JP3166333B2 - Ceramic coating method - Google Patents
Ceramic coating methodInfo
- Publication number
- JP3166333B2 JP3166333B2 JP24878192A JP24878192A JP3166333B2 JP 3166333 B2 JP3166333 B2 JP 3166333B2 JP 24878192 A JP24878192 A JP 24878192A JP 24878192 A JP24878192 A JP 24878192A JP 3166333 B2 JP3166333 B2 JP 3166333B2
- Authority
- JP
- Japan
- Prior art keywords
- coating
- layer
- ceramic substrate
- porous
- slurry
- 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
- 238000000034 method Methods 0.000 title claims description 13
- 238000005524 ceramic coating Methods 0.000 title description 2
- 239000010410 layer Substances 0.000 claims description 29
- 239000000919 ceramic Substances 0.000 claims description 25
- 238000000576 coating method Methods 0.000 claims description 19
- 239000000758 substrate Substances 0.000 claims description 17
- 239000011248 coating agent Substances 0.000 claims description 16
- 239000000446 fuel Substances 0.000 claims description 14
- 239000000463 material Substances 0.000 claims description 12
- 238000005507 spraying Methods 0.000 claims description 10
- 238000007598 dipping method Methods 0.000 claims description 9
- 239000007784 solid electrolyte Substances 0.000 claims description 8
- 239000011247 coating layer Substances 0.000 claims description 7
- 239000007787 solid Substances 0.000 claims description 3
- 239000007921 spray Substances 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 description 10
- 229910052760 oxygen Inorganic materials 0.000 description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 8
- 239000007789 gas Substances 0.000 description 7
- 239000002245 particle Substances 0.000 description 6
- 239000002002 slurry Substances 0.000 description 6
- 238000007751 thermal spraying Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 238000007581 slurry coating method Methods 0.000 description 3
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 229910001882 dioxygen Inorganic materials 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- -1 oxygen ions Chemical class 0.000 description 2
- 230000035699 permeability Effects 0.000 description 2
- 238000005240 physical vapour deposition Methods 0.000 description 2
- WUOACPNHFRMFPN-SECBINFHSA-N (S)-(-)-alpha-terpineol Chemical compound CC1=CC[C@@H](C(C)(C)O)CC1 WUOACPNHFRMFPN-SECBINFHSA-N 0.000 description 1
- 239000001856 Ethyl cellulose Substances 0.000 description 1
- ZZSNKZQZMQGXPY-UHFFFAOYSA-N Ethyl cellulose Chemical compound CCOCC1OC(OC)C(OCC)C(OCC)C1OC1C(O)C(O)C(OC)C(CO)O1 ZZSNKZQZMQGXPY-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- OVKDFILSBMEKLT-UHFFFAOYSA-N alpha-Terpineol Natural products CC(=C)C1(O)CCC(C)=CC1 OVKDFILSBMEKLT-UHFFFAOYSA-N 0.000 description 1
- 229940088601 alpha-terpineol Drugs 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 239000002518 antifoaming agent Substances 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 238000005229 chemical vapour deposition Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 229920001249 ethyl cellulose Polymers 0.000 description 1
- 235000019325 ethyl cellulose Nutrition 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000010285 flame spraying Methods 0.000 description 1
- 238000007429 general method Methods 0.000 description 1
- 238000007733 ion plating Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000004544 sputter deposition Methods 0.000 description 1
- 238000001771 vacuum deposition Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B41/00—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
- C04B41/009—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone characterised by the material treated
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B41/00—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
- C04B41/45—Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements
- C04B41/52—Multiple coating or impregnating multiple coating or impregnating with the same composition or with compositions only differing in the concentration of the constituents, is classified as single coating or impregnation
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2111/00—Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
- C04B2111/00474—Uses not provided for elsewhere in C04B2111/00
- C04B2111/00853—Uses not provided for elsewhere in C04B2111/00 in electrochemical cells or batteries, e.g. fuel cells
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Inert Electrodes (AREA)
- Fuel Cell (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は組織の緻密な吸水性の低
いセラミック基材へのコーティング方法に関し、特に燃
料電池等のセラミック多孔質電極を形成するためのセラ
ミックスのコーティング方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for coating a ceramic substrate having a fine structure and low water absorption, and more particularly to a method for coating a ceramic for forming a ceramic porous electrode of a fuel cell or the like.
【0002】[0002]
【従来の技術】一般的なセラミックスのコーティング方
法としては、プラズマトーチ炎溶射、ガス爆発式溶射等
の溶射法、スパッタリング、イオンプレーティング、真
空蒸着等のPVD法、CVD法或いはスラリー状のコー
ティング材をセラミック基材表面に流して被覆するスラ
リーコート法等が知られている。2. Description of the Related Art As a general method of coating ceramics, there are spraying methods such as plasma torch flame spraying, gas explosion type spraying, PVD method such as sputtering, ion plating and vacuum deposition, CVD method, and slurry coating material. And a slurry coating method in which the slurry is applied to the surface of a ceramic base material to cover the surface.
【0003】また緻密なセラミックスへのコーティング
に関して、例えば燃料電池については、酸素イオンが透
過可能でイオン化していない酸素ガスや水素ガスが透過
できない程度に緻密な固体電解質膜の両面に、ガスが浸
透し得る程度に粗な多孔質電極層を形成した構造になっ
ている。このような多孔質電極層は例えば溶射法による
コーティングによって、上記の緻密な固体電解質基材の
表面に形成されている。[0003] Regarding the coating of dense ceramics, for example, in the case of a fuel cell, gas permeates both surfaces of a solid electrolyte membrane which is permeable to oxygen ions but not permeable to non-ionized oxygen gas or hydrogen gas. The structure is such that a porous electrode layer as coarse as possible can be formed. Such a porous electrode layer is formed on the surface of the above-mentioned dense solid electrolyte substrate by, for example, coating by a thermal spraying method.
【0004】[0004]
【発明が解決しようとする課題】上述の溶射法について
は、燃料電池の電極以外のものを形成する場合において
も、一般に溶融粒子が沈降してしまうために形成される
コーティング層組織の制御ができず、緻密になり過ぎて
しまう問題がある。また、溶射法、PVD法及びCVD
法は厚膜化が困難であること、コストが嵩むこと等の不
利がある。更に、スラリーコート法は一般にセラミック
基材との密着性が悪いのが難点である。In the above-mentioned thermal spraying method, even when a material other than an electrode of a fuel cell is formed, the structure of the coating layer formed due to the sedimentation of molten particles generally can be controlled. However, there is a problem that it becomes too dense. In addition, thermal spraying, PVD and CVD
The method has disadvantages such as difficulty in increasing the film thickness and increase in cost. Further, the slurry coating method is generally disadvantageous in that it has poor adhesion to a ceramic substrate.
【0005】また燃料電池の電極について、その要求さ
れる特性としては、ガス透過性及び電気伝導度に優れて
いること等が挙げられる。このためには平均孔径を0.
1〜10μm程度に、気孔率を10〜50容量%程度に
することが必要である。しかしながら、従来のように溶
射法で電極を形成すると、電極の構成粒子の大きさを制
御することができないため、極めて不均一な組織となり
ガス浸透性が低下して燃料電池の効率が悪くなる。[0005] The characteristics required of an electrode of a fuel cell include excellent gas permeability and electric conductivity. For this purpose, the average pore size is set at 0.
It is necessary to set the porosity to about 1 to 10 μm and the porosity to about 10 to 50% by volume. However, when an electrode is formed by a thermal spraying method as in the prior art, the size of the constituent particles of the electrode cannot be controlled, resulting in an extremely non-uniform structure, lowering gas permeability and lowering the efficiency of the fuel cell.
【0006】[0006]
【課題を解決するための手段】上記課題を解決すべく本
発明の方法は、第1の工程として組織の緻密なセラミッ
ク基材上へスラリー状のコーティング材をスプレーコー
ティングし、吸水性を有する多孔質層を形成する。そし
て第2の工程として、この多孔質層面に更にディッピン
グによって表皮層をコーティングするものである。In order to solve the above-mentioned problems, the method of the present invention comprises, as a first step, a step of spray-coating a slurry-like coating material on a fine-textured ceramic substrate to form a porous material having a water-absorbing property. Forming a porous layer. As a second step, the surface of the porous layer is further coated with a skin layer by dipping.
【0007】[0007]
【作用】第1の工程において、緻密なセラミック基材上
へスラリー状のコーティング材をスプレーコーティング
する場合、飛行中に半乾燥状態となったコーティング材
はセラミック基材上へ密着後乾燥しながら堆積されてい
く。従って、組成の安定したコーティング層を任意の膜
厚に形成することが可能である。またこのコーティング
層は多孔質であるため、第2の工程でディッピングによ
って形成されるコーティング層との密着性も良好であ
る。In the first step, when a slurry-like coating material is spray-coated on a dense ceramic substrate, the coating material which has become semi-dry during flight is deposited on the ceramic substrate while being dried after being brought into close contact with the ceramic substrate. Will be done. Therefore, it is possible to form a coating layer having a stable composition to an arbitrary thickness. Further, since this coating layer is porous, the adhesion to the coating layer formed by dipping in the second step is also good.
【0008】[0008]
【実施例】以下に本発明の実施例を添付図面に基づいて
説明する。ここにおいて図1は本発明の第1の工程に係
るスプレーコーティングの一例を示す概略図であり、図
2は本発明の第2の工程に係るディッピング装置の概略
図である。また図3は本発明に係る多孔質電極を形成し
た燃料電池用素子の斜視図であり、図4は図3の多孔質
電極の粒子構造を示す図である。Embodiments of the present invention will be described below with reference to the accompanying drawings. Here, FIG. 1 is a schematic view showing an example of the spray coating according to the first step of the present invention, and FIG. 2 is a schematic view of a dipping apparatus according to the second step of the present invention. FIG. 3 is a perspective view of a fuel cell element on which a porous electrode according to the present invention is formed, and FIG. 4 is a view showing a particle structure of the porous electrode of FIG.
【0009】図1においては、中空の緻密なセラミック
基材1を回転体2に水平方向に固定し、この回転体2を
定速回転させながら前記第1の工程のスプレーコーティ
ングを行っている(矢印はコーティング材の飛来する方
向である)。このようにセラミック基材1を定速回転さ
せながらスラリーを吹き付けることにより、液だれを起
こすことなく、吸水性のある均質な多孔質層をセラミッ
ク基材1上に密着性よく形成することができる。またこ
の方法によれば、スプレー時間等の条件を調整すること
により、任意の厚さの多孔質層を形成することができ
る。回転体2を用いたスプレーコーティングは特に燃料
電池用等の酸素分離素子3の円筒型緻密セラミックスに
有用である。In FIG. 1, a hollow dense ceramic base material 1 is fixed to a rotating body 2 in a horizontal direction, and spray coating in the first step is performed while rotating the rotating body 2 at a constant speed. The arrow indicates the direction of the coating material). By spraying the slurry while rotating the ceramic substrate 1 at a constant speed in this manner, a uniform porous layer having water absorption can be formed on the ceramic substrate 1 with good adhesion without dripping. . Further, according to this method, a porous layer having an arbitrary thickness can be formed by adjusting conditions such as a spray time. Spray coating using the rotating body 2 is particularly useful for dense cylindrical ceramics of the oxygen separation element 3 for fuel cells and the like.
【0010】上記固体電解質型燃料電池用の酸素分離素
子3は、図3に示すように、ガス透過可能な円筒状多孔
質支持体4の表面に同じくガス透過可能な多孔質電極
(空気極)5を形成し、この多孔質電極5の表面に酸素
イオンのみを透過させて分子状態の酸素ガスを透過させ
ない緻密な固体電解質層6を形成し、この固体電解質層
6の表面にガス透過可能な多孔質電極(燃料極)7を形
成している。この多孔質電極7は本発明の第1の工程に
よって形成される多孔質層7a及び第2の工程によって
形成される多孔質の表皮層7bの二層構造である。As shown in FIG. 3, the oxygen separation element 3 for a solid oxide fuel cell has a porous electrode (air electrode) which is also gas permeable on the surface of a gas permeable cylindrical porous support 4. 5, a dense solid electrolyte layer 6 is formed on the surface of the porous electrode 5 that allows only oxygen ions to pass therethrough and does not allow oxygen gas in a molecular state to pass therethrough, and gas is permeable to the surface of the solid electrolyte layer 6. A porous electrode (fuel electrode) 7 is formed. This porous electrode 7 has a two-layer structure of a porous layer 7a formed by the first step of the present invention and a porous skin layer 7b formed by the second step.
【0011】上記固体電解質層6は低酸素側領域S1と
高酸素側領域S2とを仕切っているが、多孔質電極5、
7間に電圧を印加することで高酸素側領域S2の酸素は
イオンとして固体電解質層6を通して低酸素側領域S1
に移動できる。The solid electrolyte layer 6 partitions the low oxygen side region S1 and the high oxygen side region S2.
The oxygen in the high oxygen side region S2 passes through the solid electrolyte layer 6 as ions by applying a voltage between the low oxygen side regions S1
Can be moved to
【0012】なお上記多孔質支持体4はアルミナ等のセ
ラミックコンパウンドを押出し成形することで未焼成成
形体を得た後、この成形体を吊り焼き等の手段で焼成し
て作製したものである。また多孔質電極5、7a、7b
は図4に示すように構成粒子12(図の黒い部分)同士
が十分に結合するとともに、所定の平均孔径及び気孔率
を確保している必要がある。The porous support 4 is prepared by extruding a ceramic compound such as alumina to obtain a green body, and then firing the green body by means such as hanging grilling. Also, the porous electrodes 5, 7a, 7b
As shown in FIG. 4, it is necessary that the constituent particles 12 (black portions in the figure) are sufficiently bonded to each other and that a predetermined average pore diameter and porosity are secured.
【0013】上記固体電解質型燃料電池の緻密な固体電
解質層6上に、多孔質層7aをスプレーによって形成す
るためのスラリー状コーティング材の例を以下に示す。 金属酸化物微粒子(粒度は用途に応じて選定する。) NiO、ZrO2等 2〜40重量% バインダー エチルセルロース等 2〜14重量% 溶剤 エタノール 5〜95重量%(好ましくは40〜60重量%) α−テルピネオール 5〜95重量%(好ましくは40〜60重量%) その他、必要に応じて分散材、脱泡剤を添加する。この
スラリーの粘度は10〜1000cpsが好ましく、3
0〜300cpsが更に好ましい。このようなスラリー
状コーティング材によって多孔質層7aを数十μm程度
の厚さに形成し、乾燥及び焼成を行うことにより、吸水
性のある多孔質層7aとすることができる。An example of a slurry-like coating material for forming the porous layer 7a on the dense solid electrolyte layer 6 of the solid oxide fuel cell by spraying is shown below. Metal oxide fine particles (particle size selected depending on the application.) NiO, ZrO 2, etc. 2 to 40 wt% binder such as ethyl cellulose 2 to 14 wt% solvent ethanol 5-95% (preferably 40 to 60% by weight) alpha -Terpineol 5 to 95% by weight (preferably 40 to 60% by weight) In addition, a dispersant and a defoaming agent are added as necessary. The viscosity of the slurry is preferably 10 to 1000 cps,
0 to 300 cps is more preferable. The porous layer 7a having a water absorbing property can be formed by forming the porous layer 7a to a thickness of about several tens of μm using such a slurry-like coating material and performing drying and baking.
【0014】次に、上記第2の工程であるディッピング
による表皮層7bのコーティングを行う。この方法は例
えば図2に示すように、容器8に例えばNiOとZrO2
の複合酸化物からなるスラリー9を入れ、スターラ11
にて攪拌子10を回転せしめることで均一にスラリー9
を攪拌し、この中に多孔質層で被覆したセラミック基材
1を浸漬することで、セラミック基材1の表面に未焼成
の複合酸化物の表皮層7bを形成することができる。こ
の層をクラックが発生しない条件で十分乾燥させた後、
焼成することで製膜する。Next, coating of the skin layer 7b by dipping, which is the second step, is performed. The method as shown in FIG. 2, for example, to a container 8 for example NiO and ZrO 2
Slurry 9 made of the composite oxide of
By rotating the stirrer 10 in the slurry 9
Is stirred, and the ceramic substrate 1 covered with the porous layer is immersed therein, whereby the unfired composite oxide skin layer 7b can be formed on the surface of the ceramic substrate 1. After thoroughly drying this layer under conditions that do not cause cracks,
A film is formed by firing.
【0015】上記ディッピング用スラリーへの浸漬時間
或いは浸漬回数を変化させることによって、表皮層7b
の厚さを調節することが可能である。By changing the dipping time or the number of times of dipping in the dipping slurry, the skin layer 7 b
Can be adjusted in thickness.
【0016】[0016]
【発明の効果】本発明のセラミックスコーティング方法
によれば、吸水性のない緻密なセラミック基材に対して
も密着性よく堅固なコーティング層を形成することがで
きる。また形成されるコーティング層は、組成が均一で
あり、厚さも自在に調節することができる。According to the ceramic coating method of the present invention, a firm coating layer having good adhesion can be formed even on a dense ceramic substrate having no water absorption. The coating layer to be formed has a uniform composition and its thickness can be freely adjusted.
【図1】本発明の第1の工程に係るスプレーコーティン
グの一例を示す概略図FIG. 1 is a schematic view showing an example of spray coating according to a first step of the present invention.
【図2】本発明の第2の工程に係るディッピング装置の
概略図FIG. 2 is a schematic diagram of a dipping apparatus according to a second step of the present invention.
【図3】本発明に係る多孔質電極を形成した燃料電池素
子の斜視図FIG. 3 is a perspective view of a fuel cell element having a porous electrode according to the present invention.
【図4】図3の多孔質電極の粒子構造を示す図FIG. 4 is a view showing a particle structure of the porous electrode of FIG. 3;
1…セラミック基材、2…回転体、3…酸素分離素子、
4…多孔質支持体、5、7a…多孔質層、7b…表皮
層、11…スターラ。DESCRIPTION OF SYMBOLS 1 ... Ceramic base material, 2 ... Rotating body, 3 ... Oxygen separation element,
4 ... porous support, 5, 7a ... porous layer, 7b ... skin layer, 11 ... stirrer.
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C04B 41/80 - 41/91 B05D 1/00 - 7/26 ──────────────────────────────────────────────────続 き Continuation of the front page (58) Field surveyed (Int. Cl. 7 , DB name) C04B 41/80-41/91 B05D 1/00-7/26
Claims (4)
ィングする方法において、スラリー状のコーティング材
をスプレーコーティングすることによって、前記セラミ
ック基材表面に吸水性を有する多孔質層を形成する第1
の工程と、この多孔質層面に更にディッピングによって
表皮層をコーティングする第2の工程とを含むことを特
徴とするセラミックスのコーティング方法。In a method of coating on a ceramic substrate having a dense structure, a slurry-like coating material is spray-coated to form a water-absorbing porous layer on the surface of the ceramic substrate. The first to form
And a second step of further coating the skin layer by dipping on the surface of the porous layer.
は、前記セラミック基材を回転体に水平方向に固定し、
この回転体を定速回転させながら行うことを特徴とする
請求項1に記載のコーティング方法。2. The spray coating in the first step, wherein the ceramic substrate is horizontally fixed to a rotating body,
The coating method according to claim 1, wherein the coating is performed while rotating the rotating body at a constant speed.
項1又は2に記載のコーティング方法。3. The coating method according to claim 1, wherein the ceramic substrate has a cylindrical shape.
電池の固体電解質層であり、前記第1の工程及び第2の
工程によって形成されるコーティング層が燃料極である
請求項1乃至3のいずれか1項に記載のコーティング方
法。4. The fuel cell according to claim 1, wherein the ceramic substrate is a solid electrolyte layer of a solid oxide fuel cell, and the coating layer formed in the first and second steps is a fuel electrode. The coating method according to claim 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24878192A JP3166333B2 (en) | 1992-08-25 | 1992-08-25 | Ceramic coating method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24878192A JP3166333B2 (en) | 1992-08-25 | 1992-08-25 | Ceramic coating method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0672787A JPH0672787A (en) | 1994-03-15 |
| JP3166333B2 true JP3166333B2 (en) | 2001-05-14 |
Family
ID=17183300
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24878192A Expired - Fee Related JP3166333B2 (en) | 1992-08-25 | 1992-08-25 | Ceramic coating method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3166333B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3335780B2 (en) * | 1994-08-31 | 2002-10-21 | 富士重工業株式会社 | Body structure below the center pillar of the vehicle |
| JP5305131B2 (en) * | 2008-05-21 | 2013-10-02 | Toto株式会社 | Fuel cell and fuel cell |
| US8652707B2 (en) * | 2011-09-01 | 2014-02-18 | Watt Fuel Cell Corp. | Process for producing tubular ceramic structures of non-circular cross section |
-
1992
- 1992-08-25 JP JP24878192A patent/JP3166333B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0672787A (en) | 1994-03-15 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP5030359B2 (en) | Production of hollow ceramic membranes by electrophoretic deposition. | |
| US5190834A (en) | Composite membrarnes and electrochemical cells containing them | |
| JP4662916B2 (en) | Method for producing metal molded body having ceramic layer, metal molded body and use thereof | |
| JPH09223508A (en) | High temperature fuel cell having thin film electrolyte | |
| JPH04332474A (en) | Method for forming an electronically conductive composite layer on a device substrate containing a solid electrolyte | |
| JPH0467564A (en) | Solid electrolytic fuel cell and porous electrode body using the same | |
| US20070180689A1 (en) | Nonazeotropic terpineol-based spray suspensions for the deposition of electrolytes and electrodes and electrochemical cells including the same | |
| KR20130092368A (en) | Fabrication method of tubular solid oxide fuel cell by electrostatic slurry deposition | |
| JPH03261677A (en) | Ceramic green sheet material, electrochemical element and production thereof | |
| JP2002313350A (en) | Porous and gas-permeable layer substructure for thin airtight layer,used as functional component in high temperature fuel cell | |
| JP3166333B2 (en) | Ceramic coating method | |
| US20020127344A1 (en) | Method for making thick and/or thin film | |
| JP3347561B2 (en) | Solid oxide fuel cell | |
| JP2011510432A (en) | Current collector structure | |
| JP3525601B2 (en) | Method for forming dense ceramic thin film | |
| JPH01274815A (en) | Production of ceramics filter | |
| JP4811776B2 (en) | SOLID ELECTROLYTE FUEL CELL FUEL ELECTRODE AND METHOD FOR PRODUCING THE SAME | |
| JPH0456070A (en) | Manufacture of solid electrolytic fuel battery tube cell | |
| JPH09129250A (en) | Solid oxide fuel cell | |
| JPH07320757A (en) | Solid electrolytic fuel cell interconnector, and its manufacture | |
| JP2001297781A (en) | Film forming method | |
| JPH06283179A (en) | Method for producing electrolyte membrane of solid oxide fuel cell | |
| JP2000024579A (en) | Film forming method by dipping | |
| JPH0714594A (en) | Method for integrally forming electrode and electrolyte membrane of solid oxide fuel cell | |
| US7195794B2 (en) | Method of making an electrolytic cell |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20010206 |
|
| LAPS | Cancellation because of no payment of annual fees |