の模式図である。FIG. 1 is a schematic view of a solid oxide fuel cell.

【図2】固体電解質型燃料電池セルの断面図である。FIG. 2 is a sectional view of a solid oxide fuel cell.

【図3】スタックを示す平面図である。FIG. 3 is a plan view showing a stack.

【図4】酸素含有ガス導入管の表面に発熱体を形成した
例を示すもので、(a)は側面図、(b)は断面図であ
る。
FIGS. 4A and 4B show an example in which a heating element is formed on the surface of an oxygen-containing gas introduction pipe, wherein FIG. 4A is a side view and FIG.

【図5】空気極に発熱体を内蔵したセルを示す断面図で
ある。
FIG. 5 is a cross-sectional view showing a cell having a heating element built in an air electrode.

【符号の説明】[Explanation of symbols]

1・・・反応容器 7・・・固体電解質型燃料電池セル 9・・・酸素含有ガス導入管 21・・・空気極 22・・・固体電解質 23・・・燃料極 31,41・・・発熱体 33・・・絶縁層 DESCRIPTION OF SYMBOLS 1 ... Reaction container 7 ... Solid oxide fuel cell 9 ... Oxygen-containing gas introduction pipe 21 ... Air electrode 22 ... Solid electrolyte 23 ... Fuel electrode 31, 41 ... Heat generation Body 33 ... insulating layer

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】反応容器内に、固体電解質の内面に空気極
を、外面に燃料極を形成してなる円筒状の固体電解質型
燃料電池セルを複数収容するとともに、前記固体電解質
型燃料電池セル内に酸素含有ガス導入管を挿入してなる
固体電解質型燃料電池において、前記酸素含有ガス導入
管および/または前記固体電解質型燃料電池セルに発熱
体を設けたことを特徴とする固体電解質型燃料電池。
A plurality of cylindrical solid electrolyte fuel cells each having an air electrode formed on an inner surface of a solid electrolyte and a fuel electrode formed on an outer surface thereof are accommodated in a reaction vessel. A solid oxide fuel cell comprising an oxygen-containing gas introduction tube inserted therein, wherein a heating element is provided in the oxygen-containing gas introduction tube and / or the solid oxide fuel cell. battery.
【請求項2】酸素含有ガス導入管の固体電解質型燃料電
池セル内における外側表面に発熱体が形成され、該発熱
体が絶縁層により被覆されていることを特徴とする請求
項1記載の固体電解質型燃料電池。
2. The solid according to claim 1, wherein a heating element is formed on an outer surface of the oxygen-containing gas introduction pipe in the solid oxide fuel cell, and the heating element is covered with an insulating layer. Electrolyte fuel cell.
【請求項3】発熱体を被覆する絶縁層が、Al2 3
MgOおよびZrO2のうち少なくとも1種を主成分と
することを特徴とする請求項2記載の固体電解質型燃料
電池。
3. The insulating layer covering the heating element is made of Al 2 O 3 ,
3. The solid oxide fuel cell according to claim 2 , wherein at least one of MgO and ZrO2 is a main component.
【請求項4】固体電解質型燃料電池セルの空気極に発熱
体が内蔵されていることを特徴とする請求項1乃至3の
いずれかに記載の固体電解質型燃料電池。
4. The solid oxide fuel cell according to claim 1, wherein a heating element is built in the air electrode of the solid oxide fuel cell.
JP27686799A 1999-09-29 1999-09-29 Solid oxide fuel cell Expired - Fee Related JP4817476B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27686799A JP4817476B2 (en) 1999-09-29 1999-09-29 Solid oxide fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27686799A JP4817476B2 (en) 1999-09-29 1999-09-29 Solid oxide fuel cell

Publications (2)

Publication Number Publication Date
JP2001102075A true JP2001102075A (en) 2001-04-13
JP4817476B2 JP4817476B2 (en) 2011-11-16

Family

ID=17575529

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27686799A Expired - Fee Related JP4817476B2 (en) 1999-09-29 1999-09-29 Solid oxide fuel cell

Country Status (1)

Country Link
JP (1) JP4817476B2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002319415A (en) * 2001-04-20 2002-10-31 Kyocera Corp Solid electrolyte fuel cell and fuel cell
JP2003045464A (en) * 2001-07-26 2003-02-14 Kyocera Corp Fuel cell and its power generation method
JP2004207007A (en) * 2002-12-25 2004-07-22 Kyocera Corp Cell for fuel cell, and fuel cell
JP2005353487A (en) * 2004-06-11 2005-12-22 Toyota Motor Corp Membrane electrode composite for tube type fuel cell
JP2008047546A (en) * 2007-10-25 2008-02-28 Kyocera Corp Fuel battery

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61183878A (en) * 1985-02-07 1986-08-16 ウエスチングハウス エレクトリック コ−ポレ−ション Electrochemical dynamotor
JPH07183043A (en) * 1993-12-22 1995-07-21 Toshiba Corp Fuel-cell power generating facility
JPH10284108A (en) * 1997-03-31 1998-10-23 Toyota Motor Corp Solid electrolyte, and fuel cell, hydrogen pump, oxygen concentration sensor, and steam concentration sensor using the electrolyte
JPH11224683A (en) * 1997-11-25 1999-08-17 Sulzer Hexis Ag Fuel battery module with built-in auxiliary heater unit and plant provided with the module

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61183878A (en) * 1985-02-07 1986-08-16 ウエスチングハウス エレクトリック コ−ポレ−ション Electrochemical dynamotor
JPH07183043A (en) * 1993-12-22 1995-07-21 Toshiba Corp Fuel-cell power generating facility
JPH10284108A (en) * 1997-03-31 1998-10-23 Toyota Motor Corp Solid electrolyte, and fuel cell, hydrogen pump, oxygen concentration sensor, and steam concentration sensor using the electrolyte
JPH11224683A (en) * 1997-11-25 1999-08-17 Sulzer Hexis Ag Fuel battery module with built-in auxiliary heater unit and plant provided with the module

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002319415A (en) * 2001-04-20 2002-10-31 Kyocera Corp Solid electrolyte fuel cell and fuel cell
JP2003045464A (en) * 2001-07-26 2003-02-14 Kyocera Corp Fuel cell and its power generation method
JP2004207007A (en) * 2002-12-25 2004-07-22 Kyocera Corp Cell for fuel cell, and fuel cell
JP2005353487A (en) * 2004-06-11 2005-12-22 Toyota Motor Corp Membrane electrode composite for tube type fuel cell
JP2008047546A (en) * 2007-10-25 2008-02-28 Kyocera Corp Fuel battery

Also Published As

Publication number Publication date
JP4817476B2 (en) 2011-11-16

Similar Documents

Publication Publication Date Title
JP3731650B2 (en) Fuel cell
JP4707023B2 (en) Solid oxide fuel cell
KR20150128716A (en) Soec stack with integrated heater
KR101009453B1 (en) A thermally self-controllable solid oxide fuel cell system
JP4325924B2 (en) Fuel cell
JP2003282132A (en) Fuel cell
JP3796182B2 (en) Fuel cell
KR100599735B1 (en) Fuel cell system and reformer
JP2004335163A (en) Solid oxide type fuel cell and its operation method
JP4991059B2 (en) Fuel cell and power generation method thereof
JP4513281B2 (en) Fuel cell
JP2001102075A (en) Solid electrolyte fuel cell
JP3706959B2 (en) Structure of a cylindrical solid oxide fuel cell having a conductive tube inserted therein, a structure of a bundle in which a plurality of such cells are bundled, and a structure of a power generation module using the bundle
JP2007018966A (en) Fuel cell
JP2005100818A (en) Fuel cell
JP3580704B2 (en) Fuel cell
JP3686773B2 (en) Solid oxide fuel cell
JP3585381B2 (en) Solid oxide fuel cell
JP3686781B2 (en) Fuel cell
CN109962261A (en) A kind of solid oxide fuel cell power generating system
JP3610223B2 (en) Solid oxide fuel cell
JP4461705B2 (en) Operation method of solid oxide fuel cell
JP2003234122A (en) Fuel cell
JP2005285340A (en) Fuel battery and operation method of the same
JP3854170B2 (en) Fuel cell

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20060912

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20100303

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20100601

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20100802

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20110802

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20110830

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140909

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

LAPS Cancellation because of no payment of annual fees