JPH04315772A - Manufacture of interconnector for solid electrolyte fuel cell - Google Patents
Manufacture of interconnector for solid electrolyte fuel cellInfo
- Publication number
- JPH04315772A JPH04315772A JP3003107A JP310791A JPH04315772A JP H04315772 A JPH04315772 A JP H04315772A JP 3003107 A JP3003107 A JP 3003107A JP 310791 A JP310791 A JP 310791A JP H04315772 A JPH04315772 A JP H04315772A
- Authority
- JP
- Japan
- Prior art keywords
- lanthanum
- slurry
- chromate
- interconnector
- doped
- 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
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- 239000000446 fuel Substances 0.000 title claims description 4
- 239000007784 solid electrolyte Substances 0.000 title claims description 4
- DTDCCPMQHXRFFI-UHFFFAOYSA-N dioxido(dioxo)chromium lanthanum(3+) Chemical compound [La+3].[La+3].[O-][Cr]([O-])(=O)=O.[O-][Cr]([O-])(=O)=O.[O-][Cr]([O-])(=O)=O DTDCCPMQHXRFFI-UHFFFAOYSA-N 0.000 claims abstract description 17
- 238000000034 method Methods 0.000 claims abstract description 16
- HBAGRTDVSXKKDO-UHFFFAOYSA-N dioxido(dioxo)manganese lanthanum(3+) Chemical compound [La+3].[La+3].[O-][Mn]([O-])(=O)=O.[O-][Mn]([O-])(=O)=O.[O-][Mn]([O-])(=O)=O HBAGRTDVSXKKDO-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000002002 slurry Substances 0.000 claims abstract description 13
- 239000010409 thin film Substances 0.000 claims abstract description 9
- 230000007547 defect Effects 0.000 claims abstract description 7
- 230000003647 oxidation Effects 0.000 abstract 1
- 238000007254 oxidation reaction Methods 0.000 abstract 1
- 239000010408 film Substances 0.000 description 8
- 238000005245 sintering Methods 0.000 description 5
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 230000002411 adverse Effects 0.000 description 2
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 2
- 150000001342 alkaline earth metals Chemical class 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 229910020854 La(OH)3 Inorganic materials 0.000 description 1
- 229910016978 MnOx Inorganic materials 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011195 cermet Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 229910052712 strontium Inorganic materials 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 238000007751 thermal spraying Methods 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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0215—Glass; Ceramic materials
-
- 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
- H01M2008/1293—Fuel cells with solid oxide electrolytes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2300/00—Electrolytes
- H01M2300/0017—Non-aqueous electrolytes
- H01M2300/0065—Solid electrolytes
- H01M2300/0068—Solid electrolytes inorganic
- H01M2300/0071—Oxides
- H01M2300/0074—Ion conductive at high temperature
-
- 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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0215—Glass; Ceramic materials
- H01M8/0217—Complex oxides, optionally doped, of the type AMO3, A being an alkaline earth metal or rare earth metal and M being a metal, e.g. perovskites
- H01M8/0219—Chromium complex oxides
-
- 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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Fuel Cell (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は、固体電解質燃料電池用
インターコネクターの製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing an interconnector for solid electrolyte fuel cells.
【0002】0002
【従来の技術及び発明が解決しようとする課題】固体電
解質燃料電池用インターコネクターには、1,000℃
の高温で酸化還元の両雰囲気に対して安定であること、
及び、ある程度以上の電子伝導性を有することが求めら
れる。このようなインターコネクターの製造には、ほと
んどの場合、アルカリ土類金属(Ca、Sr、Mg等)
をドープしたランタンクロメート(LaCrOx)が用
いられている。しかし、このようなLaCrOxは難焼
結性であり、常法では温度を1,600℃まで上げなけ
れば焼結しないため、インターコネクターの製造は必ず
しも容易ではなかった。[Prior Art and Problems to be Solved by the Invention] Interconnectors for solid electrolyte fuel cells have a temperature of 1,000℃.
be stable in both redox and redox atmospheres at high temperatures;
In addition, it is required to have a certain level of electronic conductivity. The manufacture of such interconnectors mostly involves the use of alkaline earth metals (Ca, Sr, Mg, etc.)
Lanthanum chromate (LaCrOx) doped with is used. However, such LaCrOx is difficult to sinter, and cannot be sintered by conventional methods unless the temperature is raised to 1,600° C., so it has not always been easy to manufacture interconnectors.
【0003】そのため、過去には次のような方法が試み
られていた。[0003] For this reason, the following methods have been attempted in the past.
【0004】1.LaCrOxを単独で焼結し、他の部
材と接合する方法。1. A method of sintering LaCrOx alone and joining it with other parts.
【0005】2.ランタンマンガネ―ト(LaMnOx
)あるいはNi/ZrO2サーメット等の電極材料多孔
質体上にCVD、EVD、溶射等のドライプロセスでL
aCrOx薄膜を形成する方法。2. Lanthanum manganate (LaMnOx)
) or by a dry process such as CVD, EVD, or thermal spraying on a porous electrode material such as Ni/ZrO2 cermet.
A method of forming aCrOx thin film.
【0006】前者の場合には、内部抵抗の制約から膜の
厚さが限られるため膜面積が大きくできないといった欠
点や、形状が平板類似のものに限られるといった欠点が
あった。一方、後者の場合にはドライプロセスであるた
め設備費が大きくなるという欠点があった。In the former case, the thickness of the film is limited due to internal resistance constraints, so the film area cannot be increased, and the shape is limited to a flat plate. On the other hand, the latter method has the disadvantage that the equipment cost is high because it is a dry process.
【0007】また、Caド―プLaCrOxを用いた共
焼結法も試みられたが、CaO相の移動によりLaMn
OxやNi/ZrO2サーメットの焼結が妨げられると
いう欠点があった。A co-sintering method using Ca-doped LaCrOx was also attempted, but due to the movement of the CaO phase, LaMn
There was a drawback that sintering of Ox and Ni/ZrO2 cermets was hindered.
【0008】本発明の課題は、上記欠点を解消し、La
MnOx焼結体上にLaCrOx薄膜をウェットプロセ
スで成膜する方法を提供する処にある。このような方法
によれば、大面積あるいは非平面のインターコネクター
が容易に得られるという利点もある。The object of the present invention is to solve the above-mentioned drawbacks and to solve the problem of La
The present invention provides a method for forming a LaCrOx thin film on a MnOx sintered body by a wet process. This method also has the advantage that large-area or non-planar interconnectors can be easily obtained.
【0009】[0009]
【課題を解決するための手段】Aサイト欠陥を有するア
ルカリ土類金属ドープランタンマンガネートからなる多
孔質体上に、Aサイト過剰のカルシウムドープランタン
クロメートのスラリーを薄膜状に塗布し、これを酸化雰
囲気で焼結させる。[Means for solving the problem] A slurry of calcium-doped lanthanum chromate with an excess of A sites is applied in a thin film onto a porous body made of alkaline earth metal-doped lanthanum manganate having A-site defects, and this is oxidized. Sinter in the atmosphere.
【0010】ランタンクロメートのスラリーを真空吸引
法により塗布することが好ましい。Preferably, the lanthanum chromate slurry is applied by vacuum suction.
【0011】[0011]
【作用】AサイトにCaを過剰にドープしたランタンク
ロメート(例えば、La0.70Ca0.35CrOx
;式中xは3±δ)は易焼結性のランタンクロメートと
して知られている。このスラリーを用いて、アルカリ土
類金属をドープしたAサイト欠陥を有するランタンマン
ガネートからなる多孔質体上に薄膜を形成し、これを約
1,300℃で焼成すると、ランタンマンガネートの多
孔質体上にランタンクロメートの緻密な薄膜が形成され
る。この際、ランタンマンガネートは再焼結しない(ラ
ンタンマンガネートは約1,350℃まで昇温しないと
再焼結しない。)ランタンクロメート中の過剰のCaは
粒子間にCaO相を作り、この一部がLaMnOx相へ
移動するが、LaMnOxはすでに焼結されているので
悪影響を受けない。また、LaMnOxとの反応という
点ではLaMnOx中のAサイト欠陥にCaが配位する
ため悪影響を受けにくい。[Action] Lanthanum chromate doped with excessive Ca at the A site (for example, La0.70Ca0.35CrOx
; where x is 3±δ) is known as an easily sinterable lanthanum chromate. Using this slurry, a thin film is formed on a porous body made of lanthanum manganate doped with an alkaline earth metal and having A-site defects, and when this is fired at about 1,300°C, the porous lanthanum manganate A dense thin film of lanthanum chromate forms on the body. At this time, lanthanum manganate does not resinter (lanthanum manganate does not resinter unless the temperature is raised to approximately 1,350°C). Excess Ca in lanthanum chromate creates a CaO phase between particles, and this However, since LaMnOx has already been sintered, it is not adversely affected. In addition, in terms of reaction with LaMnOx, Ca is coordinated to the A-site defects in LaMnOx, so that it is less likely to be adversely affected.
【0012】また、ランタンクロメートのスラリーを真
空吸引法により塗布すれば、円筒などの曲面にも成膜す
ることができる。Furthermore, by applying the lanthanum chromate slurry by vacuum suction, it is possible to form a film on a curved surface such as a cylinder.
【0013】[0013]
実施例1
SrをドープしたAサイト欠陥を有するランタンマンガ
ネート[(La0.9Sr0.1)0.9MnO3±δ
]の多孔質円筒上に、La0.70Ca0.35CrO
3±δ粉末(平均粒径2μm)のスラリー(LaCaC
rOx粉が50〜70重量%、他は水、ポリビニルアル
コール及び界面活性剤)を真空吸引により成膜し、室温
で乾燥した後に空気中で1,300℃で5時間焼成した
。その結果、厚さ30μmのLaCaCrOxの緻密膜
が得られた。Example 1 Sr-doped lanthanum manganate with A-site defects [(La0.9Sr0.1)0.9MnO3±δ
] on the porous cylinder of La0.70Ca0.35CrO
Slurry of 3±δ powder (average particle size 2 μm) (LaCaC
A film containing 50 to 70% by weight of rOx powder (others being water, polyvinyl alcohol, and surfactant) was formed by vacuum suction, dried at room temperature, and then calcined in air at 1,300° C. for 5 hours. As a result, a dense film of LaCaCrOx with a thickness of 30 μm was obtained.
【0014】得られた膜を1,100℃で500時間処
理したが、電気物性や機械物性において実用上支障のあ
る変化はみられなかった。[0014] The obtained film was treated at 1,100°C for 500 hours, but no practically harmful changes were observed in the electrical or mechanical properties.
【0015】比較例1
実施例1と同じ多孔質円筒上に真空吸引をせずにスラリ
ーを塗布し、同様の焼成を行なったが、得られた膜はガ
ス透過性があり、緻密な膜は得られなかった。
比較例2
Aサイト過剰でないカルシウムドープランタンクロメー
ト(La0.84Ca0.16CrO3±δ)粉末を用
いて実施例1と同様の実験を行なったが、まったく焼結
しなかった。Comparative Example 1 A slurry was applied onto the same porous cylinder as in Example 1 without vacuum suction, and the same firing was performed, but the resulting film was gas permeable and the dense film was I couldn't get it. Comparative Example 2 An experiment similar to Example 1 was conducted using calcium-doped lanthanum chromate (La0.84Ca0.16CrO3±δ) powder that did not have an excess of A sites, but no sintering occurred.
【0016】比較例3
Aサイト欠陥でないストロンチウムドープランタンマン
ガネート(La0.9Sr0.1MnO3±δ)の多孔
質円筒を用いて同様の実験を行なったところ、Caがド
ープしてAサイト過剰となり、空気中のH2Oを吸収し
てLa(OH)3・nH2Oを生じたため、円筒の強度
が大幅に低下した。Comparative Example 3 When a similar experiment was carried out using a porous cylinder of strontium-doped lanthanum manganate (La0.9Sr0.1MnO3±δ) with no A-site defects, the A-site was excessive due to Ca doping, and air Since the H2O inside was absorbed and La(OH)3.nH2O was produced, the strength of the cylinder was significantly reduced.
【0017】[0017]
【発明の効果】本発明によれば、ランタンマンガネート
焼結体上にランタンクロメート薄膜をウェットプロセス
で成膜することができる。従って、設備費を低価に抑え
ることができる。According to the present invention, a lanthanum chromate thin film can be formed on a lanthanum manganate sintered body by a wet process. Therefore, equipment costs can be kept low.
【0018】また、CaO相の移動によりLaMnOx
の焼結が妨げられるということも生じない。Furthermore, due to the movement of the CaO phase, LaMnOx
The sintering of the material is not hindered.
【0019】さらに、ランタンクロメートのスラリーを
真空吸引法により塗布すれば、非平面のインターコネク
ターが容易に得られる。Furthermore, a non-planar interconnector can be easily obtained by applying a slurry of lanthanum chromate by a vacuum suction method.
Claims (3)
ープランタンマンガネートからなる多孔質体上に、Aサ
イト過剰のカルシウムドープランタンクロメートのスラ
リーを薄膜状に塗布し、これを焼結させる固体電解質燃
料電池用インターコネクターの製造方法。Claim 1: A solid electrolyte in which a slurry of calcium-doped lanthanum chromate with an excess of A sites is applied in a thin film form on a porous body made of alkaline earth metal-doped lanthanum manganate having A-site defects, and the slurry is sintered. A method for manufacturing a fuel cell interconnector.
法により塗布することを特徴とする請求項1記載の方法
。2. The method according to claim 1, wherein the lanthanum chromate slurry is applied by vacuum suction.
ンタンクロメートスラリーを塗布すべき面が平面でない
ことを特徴とする請求項2記載の方法。3. The method according to claim 2, wherein the surface of the lanthanum manganate porous body to which the lanthanum chromate slurry is applied is not flat.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP03003107A JP3101720B2 (en) | 1991-01-16 | 1991-01-16 | Method for manufacturing interconnector for solid oxide fuel cell |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP03003107A JP3101720B2 (en) | 1991-01-16 | 1991-01-16 | Method for manufacturing interconnector for solid oxide fuel cell |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04315772A true JPH04315772A (en) | 1992-11-06 |
JP3101720B2 JP3101720B2 (en) | 2000-10-23 |
Family
ID=11548126
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP03003107A Expired - Fee Related JP3101720B2 (en) | 1991-01-16 | 1991-01-16 | Method for manufacturing interconnector for solid oxide fuel cell |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3101720B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1997004494A1 (en) * | 1995-07-21 | 1997-02-06 | Siemens Aktiengesellschaft | High-temperature fuel cell and high-temperature fuel cell stack with interconnecting conducting plates provided with a chromium spinel contact layer |
-
1991
- 1991-01-16 JP JP03003107A patent/JP3101720B2/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1997004494A1 (en) * | 1995-07-21 | 1997-02-06 | Siemens Aktiengesellschaft | High-temperature fuel cell and high-temperature fuel cell stack with interconnecting conducting plates provided with a chromium spinel contact layer |
AU695778B2 (en) * | 1995-07-21 | 1998-08-20 | Siemens Aktiengesellschaft | High temperature fuel cell, high temperature fuel cell stack and method for producing a high temperature fuel cell |
Also Published As
Publication number | Publication date |
---|---|
JP3101720B2 (en) | 2000-10-23 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AU2008291251B2 (en) | Removal of impurity phases from electrochemical devices | |
Chen et al. | Direct application of cobaltite-based perovskite cathodes on the yttria-stabilized zirconia electrolyte for intermediate temperature solid oxide fuel cells | |
Shang et al. | A promising cathode for intermediate temperature protonic ceramic fuel cells: BaCo 0.4 Fe 0.4 Zr 0.2 O 3− δ | |
Wang et al. | Liquid-phase synthesis of SrCo0. 9Nb0. 1O3-δ cathode material for proton-conducting solid oxide fuel cells | |
JP5465240B2 (en) | Sol-gel derived high performance catalytic thin films for sensors, oxygen separators, and solid oxide fuel cells | |
JPH05135787A (en) | Manufacture of solid electrolyte film and manufacture of solid electrolyte fuel cell | |
KR101978952B1 (en) | High temperature solid oxide cell comprising barrier layer, method for manufacturing the same | |
WO1992010862A1 (en) | Method for manufacturing solid-state electrolytic fuel cell | |
US8337939B2 (en) | Method of processing a ceramic layer and related articles | |
CN110797542A (en) | Symmetric solid oxide fuel cell electrode material and preparation method thereof | |
CN107017423A (en) | A kind of low-temperature solid oxide fuel cell and preparation method thereof | |
Zhou et al. | Novel metal-supported solid oxide fuel cells with impregnated symmetric La0. 6Sr0. 4Fe0. 9Sc0. 1O3− δ electrodes | |
Sun et al. | Fabrication of BaZr0. 1Ce0. 7Y0. 2O3–δ‐Based Proton‐Conducting Solid Oxide Fuel Cells Co‐Fired at 1,150° C | |
US20080299436A1 (en) | Composite ceramic electrolyte structure and method of forming; and related articles | |
JP3565696B2 (en) | Method for manufacturing electrode of solid oxide fuel cell | |
EP0478185A2 (en) | Fuel electrodes for solid oxide fuel cells and production thereof | |
JP2008047445A (en) | Method of manufacturing solid electrolytic ceramic membrane, and electrochemical device | |
JP3661676B2 (en) | Solid oxide fuel cell | |
CN113991122A (en) | Electrode material with core-shell structure for symmetric solid oxide fuel cell and preparation method and application thereof | |
Xin et al. | Fabrication of dense YSZ electrolyte membranes by a modified dry-pressing using nanocrystalline powders | |
Yamamoto et al. | Anomalous low-temperature sintering of a solid electrolyte thin film of tailor-made nanocrystals on a porous cathode support for low-temperature solid oxide fuel cells | |
JP2014159642A (en) | Method for fabricating nickel-cermet electrode | |
JPH04315772A (en) | Manufacture of interconnector for solid electrolyte fuel cell | |
JP4889166B2 (en) | Low-temperature sinterable solid electrolyte material, electrolyte electrode assembly and solid oxide fuel cell using the same | |
JP5550223B2 (en) | Ceramic electrolyte processing method and related products |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |