JP2936331B2 - Support tube for solid electrolyte fuel cell - Google Patents
Support tube for solid electrolyte fuel cellInfo
- Publication number
- JP2936331B2 JP2936331B2 JP1167425A JP16742589A JP2936331B2 JP 2936331 B2 JP2936331 B2 JP 2936331B2 JP 1167425 A JP1167425 A JP 1167425A JP 16742589 A JP16742589 A JP 16742589A JP 2936331 B2 JP2936331 B2 JP 2936331B2
- Authority
- JP
- Japan
- Prior art keywords
- support tube
- fuel cell
- solid electrolyte
- calcia
- sintered body
- 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
Links
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
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
- H01M8/1231—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte with both reactants being gaseous or vaporised
-
- 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
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
- H01M8/1213—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte characterised by the electrode/electrolyte combination or the supporting material
- H01M8/1226—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte characterised by the electrode/electrolyte combination or the supporting material characterised by the supporting layer
-
- 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)
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燃料電池用支持管として用いられ
るカルシア安定化ジルコニア質焼結体に関するものであ
る。Description: TECHNICAL FIELD The present invention relates to a calcia-stabilized zirconia sintered body used as a support tube for a solid oxide fuel cell.
〔従来の技術〕 従来より電力供給源として石炭、石油、天然ガス等を
用いる火力発電とともに該燃料を用いる原子力発電等が
あるが、いずれも前記石炭、石油、天然ガス等の燃料を
燃焼させるか、該燃料を核分裂させて熱エネルギーに変
え、機械エネルギーを経由して電気エネルギーに変換し
ており、前記熱エネルギーから電気エネルギーに変換す
る際の熱効率は40%程度がほぼ限界とされている。ま
た、前記電力供給源は大気汚染物質の排出、騒音の発
生、大量の冷却水が必要であること等の環境上の問題が
あり、立地に対する制約も極めて多いという課題を有し
ている。[Prior art] Conventionally, there is a nuclear power generation using the fuel together with a thermal power generation using coal, oil, natural gas or the like as an electric power supply source. The fuel is fissioned and converted into thermal energy, which is converted into electrical energy via mechanical energy. The thermal efficiency of converting the thermal energy into electrical energy is almost limited to about 40%. In addition, the power supply source has environmental problems such as emission of air pollutants, generation of noise, and necessity of a large amount of cooling water, and has a problem that the location is extremely restricted.
そこで、前記従来の電気供給源としての火力発電や原
子力発電等の課題を解決せんとして機械エネルギーを経
由することなく熱エネルギーを直接電気エネルギーに変
換する、所謂直接発電方式、例えばMHD発電(Magneto−
Hydro−Dynamic Generation),EFD発電(Electro−Flui
d−Dynamic Generation),熱電発電あるいは熱電子発
電等が提案されているが、現在のところ、その熱効率は
10〜205程度と低く、実用性に乏しい。Therefore, a so-called direct power generation method, in which thermal energy is directly converted into electric energy without passing through mechanical energy in order to solve the problems of the thermal power generation and nuclear power generation as the conventional power supply sources, for example, MHD power generation (Magneto-
Hydro-Dynamic Generation), EFD power generation (Electro-Flui)
d-Dynamic Generation), thermoelectric power generation or thermionic power generation have been proposed.
It is low, about 10-205, and is not practical.
更に、前記熱エネルギーをも経由せず、燃料の化学エ
ネルギーを直接電気エネルギーに変換する高効率の発電
方式として、例えば起電反応の源となる物質、つまり還
元剤と酸化剤とを連続的に供給し、これらが反応すると
き放出するエネルギーを直接電力の形式で取り出す燃料
電池による発電が提案されている。Furthermore, as a high-efficiency power generation system that directly converts chemical energy of fuel into electric energy without passing through the heat energy, for example, a substance serving as a source of an electromotive reaction, that is, a reducing agent and an oxidizing agent are continuously used. It has been proposed to generate electricity by means of fuel cells, which supply and extract in the form of direct power the energy released when they react.
前記燃料電池としては、低温型燃料電池と高温型燃料
電池がある。The fuel cell includes a low-temperature fuel cell and a high-temperature fuel cell.
低温型燃料電池としては、例えばリン酸溶液からなる
酸性電解液を電解質とし、酸化剤として空気を使用する
ことができ、石炭、石油、天然ガス等の化石燃料からの
改質水素を燃料とする酸性電解液燃料電池がある。しか
しながら、300℃程度以下で作動する前記低温型燃料電
池では高価な白金触媒を使用して電池反応を促進しなけ
れば高い電圧下では高い電流密度が得られず、また燃料
として最終的に水素に変成したものでなければならない
という制約があった。As a low-temperature fuel cell, for example, an acidic electrolytic solution composed of a phosphoric acid solution is used as an electrolyte, air can be used as an oxidizing agent, and reformed hydrogen from fossil fuels such as coal, oil, and natural gas is used as a fuel. There is an acidic electrolyte fuel cell. However, in the low-temperature fuel cell that operates at about 300 ° C. or lower, a high current density cannot be obtained at a high voltage unless an expensive platinum catalyst is used to promote the cell reaction, and finally hydrogen is used as a fuel. There was a restriction that it must be a metamorphic one.
また、高温型燃料電池としてはアルカリ炭素塩の溶融
液を電解質とし、酸化剤として空気を使用し、改質水素
の他に石油ガス、天然ガス、メタノール等を燃料とし、
約600℃程度の温度で作動する溶融塩電解質燃料電気等
がある。しかし乍ら、前記溶融塩電解質燃料電池は高温
により前記電解質の経時的変化から該電解質の劣化が起
こり、該電池の反応速度が低下したり、更には腐蝕が発
生するという課題を有していた。In addition, as a high-temperature fuel cell, a molten solution of an alkali carbon salt is used as an electrolyte, air is used as an oxidizing agent, and petroleum gas, natural gas, methanol, etc. are used as fuel in addition to reformed hydrogen,
There is a molten salt electrolyte fuel operated at a temperature of about 600 ° C. However, the molten salt electrolyte fuel cell has a problem in that the electrolyte deteriorates due to a temporal change of the electrolyte due to a high temperature, so that the reaction speed of the battery is reduced and furthermore, corrosion is generated. .
このような課題を解決するために、酸化物固溶体から
成る固体電解質を介し、空気を酸化剤として300℃程度
の低温では作動し難い石炭の他に、改質水素、一酸化水
素、炭化水素等も燃料として使用可能であり、約1000℃
の高温で作動させることにより良好な電池の効率と電極
面での高い電流密度が得られる高温型固体電解質燃料電
池が提案されている。In order to solve such problems, in addition to coal, which is hard to operate at low temperatures of about 300 ° C using air as an oxidant, reformed hydrogen, hydrogen monoxide, hydrocarbons, etc., through a solid electrolyte composed of an oxide solid solution Can also be used as fuel, about 1000 ℃
There has been proposed a high-temperature type solid electrolyte fuel cell which can obtain good cell efficiency and a high current density on the electrode surface by operating at a high temperature.
そこで、高温型固体電解質燃料電池についてその一例
を示す第1図を参照して説明する。Therefore, a high-temperature solid electrolyte fuel cell will be described with reference to FIG.
支持管1はカルシアで安定化した安定化ジルコニアか
ら成り、耐熱性とともに適度の気体を通し、隔壁機能が
最大限に生かされる開気孔率40%程度の多孔質から成
る。支持管1の外表面は、電極及び固体電解質が形成さ
れている。すなわち前記支持管1の外表面上に例えばカ
ルシウムをドープしたランタンとマンガンの複合酸化物
(LaMnO3)から成る陽極2と、多孔性のカルシア安定化
ジルコニアから成る固体電解質3及び酸化ニッケルと安
定化ジルコニアの混合物から成る陰極4が順次積層され
た構造をなしており、更に該陰極4の切り欠き部4aには
単位電池を直列に接続するためのインタコネクタ5が形
成されている。前記支持管1の内側には空気6を、電池
の外側には燃料7をそれぞれ供給し、これらが支持管
1、陽極2及び陰極4、固体電解質3を介して反応する
時のエネルギーを直接電力の形式で取り出すものであ
る。The support tube 1 is made of stabilized zirconia stabilized by calcia, and is made of a porous material having an open porosity of about 40%, which allows the passage of an appropriate gas with heat resistance and maximizes the partition wall function. An electrode and a solid electrolyte are formed on the outer surface of the support tube 1. That is, an anode 2 made of, for example, a complex oxide of lanthanum and manganese (LaMnO 3 ) doped with calcium, a solid electrolyte 3 made of porous calcia-stabilized zirconia, and a nickel oxide are formed on the outer surface of the support tube 1. The cathode 4 made of a mixture of zirconia has a structure in which the cathodes 4 are sequentially laminated, and a cutout 4a of the cathode 4 is formed with an interconnector 5 for connecting unit batteries in series. Air 6 is supplied to the inside of the support tube 1 and fuel 7 is supplied to the outside of the battery, and the energy when these react via the support tube 1, the anode 2 and the cathode 4, and the solid electrolyte 3 is directly supplied to the electric power. In the form of
前記燃料電池は基本単位の電池の出力が10W前後と低
いため、商用発電を実現するためには前記基本単位の電
池を大量に直列に連結することによって高出力化をはか
る必要がある。ところが、前記カルシア安定化ジルコニ
ア質焼結体よりなる支持管1は、該支持管1の外表面に
電極2,4及び固体電解質3を形成する際の高温加熱によ
るわずかな変形によって、前記電池を大量に連結するこ
とが困難となったり、また、常時1000〜1200℃の高温状
態での作動中に前記支持管1が変形を起こし、該支持管
1より電極2,4及び固体電解質3が剥離または脱落した
り、ひいては支持管1自体の破損を招き、燃料電池の破
壊に至るという問題点があった。Since the output of the fuel cell in the basic unit is as low as about 10 W, it is necessary to increase the output by connecting a large number of the cells in the basic unit in series in order to realize commercial power generation. However, the support tube 1 made of the calcia-stabilized zirconia-based sintered body has a problem in that the battery is slightly deformed by high-temperature heating when the electrodes 2, 4 and the solid electrolyte 3 are formed on the outer surface of the support tube 1. It becomes difficult to connect a large amount, and the support tube 1 is deformed during the operation at a high temperature of 1000 to 1200 ° C., and the electrodes 2, 4 and the solid electrolyte 3 are separated from the support tube 1. Alternatively, there has been a problem that the fuel cell may fall off, and eventually, the support tube 1 itself may be damaged, leading to the destruction of the fuel cell.
そこで、従来から、カルシア安定化ジルコニア質焼結
体におけるジルコニア粉末から混入されるSiO2,Al2O3,F
e2O3等の不可避不純物か焼結体中の粒界に於いて低融点
のガラス質相を形成することから、この不純物を低減さ
せることによって焼結体の化学的、機械的安定性を保つ
ことが行われていた。Therefore, conventionally, SiO 2 , Al 2 O 3 , F mixed from zirconia powder in a calcia-stabilized zirconia sintered body
Since unavoidable impurities such as e 2 O 3 form a low-melting glassy phase at the grain boundaries in the sintered body, reducing these impurities will improve the chemical and mechanical stability of the sintered body. Keeping was done.
しかしながら、これらの不純物の低減はそれ自体限界
があるとともに効果としても不十分であり実用的ではな
かった。However, the reduction of these impurities has limitations in themselves and is insufficient in effect, and is not practical.
また、本出願人はカルシア安定化ジルコニア質焼結体
における不純物中のマグネシア量を低減させることによ
って、焼結体の熱変形量を低減させられることをすでに
提案した(特開昭64−33853号公報参照)。しかし、こ
れでも1400℃で熱処理した後の単位長さあたりの変形率
は1.25%程度であり、固体電解質燃料電池用支持管に要
求される、変形率0.25%以下のレベルに達していなかっ
た。The present applicant has already proposed that the amount of thermal deformation of a sintered body can be reduced by reducing the amount of magnesia in impurities in a calcia-stabilized zirconia sintered body (Japanese Patent Application Laid-Open No. 64-33853). Gazette). However, even in this case, the deformation rate per unit length after heat treatment at 1400 ° C. was about 1.25%, and did not reach the level of the deformation rate of 0.25% or less required for the solid oxide fuel cell support tube.
本発明は上記課題を解決することを主たる目的とする
もので、具体的には多孔性の支持管の熱変形を軽減し、
該支持管の外表面に形成された電極や固体電解質の剥離
や脱落が皆無で、燃料電池としての機能に支障を来すこ
とのない、耐熱性に優れた固体電解質燃料電池用支持管
を提供することを目的とするものである。The present invention has a main object to solve the above problems, specifically, to reduce thermal deformation of a porous support tube,
Provided is a support tube for a solid electrolyte fuel cell which is excellent in heat resistance without any peeling or falling off of electrodes and solid electrolyte formed on the outer surface of the support tube and which does not hinder the function as a fuel cell. It is intended to do so.
本発明は、多孔質カルシア安定化ジルコニア質焼結体
よりなる固定電解質燃料電池用支持管において、前記カ
ルシア安定化ジルコニア質焼結体中のマグネシア及びア
ルミナの量を全添加物量に対しそれぞれ2.5重量%以
下、5.0重量%以下としたものである。The present invention provides a support tube for a fixed electrolyte fuel cell made of a porous calcia-stabilized zirconia sintered body, wherein the amounts of magnesia and alumina in the calcia-stabilized zirconia sintered body are each 2.5 wt. % Or less and 5.0% by weight or less.
本発明においてカルシア安定化ジルコニア質焼結体中
のマグネシアおよびアルミナの量はICP発光分光分析法
により求めた。また、X線マイクロアナライザーによる
分析の結果から、これらマグネシア、アルミナは通常結
晶粒界に編析して低融点のガラス質相の主成分をなして
おり、該ガラス質相が粒界のすべりを起こして変形に至
ると考えられる。よって、本発明はマグネシア、アルミ
ナを優先的に低減することにより、ガラス質相粒界すべ
りを起こすことによる支持管の変形を防止しようとする
ものである。In the present invention, the amounts of magnesia and alumina in the calcia-stabilized zirconia sintered body were determined by ICP emission spectroscopy. Also, from the results of analysis by an X-ray microanalyzer, these magnesia and alumina usually form a main component of a low melting point glassy phase by crystallizing at crystal grain boundaries, and the glassy phase causes slip of the grain boundaries. It is thought that it wakes up and leads to deformation. Therefore, the present invention aims to prevent the deformation of the support tube due to the vitreous phase grain boundary sliding by preferentially reducing magnesia and alumina.
また、本発明において、マグネシア及びアルミナの全
添加物に対する割合をそれどれ2.5重量%以下、5.0重量
%以下としたのは、前記支持管の外表面に電極および固
体電解質を密着形成したり、直列に連結して大出力の燃
料電池を構成する上で要求される単位長さ当たりの変形
率が0.25%以下の範囲内とするためである。In the present invention, the ratio of magnesia and alumina to the total additive is set to 2.5% by weight or less and 5.0% by weight or less, respectively, because an electrode and a solid electrolyte are closely formed on the outer surface of the support tube, This is because the deformation rate per unit length required for forming a high-power fuel cell by connecting to the above is within the range of 0.25% or less.
なお、ここでの全添加物とは、焼結助剤などの添加剤
の他に原料粉末としてのカルシア粉末、ジルコニア粉末
中の不純物、及び製造工程中に混入する不純物も含むも
のであり、焼結体の主成分であるカルシアおよびジルコ
ニアを除く他の成分の全量を意味する。また、焼結体中
の全添加物量は10重量%以下であることが望ましいが、
少なすぎると焼結性が悪くなることから、全添加物量は
8重量%程度のものが最も優れていた。The term “all additives” used herein includes not only additives such as sintering aids but also impurities in calcia powder and zirconia powder as raw material powders, and impurities mixed in the manufacturing process. It means the total amount of other components except calcia and zirconia which are the main components of the consolidation. In addition, the total amount of additives in the sintered body is desirably 10% by weight or less,
If the amount is too small, the sinterability deteriorates, so that the total amount of additives is about 8% by weight.
以下、本発明を実施例に基づき説明する。 Hereinafter, the present invention will be described based on examples.
カルシアを15モル%含有し、全添加物量がほぼ8重量
%に設定され、この全添加物中のマグネシアおよびアル
ミナ量を第1表のように種々に変化させたカルシア安定
化ジルコニア原料粉末を用意した。この原料粉末にセラ
ミゾール等の分散剤、グリセリン等の可塑剤およびPVA
等の結合剤の他に、焼結体中の開気孔率が約38%となる
ように繊維状のセルロース等を加え、混合攪拌機を用い
て混合した。かくして得られた混合材を真空混練機を使
用して減圧下で混練しながら、口金部より該混練材を押
出成形し、中空の円筒状成形体を得た。次いで、前記円
筒状成形体をムライト等の治具を使用して焼成炉中に立
てて収納し、大気中1500〜1600℃の温度で2〜6時間焼
成して内径10mm、外径12mm、長さ200mmのカルシア安定
化ジルコニアよりなる円筒状焼結体を得た。A calcia-stabilized zirconia raw material powder containing 15 mol% of calcia, the total amount of additives being set to approximately 8% by weight, and varying the amounts of magnesia and alumina in all the additives as shown in Table 1 was prepared. did. Dispersants such as ceramisol, plasticizers such as glycerin, and PVA
In addition to such a binder, fibrous cellulose or the like was added so that the open porosity in the sintered body was about 38%, and mixed using a mixing stirrer. While kneading the thus obtained mixed material under reduced pressure using a vacuum kneader, the kneaded material was extruded from a die portion to obtain a hollow cylindrical molded body. Next, the cylindrical molded body is set up and stored in a firing furnace using a jig such as mullite, and fired in the atmosphere at a temperature of 1500 to 1600 ° C. for 2 to 6 hours, and the inner diameter is 10 mm, the outer diameter is 12 mm, and the length is longer. A cylindrical sintered body made of calcia-stabilized zirconia having a thickness of 200 mm was obtained.
次に、各円筒状焼結体の一端から分析用試料を切り出
し、ICP発光分光分析法によりマグネシア及びアルミナ
の量を測定した。また、各円筒状焼結体の側面の真直度
を真直度測定器により測定した。Next, a sample for analysis was cut out from one end of each cylindrical sintered body, and the amounts of magnesia and alumina were measured by ICP emission spectroscopy. The straightness of the side surface of each cylindrical sintered body was measured by a straightness measuring device.
さらに、加熱炉中にムライト等からなる支持治具を15
0mm離して設置し、該支持治具上に水平に上記円筒状焼
結体を載置し、大気中1450℃の温度で、2時間加熱処理
を施した。その後、真直度測定器により真直度を測定
し、加熱処理前後の真直度の差を最大変形量として、こ
の最大変形量を前記支持治具間距離で割った値を変形率
とした。Further, a supporting jig made of mullite or the like is placed in a heating furnace for 15 minutes.
The cylindrical sintered body was placed horizontally on the support jig, and subjected to a heat treatment at a temperature of 1450 ° C. in the atmosphere for 2 hours. Thereafter, the straightness was measured by a straightness measuring device, and a difference between the straightness before and after the heat treatment was defined as a maximum deformation amount, and a value obtained by dividing the maximum deformation amount by the distance between the support jigs was defined as a deformation ratio.
各円筒状焼結体の、全添加物量に対するマグネシア、
アルミナの割合、および熱処理後の変形率は第1表に示
す通りである。なお、固体電解質燃料電池用支持管に要
求される変形率は0.25%以下であることから、これを満
たすかどうかで○、×の判定を行った。Magnesia of each cylindrical sintered body with respect to the total amount of additives,
The ratio of alumina and the deformation ratio after heat treatment are as shown in Table 1. Since the deformation rate required for the support tube for a solid electrolyte fuel cell was 0.25% or less, it was judged whether the condition was satisfied or not.
第1表より、No.1〜12の円筒状焼結体はいずれも全添
加物量、気孔率は同じものであるが、マグネシア、アル
ミナの量によって熱処理後の変形率が異なることが理解
され、全添加物に対するマグネシア、アルミナの割合が
2.5重量%、5.0重量%をこえるNo.3,6,9,10,11,12では
変形率が0.25%より大きかった。これに対し、全添加物
に対するマグネシア、アルミナの割合が2.5重量%以
下、5.0重量%以下のものでは、いずれも変形率が0.25
%以下になり、前記要求範囲内となっていた。 From Table 1, it is understood that all of the cylindrical sintered bodies of Nos. 1 to 12 have the same total additive amount and porosity, but have different deformation rates after heat treatment depending on the amounts of magnesia and alumina. The ratio of magnesia and alumina to all additives is
In Nos. 3, 6, 9, 10, 11, and 12 exceeding 2.5% by weight and 5.0% by weight, the deformation ratio was larger than 0.25%. On the other hand, when the ratio of magnesia and alumina to all additives is 2.5% by weight or less and 5.0% by weight or less, the deformation ratio is 0.25% or less.
% Or less, which is within the required range.
なお、本実施例におけるカルシア安定化ジルコニア質
焼結体の添加物としては、上記マグネシア、アルミナの
他に、シリカ、チタニアが大部分を占めていた。また、
添加物中のマグネシアを低減するためには、カルシア原
料粉末の精製度を高め、高純度のものを用いればよく、
一方アルミナを低減するためには、たとえば原料粉砕時
の粉砕ボールをアルミナ製のものからジルコニア製のも
のに変更するなど製造工程中のアルミナ混入を防止すれ
ば良い。In addition, in addition to the above-mentioned magnesia and alumina, silica and titania occupied most of the additives of the calcia-stabilized zirconia sintered body in this example. Also,
In order to reduce magnesia in the additive, the purity of the calcia raw material powder is increased, and a high-purity material may be used.
On the other hand, in order to reduce the amount of alumina, it is only necessary to prevent the mixing of alumina during the manufacturing process, for example, by changing the grinding balls at the time of grinding the raw materials from those made of alumina to those made of zirconia.
叙上の如く、本発明においては固体電解質燃料電池用
支持管をなすカルシア安定化ジルコニア質焼結体中にお
けるマグネシア及びアルミナの含有量を全添加物量に対
し、それぞれ2.5重量%以下、5.0重量%以下としたこと
により、該支持管の熱変形を著しく軽減し、耐熱性の改
善された信頼性の高い高品質の固体電解質燃料電池用支
持管を得ることができる。As described above, in the present invention, the contents of magnesia and alumina in the calcia-stabilized zirconia sintered body forming the support tube for the solid oxide fuel cell are respectively 2.5% by weight or less and 5.0% by weight with respect to the total additive amount. By adopting the following conditions, thermal deformation of the support tube is remarkably reduced, and a highly reliable and high-quality support tube for a solid electrolyte fuel cell with improved heat resistance can be obtained.
第1図は本発明の固体電解質燃料電池用支持管を説明す
るための高温型固体電解質燃料電池の一部破断斜視図で
ある。 1……支持管 2……陽極 3……固体電解質 4……陰極FIG. 1 is a partially cutaway perspective view of a high-temperature type solid electrolyte fuel cell for illustrating a support tube for a solid oxide fuel cell of the present invention. DESCRIPTION OF SYMBOLS 1 ... Support tube 2 ... Anode 3 ... Solid electrolyte 4 ... Cathode
Claims (1)
体よりなる固体電解質燃料電池用支持管において、前記
カルシア安定化質ジルコニア質焼結体の主成分であるジ
ルコニアとカルシアを除く全添加物におけるマグネシア
及びアルミナの全添加物に対する割合をそれぞれ2.5重
量%以下、5.0重量%以下とすることにより、1450℃で
2時間加熱処理した後の変形率を0.25%以下としたこと
を特徴とする固体電解質燃料電池用支持管。1. A solid electrolyte fuel cell support tube comprising a porous calcia-stabilized zirconia sintered body, wherein all additives except for zirconia and calcia which are main components of the calcia-stabilized zirconia sintered body are provided. The solids are characterized in that the ratio of magnesia and alumina to the total additive in the above is 2.5% by weight or less and 5.0% by weight or less, respectively, so that the deformation rate after heat treatment at 1450 ° C for 2 hours is 0.25% or less. Support tube for electrolyte fuel cells.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1167425A JP2936331B2 (en) | 1989-06-29 | 1989-06-29 | Support tube for solid electrolyte fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1167425A JP2936331B2 (en) | 1989-06-29 | 1989-06-29 | Support tube for solid electrolyte fuel cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0334259A JPH0334259A (en) | 1991-02-14 |
| JP2936331B2 true JP2936331B2 (en) | 1999-08-23 |
Family
ID=15849463
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1167425A Expired - Fee Related JP2936331B2 (en) | 1989-06-29 | 1989-06-29 | Support tube for solid electrolyte fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2936331B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6386053B1 (en) | 1997-09-08 | 2002-05-14 | Ngk Insulators, Ltd. | Mass sensor and mass detection method |
| JP5086507B2 (en) * | 2001-09-28 | 2012-11-28 | 三菱重工業株式会社 | Manufacturing method of fuel cell tube and ceramic manufacturing apparatus |
| JP5284022B2 (en) * | 2008-09-19 | 2013-09-11 | 東京瓦斯株式会社 | Horizontally-striped solid oxide fuel cell stack and manufacturing method thereof |
-
1989
- 1989-06-29 JP JP1167425A patent/JP2936331B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0334259A (en) | 1991-02-14 |
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