JPH07142072A - Formation of electrolyte film - Google Patents

Formation of electrolyte film

Info

Publication number
JPH07142072A
JPH07142072A JP5290757A JP29075793A JPH07142072A JP H07142072 A JPH07142072 A JP H07142072A JP 5290757 A JP5290757 A JP 5290757A JP 29075793 A JP29075793 A JP 29075793A JP H07142072 A JPH07142072 A JP H07142072A
Authority
JP
Japan
Prior art keywords
electrolyte
pipe
electrode support
support tube
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.)
Withdrawn
Application number
JP5290757A
Other languages
Japanese (ja)
Inventor
Junichi Kanzaki
潤一 神前
Osao Kudome
長生 久留
Katsumi Nagata
勝巳 永田
Koji Ikeda
浩二 池田
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP5290757A priority Critical patent/JPH07142072A/en
Publication of JPH07142072A publication Critical patent/JPH07142072A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/10Fuel cells with solid electrolytes
    • H01M8/12Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
    • H01M8/124Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte characterised by the process of manufacturing or by the material of the electrolyte
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/10Fuel cells with solid electrolytes
    • H01M8/12Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
    • H01M8/1231Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte with both reactants being gaseous or vaporised
    • 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
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Fuel Cell (AREA)

Abstract

PURPOSE:To make an electrolyte film highly dense, and reduce a process by baking the electrolyte film regularly after the process that an electrode support pipe is soaked in slurry of particles larger than the pare diameter and is pulled up and is baked temporarily is repeated several times. CONSTITUTION:After masking 12 is applied to a film formation unnecessary part of an electrode support pipe (fuel electrode pipe) 11, a plug 13 is put in an opening part on one end side of the pipe 11, and a suction pump 15 is installed in an opening part on the opposite side through a suction pipe 14, and the whole is installed on a vertically moving device 16. A vessel 18 housing slurry like electrolyte slurry 17 is arranged under the pipe 11, and the particle diameter of the electrolyte is larger than the pore diameter of the pipe 11. The suction pump 15 is actuated, and the pipe 11 is soaked in the slurry 17, and after an electrolyte film 19 is formed by sucking near electrolyte particles, the pipe 11 is pulled up, and is dried. After this is repeated ten times, it is baked temporarily. After the process is repeated, it is baked regularly, and the electrolyte film 19 is formed.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、電解質膜の形成方法
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for forming an electrolyte membrane.

【0002】[0002]

【従来の技術】従来、円筒焼結型固体電解質燃料電池に
おける電解質の成膜法は、図6(A)〜(C)に示すよ
うに行われている。まず、電極支持管(燃料極管)1の
電解質膜が不要な部分にマスキング2を施すとともに、
電解質スラリー(泥しょう状)3を用意する(図6
(A)参照)。なお、図6(A)において、符番4は電
極支持管1を上下動させる上下移動装置を示す。次に、
図6(B)のようにその電極支持管1を電解質スラリー
3に浸たした後、図6(C)のように電極支持管1を電
解質スラリー3から取り出し、この状態で約90℃で乾
燥させる。ここで、浸す工程と乾燥工程をディピングと
称する。ひきつづき、ディッピングを9回(合計10
回)行い、最後に本焼を行い、緻密な電解質膜5を得
る。
2. Description of the Related Art Conventionally, a method for forming an electrolyte in a cylindrical sintered solid oxide fuel cell has been carried out as shown in FIGS. First, masking 2 is applied to a portion of the electrode support tube (fuel electrode tube) 1 where the electrolyte membrane is unnecessary,
Prepare an electrolyte slurry (slurry) 3 (Fig. 6)
(See (A)). In FIG. 6 (A), reference numeral 4 indicates a vertical movement device for moving the electrode support tube 1 up and down. next,
After immersing the electrode support tube 1 in the electrolyte slurry 3 as shown in FIG. 6 (B), the electrode support tube 1 is taken out of the electrolyte slurry 3 as shown in FIG. 6 (C) and dried at about 90 ° C. in this state. Let Here, the dipping process and the drying process are called dipping. Continue to dip 9 times (total 10
Times), and finally firing is performed to obtain a dense electrolyte membrane 5.

【0003】[0003]

【発明が解決しようとする課題】ところで、固体電解質
燃料電池の電解質に要求する性質として、薄膜化と緻密
化がある。ここで、従来の電解質の成膜法(工程順を下
記(1) 〜(5) に示す)では、比較的緻密でかつ薄い膜が
得られているが、得られる膜にバラツキがある。従っ
て、固体電解質燃料電池の性能のバラツキがあり、ひい
ては性能の低下となる。また、従来の電解質の成膜法で
は、ディッピングと仮焼が5回もあり、工程的に律速と
なっている。
By the way, as the properties required for the electrolyte of the solid oxide fuel cell, there are thinning and densification. Here, in the conventional electrolyte film forming method (the order of steps is shown in (1) to (5) below), a relatively dense and thin film is obtained, but the obtained film has variations. Therefore, there are variations in the performance of the solid oxide fuel cell, which in turn results in a decrease in performance. Further, in the conventional electrolyte film-forming method, dipping and calcination are performed 5 times, which is rate-limiting in terms of process.

【0004】(1) 電極支持管にマスキングする。 (2) 電極支持管を電解質スラリーに浸す。 (3) 電極支持管に付着した電解質粒子を乾燥させる。(1) Mask the electrode support tube. (2) Immerse the electrode support tube in the electrolyte slurry. (3) The electrolyte particles attached to the electrode support tube are dried.

【0005】(4) ディッピングが10回終了後、仮焼す
る。 (5) ディッピング10回につき、仮焼1回の工程が5回
終了した時点で、最後にこの電解質膜を本焼して膜を得
る。 なお、上記(2) から(3) の工程を総じてディッピングと
する。
(4) After 10 times of dipping, calcination is performed. (5) When the process of one calcination is completed 5 times for every 10 dippings, the electrolyte membrane is finally calcined to obtain a membrane. The steps (2) to (3) above are collectively called dipping.

【0006】この発明はこうした事情を考慮してなされ
たもので、緻密でしかもバラツキも少なく固体電解質燃
料電池の性能を向上させるとともに、工程数も削減しえ
る電解質膜の形成方法を提供することを目的とする。
The present invention has been made in view of these circumstances, and it is an object of the present invention to provide a method of forming an electrolyte membrane which is dense and has little variation and which improves the performance of a solid electrolyte fuel cell and can reduce the number of steps. To aim.

【0007】[0007]

【課題を解決するための手段】この発明は、円筒型の電
極支持管内を密閉するとともに、前記電極支持管の一端
側より該電極支持管内の空気を吸引可能にした後、前記
電極支持管を該電極支持管の気孔径より大きい粒子の電
解質スラリー中に浸漬し、その後電極支持管を引き上げ
て乾燥を数回繰り返すことにより電解質を仮焼し、更に
前記浸漬工程と仮焼工程を数回繰り返した後に本焼する
ことを特徴とする電解質膜の形成方法に関する。
According to the present invention, the inside of a cylindrical electrode support tube is hermetically sealed, and air inside the electrode support tube can be sucked from one end side of the electrode support tube. The electrolyte is calcinated by immersing it in an electrolyte slurry of particles having a pore size larger than that of the electrode support tube, then pulling up the electrode support tube and repeating drying several times to calcine the electrolyte, and further repeating the dipping step and calcination step several times. The present invention relates to a method for forming an electrolyte membrane, which is characterized by performing firing after firing.

【0008】[0008]

【作用】図2は本発明方法の要部を示す説明図であり、
図3は図2の要部の拡大図である。図において、図中の
符番21は電解質粒子を、符番22は電極支持管を、符番2
3は吸引ポンプを示す。本発明方法で電解質膜を成膜す
ると、図2,図3に示すように、吸引ポンプ23の泥し
ょう状の電解質スラリーが電解質粒子が良好に電極支持
管に付着する。その後、仮焼して同様な工程を繰り返す
と、前回の仮焼で電解質が緻密でない場合でも、吸引力
によりその緻密でない部分を塞ぐことが可能となり、緻
密な電解質膜を得ることができる。また、この吸引力は
吸引ポンプによって操作することが可能であれば、膜厚
も調整することができると考えらる。一方、従来方法に
よれば、図6に示すように電極支持管22の方面にある程
度の電解質粒子21は付着するが、本発明方法にような吸
引ポンプによる効果がないため、十分な電解質粒子21の
付着がない。
FIG. 2 is an explanatory view showing an essential part of the method of the present invention.
FIG. 3 is an enlarged view of the main part of FIG. In the figure, reference numeral 21 in the figure is an electrolyte particle, reference numeral 22 is an electrode support tube, reference numeral 2
Reference numeral 3 represents a suction pump. When the electrolyte membrane is formed by the method of the present invention, as shown in FIGS. 2 and 3, the slurry-like electrolyte slurry of the suction pump 23 has the electrolyte particles favorably attached to the electrode support tube. After that, if calcination is performed and the same steps are repeated, even if the electrolyte is not dense in the previous calcination, it is possible to close the non-dense portion by the suction force, and a dense electrolyte membrane can be obtained. Further, it is considered that the film thickness can be adjusted if the suction force can be operated by a suction pump. On the other hand, according to the conventional method, as shown in FIG. 6, a certain amount of the electrolyte particles 21 are attached to the surface of the electrode support tube 22, but since the effect of the suction pump as in the method of the present invention is not exerted, sufficient electrolyte particles 21 are not formed. There is no sticking.

【0009】[0009]

【実施例】以下、この発明の一実施例を図1(A)〜
(C)を参照して説明する。 (1) まず、円筒の電極支持管(燃料極管)11上の成膜不
要な部分にマスキング12を施した後、電極支持管11の一
端側の開放部に栓13をし、その反対側の開放部に吸引管
14を介して吸引ポンプ15を取り付け、全体を上下移動装
置16に取り付ける。この時、電極支持管11は複数本を同
時に準備し、上下移動装置16に取り付けることにより生
産性の向上が図れる。また、これとは別に、電極支持管
11の下方には、泥しょう状の電解質スラリー17を収容し
た容器18を配置する(図1(A)参照)。ここで、電解
質スラリー17中の電解質の粒子径は、電極支持管11の気
孔径よりも大きい粒子を用いる。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT An embodiment of the present invention will be described below with reference to FIGS.
This will be described with reference to (C). (1) First, after masking 12 on the cylindrical electrode support tube (fuel electrode tube) 11 where film formation is not required, plug 13 on the open end of the electrode support tube 11 on the opposite side. Suction tube at the open part of
The suction pump 15 is attached via 14 and the whole is attached to the vertical movement device 16. At this time, by preparing a plurality of electrode support tubes 11 at the same time and attaching them to the vertical movement device 16, productivity can be improved. Separately from this, an electrode support tube
A container 18 containing a slurry-like electrolyte slurry 17 is arranged below 11 (see FIG. 1A). Here, the particle size of the electrolyte in the electrolyte slurry 17 is larger than the pore size of the electrode support tube 11.

【0010】(2) 次に、前記吸引ポンプ15を作動させ、
電極管支持管11内の空気を吸引しつつ、前記電極支持管
11を電解質スラリー17に浸し(図1(B)参照)、表面
に電解質粒子が吸いよせられ電解質膜19が形成された
ら、前記電極支持管11を電解質スラリー17から引き上げ
る。
(2) Next, the suction pump 15 is operated,
While sucking air in the electrode tube support tube 11, the electrode support tube
11 is dipped in the electrolyte slurry 17 (see FIG. 1B), and when the electrolyte particles are absorbed on the surface and the electrolyte membrane 19 is formed, the electrode support tube 11 is pulled out from the electrolyte slurry 17.

【0011】(3) つづいて、この状態で電極支持管11を
約90℃で乾燥させる。 (4) 次に、上記(2) 及び(3) の工程(ディピング;Dip
pingと称する)を10回繰返した後、仮焼を行う。
(3) Subsequently, in this state, the electrode support tube 11 is dried at about 90 ° C. (4) Next, the steps (2) and (3) above (dipping; Dip
(Ping) is repeated 10 times, and then calcination is performed.

【0012】(5) 次に、上記(2) ,(3) 及び(4) の工程
を数回繰り返して、電解質膜19を必要な厚みにする。 (6) 最後に、電極支持管11の全体を本焼し、電解質膜19
の成膜を完了し、固体電解質燃料電池を製造する(図1
(C)参照)。
(5) Next, the above steps (2), (3) and (4) are repeated several times to make the electrolyte membrane 19 have a required thickness. (6) Finally, the entire electrode support tube 11 is fired to form the electrolyte membrane 19
Film formation is completed, and a solid oxide fuel cell is manufactured (Fig. 1
(See (C)).

【0013】このように、上記実施例によれば、図2,
図3に示すように、吸引ポンプ23の泥しょう状の電解質
スラリー17が電解質粒子が良好に電極支持管11に付着す
る。その後、仮焼して同様な工程を繰り返すと、前回の
仮焼で電解質が緻密でない場合でも、吸引力によりその
緻密でない部分を塞ぐことが可能となり、緻密な電解質
膜19を得ることができる。また、この吸引力は吸引ポン
プ23によって操作することが可能であれば、膜厚も調整
することができる。
As described above, according to the above embodiment, as shown in FIG.
As shown in FIG. 3, the slurry-like electrolyte slurry 17 of the suction pump 23 has the electrolyte particles favorably attached to the electrode support tube 11. Then, by calcination and repeating the same steps, even if the electrolyte is not dense in the previous calcination, it is possible to close the non-dense portion by the suction force, and the dense electrolyte membrane 19 can be obtained. Further, if this suction force can be operated by the suction pump 23, the film thickness can be adjusted.

【0014】図4は、上記実施例による方法及び従来方
法から得た電解質膜のガス透過係数をディッピング後の
仮焼回数別に示す。図4において、曲線(イ)は本発明
方法を、曲線(ロ)は従来方法を示す。図4より、本発
明方法は従来方法よりガス透過係数が小さく、かなり緻
密であることが分かる。また、ディッピング後の仮焼回
数も従来方法より少ない回数で緻密な膜が得られてお
り、今回採用した吸引力が電解質の高緻密化及び工程削
減にかなり有効であることが示唆された。従って、今回
発明した方法で円筒焼結型電解質燃料電池の電解質を成
膜することで、従来のセルより高い性能(高開回路電圧
等)を示すことが多いに期待できる。
FIG. 4 shows the gas permeation coefficients of the electrolyte membranes obtained by the method according to the above-described embodiment and the conventional method, by the number of times of calcination after dipping. In FIG. 4, curve (a) shows the method of the present invention, and curve (b) shows the conventional method. It can be seen from FIG. 4 that the method of the present invention has a smaller gas permeation coefficient than the conventional method and is considerably dense. In addition, the number of times of calcination after dipping was smaller than that of the conventional method, and a dense film was obtained. It was suggested that the suction force adopted this time is quite effective for increasing the density of the electrolyte and reducing the number of steps. Therefore, by forming the film of the electrolyte of the cylindrical sintered electrolyte fuel cell by the method of the present invention, it can be expected that it often exhibits higher performance (high open circuit voltage etc.) than the conventional cell.

【0015】[0015]

【発明の効果】以上詳述したようにこの発明によれば、
緻密でしかもバラツキも少なく固体電解質燃料電池の性
能を向上させるとともに、工程数も削減しえる電解質膜
の形成方法を提供できる。
As described above in detail, according to the present invention,
It is possible to provide a method for forming an electrolyte membrane that is dense and has little variation and that can improve the performance of the solid electrolyte fuel cell and reduce the number of steps.

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

【図1】この発明の一実施例に係る固体電解質燃料電池
の固体電解質膜の成膜法を工程順に示す説明図。
FIG. 1 is an explanatory view showing a method of forming a solid electrolyte membrane of a solid electrolyte fuel cell according to an embodiment of the present invention in the order of steps.

【図2】本発明による電解質膜の形成方法のよる電解質
の付着概念図。
FIG. 2 is a conceptual diagram of attachment of an electrolyte according to the method for forming an electrolyte membrane according to the present invention.

【図3】本発明法及び従来法による電解質膜のガス透過
係数と仮焼回数の関係を示す特性図。
FIG. 3 is a characteristic diagram showing the relationship between the gas permeation coefficient and the number of times of calcination of the electrolyte membrane according to the present invention method and the conventional method.

【図4】図1の要部の詳細を示す回路構成図。FIG. 4 is a circuit configuration diagram showing details of a main part of FIG.

【図5】従来の固体電解質燃料電池の固体電解質膜の成
膜法を工程順に示す説明図。
FIG. 5 is an explanatory view showing a method of forming a solid electrolyte membrane of a conventional solid electrolyte fuel cell in the order of steps.

【図6】従来の電解質膜の成膜法による電解質の付着概
念図。
FIG. 6 is a conceptual diagram of attachment of an electrolyte by a conventional method of forming an electrolyte membrane.

【符号の説明】[Explanation of symbols]

11…電極支持管(燃料極管)、12…マスキング、
13…栓、14…吸引管、 15…吸引ポン
プ、 16…上下移動装置、17…電解質スラリー、
18…容器、 19…電解質膜、21…電解
質粒子。
11 ... Electrode support tube (fuel electrode tube), 12 ... Masking,
13 ... Plug, 14 ... Suction tube, 15 ... Suction pump, 16 ... Vertical movement device, 17 ... Electrolyte slurry,
18 ... Container, 19 ... Electrolyte membrane, 21 ... Electrolyte particles.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 池田 浩二 長崎県長崎市飽の浦町1番1号 三菱重工 業株式会社長崎造船所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Koji Ikeda 1-1 1-1 Atsunoura-machi, Nagasaki-shi, Nagasaki Mitsubishi Heavy Industries Ltd. Nagasaki Shipyard

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 円筒型の電極支持管内を密閉するととも
に、前記電極支持管の一端側より該電極支持管内の空気
を吸引可能にした後、前記電極支持管を該電極支持管の
気孔径より大きい粒子の電解質スラリー中に浸漬し、そ
の後電極支持管を引き上げて乾燥を数回繰り返すことに
より電解質を仮焼し、更に前記浸漬工程と仮焼工程を数
回繰り返した後に本焼することを特徴とする電解質膜の
形成方法。
1. A cylindrical electrode support tube is hermetically sealed, and air in the electrode support tube can be sucked from one end side of the electrode support tube, and then the electrode support tube is made smaller than the pore diameter of the electrode support tube. Characterized by immersing in an electrolyte slurry of large particles, then raising the electrode support tube and repeating drying several times to calcine the electrolyte, and further repeating the dipping step and calcining step several times and then performing main firing And a method for forming an electrolyte membrane.
JP5290757A 1993-11-19 1993-11-19 Formation of electrolyte film Withdrawn JPH07142072A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5290757A JPH07142072A (en) 1993-11-19 1993-11-19 Formation of electrolyte film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5290757A JPH07142072A (en) 1993-11-19 1993-11-19 Formation of electrolyte film

Publications (1)

Publication Number Publication Date
JPH07142072A true JPH07142072A (en) 1995-06-02

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JP5290757A Withdrawn JPH07142072A (en) 1993-11-19 1993-11-19 Formation of electrolyte film

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002019454A1 (en) * 2000-08-30 2002-03-07 Sanyo Electric Co., Ltd. Fuel cell unit and its manufacturing method
JP2007042356A (en) * 2005-08-02 2007-02-15 Mitsubishi Heavy Ind Ltd Method for manufacturing cell of fuel cell

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002019454A1 (en) * 2000-08-30 2002-03-07 Sanyo Electric Co., Ltd. Fuel cell unit and its manufacturing method
JP2007042356A (en) * 2005-08-02 2007-02-15 Mitsubishi Heavy Ind Ltd Method for manufacturing cell of fuel cell

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