[go: up one dir, main page]

JPH03203166A - Manufacture of solid electrolyte membrane - Google Patents

Manufacture of solid electrolyte membrane

Info

Publication number
JPH03203166A
JPH03203166A JP1342645A JP34264589A JPH03203166A JP H03203166 A JPH03203166 A JP H03203166A JP 1342645 A JP1342645 A JP 1342645A JP 34264589 A JP34264589 A JP 34264589A JP H03203166 A JPH03203166 A JP H03203166A
Authority
JP
Japan
Prior art keywords
solid electrolyte
electrolyte membrane
membrane
ysz
porous
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.)
Pending
Application number
JP1342645A
Other languages
Japanese (ja)
Inventor
Koichi Tachibana
立花 弘一
Yoshinori Toyoguchi
豊口 吉徳
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP1342645A priority Critical patent/JPH03203166A/en
Publication of JPH03203166A publication Critical patent/JPH03203166A/en
Pending 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
    • 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

  • Conductive Materials (AREA)
  • Fuel Cell (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 産業上の利用分野 本発明法 固体電解質型燃料電池 固体電解質型酸素セ
ンサ、酸素ポンプなどの電気化学デバイスに用いる固体
電解質膜の作製方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Industrial Field of Application Method of the Invention Solid Electrolyte Fuel Cell The present invention relates to a method for producing a solid electrolyte membrane used in electrochemical devices such as solid electrolyte oxygen sensors and oxygen pumps.

従来の技術 従来のこの種の電気化学デバイスにおいてit固体電解
質としてysz <イツトリア安定化ジルコニア)が多
用されてい凡 そして例えば高温固体電解質型燃料電池
において(友 固体電解質膜の作製に(よ 製膜速度が
大きいという利点がある溶射法等が一般に用いられてい
も 発明が解決しようとする課題 しかしながら上記方法でζよ 例えば溶射法は製膜速度
が大きく量産向きではあるが、固体電解質膜が多孔質状
態になりやすく、電気化学デバイスとして用いる場合に
 ガスリークの原因となって十分な特性が得られなかっ
たり、膜厚が薄い場合には電極の短絡の原因となったり
することが多かっ九 まな 固体電解質膜を高温で焼結
させることによりある程度緻密化させることは可能であ
るバ 電極材料が酸化物であると固体電解質と反応して
不活性な物質を固体電解質と電極の界面に形成したり、
白金電極などの場合には焼結が過度になって表面積が著
しく減少するなどの不都合が生じるために適した方法と
は言えな鶏 課題を解決するための手段 本発明において(戴 あらかじめ固体電解質微粒子を均
一に分散させて調製した溶液を、多孔質の固体電解質膜
に含浸させて焼成することにより膜を緻密化させるもの
である。
Conventional technology In conventional electrochemical devices of this type, ysz <yttria-stabilized zirconia) is commonly used as a solid electrolyte. For example, thermal spraying has a large film forming speed and is suitable for mass production; When used as an electrochemical device, it often causes gas leaks and insufficient properties, or if the film is thin, it often causes electrode short circuits.9 Mana Solid Electrolyte Membrane If the electrode material is an oxide, it may react with the solid electrolyte to form an inert substance at the interface between the solid electrolyte and the electrode.
In the case of platinum electrodes, this method cannot be said to be suitable because it causes problems such as excessive sintering and a significant decrease in surface area. A porous solid electrolyte membrane is impregnated with a solution prepared by uniformly dispersing it and fired, thereby making the membrane dense.

作用 本発明(よ 従来法により作製した固体電解質膜を簡単
な方法で緻密化でき、 しかし 電極との反応や電極面
積の減少などの不都合を生じることがなく、信頼度の高
い電気化学デバイスを得ることができるものであも 実施例 第1図!よ 本発明になる固体電解質膜の断面構造を示
す模式図であり、固体電解質微粉末分散溶液を含浸し乾
燥させた後の状態を示すものであもlはあらかじめNi
/YSZ系電極3を形電極3カルシア安定化ジルコニア
からなる多孔質基体4上に粒径的23umのYSZ (
8mo 1%Y20□〉粉末をプラズマ溶射により付着
させて形成した骨格となる多孔質固体電解質11L2は
粒径的0.1μmのYSZ (同)微粒子を分散(30
wt%)させた水溶液を減圧含浸することにより骨格と
なる多孔質固体電解質膜の気孔内部等に付着したYSZ
の微粒子であも 第2図は このようにして形成した固体電解質膜上にさ
らに(L a S r) −Mn Os系電極5を形成
した後、全体を1300℃で焼成した後の断面構造を示
していも 焼成後、YSZの微粒子が多孔質溶射膜の気
孔内部で焼結して気孔を埋めている様子(2′)を模式
的に示していも このようにして作製した固体電解質膜を以下のようにし
て評価しtラ  先ずYSZ微粒子の含浸処理の効果を
定量的に把握するために固体電解質膜の気孔率を求め1
.  含浸処理をせずに1300℃で焼成した場合の多
孔質固体電解質膜の気孔率は約23%であった(焼成し
ていなくてもこの値にあまり変化はない)。これに対し
て、含浸処理を行な1.%  かつ1300℃で焼成す
ると気孔率は約2%にまで減少し?、YSZ粒子が十分
小さいために このような低温においても焼結が進行し
半溶融状態になったYSZによって多孔質溶射膜の気孔
の大部分が充填されたものと考えられる。
Effects of the present invention A solid electrolyte membrane prepared by a conventional method can be densified by a simple method, but a highly reliable electrochemical device can be obtained without causing disadvantages such as reaction with electrodes or reduction in electrode area. Embodiment Figure 1 is a schematic diagram showing the cross-sectional structure of the solid electrolyte membrane according to the present invention, and shows the state after being impregnated with a solid electrolyte fine powder dispersion solution and dried. Amo l is Ni in advance
/YSZ-based electrode 3 is formed on a porous substrate 4 made of calcia-stabilized zirconia.
The porous solid electrolyte 11L2, which forms the framework by attaching 8mo 1% Y20□> powder by plasma spraying, is made by dispersing YSZ fine particles (30
YSZ adhered to the inside of the pores of the porous solid electrolyte membrane, which becomes the framework, by impregnating the aqueous solution (wt%) under reduced pressure.
Even with the fine particles of The solid electrolyte membrane prepared in this manner is shown below as a schematic diagram showing how the YSZ particles sinter and fill the pores of the porous sprayed membrane after firing (2'). First, in order to quantitatively understand the effect of impregnation treatment with YSZ fine particles, the porosity of the solid electrolyte membrane was determined.
.. The porosity of the porous solid electrolyte membrane when fired at 1300° C. without impregnation treatment was approximately 23% (this value does not change much even without firing). For this, impregnation treatment is performed.1. % and when fired at 1300℃, the porosity decreases to about 2%. It is thought that because the YSZ particles were sufficiently small, sintering progressed even at such a low temperature, and most of the pores in the porous sprayed film were filled with semi-molten YSZ.

−力、含浸処理をせずに気孔率を2%にするためには約
1600℃の焼成温度を必要とした力曳焼成後の固体電
解質と(LaSr)MnOs系電極の界面には5rZr
O*やLa*Z r*Qv等の高抵抗物質が生成してい
るのが認められた な抵 含浸のみを行い焼成を行わな
い場合でf1気孔率は約7%となり、微粒子の含浸のみ
でも膜の緻密化の効果が大きいことが明らかになり?、
YSZ微粒子の粒径をさらに小さくすることにより、含
浸の−みによる緻密化をさらに促進でき、これを焼成す
ることによって気孔率をほぼ0%にすることも可能であ
る。
- 5rZr was used at the interface between the solid electrolyte and (LaSr)MnOs-based electrode after force-pulling firing, which required a firing temperature of approximately 1600°C to achieve a porosity of 2% without mechanical impregnation.
It was observed that high-resistance substances such as O* and La*Zr*Qv were generated.If only impregnation was performed and no firing was performed, f1 porosity was approximately 7%, and even if only fine particles were impregnated, Did it become clear that the effect of densification of the membrane is large? ,
By further reducing the particle size of the YSZ fine particles, it is possible to further promote densification through impregnation, and by firing the particles, it is also possible to reduce the porosity to approximately 0%.

さらにまた 含浸処理は固体電解質膜の緻密化に寄与す
るだけでなく、YSZ微粒子が固体電解質と電極の接合
界面において脚材として作用する効果をもたらし 固体
電解質と電極の接合性を著しく高める効果も得られるこ
とがわかっtラ  この効果を実際に確認するたべ 前
記同様の含浸・焼成処理を行った積層体及び含浸帆1′
lをしていない積層体をそれぞれ空気+4=1.  R
T〜1000℃(300℃/hの昇降温)のヒートリー
rクル試験(連続30回)に供し 試験後積層体の断面
を観察することにより固体電解質と電極の剥離の有無な
どを解析した その結巣 含浸処理を行へ かつ130
0℃で焼成した試料の場合、固体電解質と電極の桜合界
面には何等の異常も認められなかつtうしかし 含浸処
理をしていない試料においては電極の一部に剥離が生じ
たり電極にマイクロクラックの発生が認められたりしt
も このように 微粒子含浸・焼成処理は固体電解質膜の緻
密化等に対して著しい効果を持つものであることがわか
る。
Furthermore, the impregnation treatment not only contributes to the densification of the solid electrolyte membrane, but also has the effect of the YSZ fine particles acting as a leg material at the bonding interface between the solid electrolyte and the electrode, and has the effect of significantly improving the bonding property between the solid electrolyte and the electrode. To actually confirm this effect, a laminate and impregnated sail 1' were subjected to the same impregnation and firing treatment as described above.
Air + 4 = 1. R
The laminate was subjected to a heat leak test (30 times in a row) at T ~ 1000℃ (temperature increase/decrease at 300℃/h), and the presence or absence of separation between the solid electrolyte and electrodes was analyzed by observing the cross section of the laminate after the test. Nest Go to impregnation treatment and 130
In the case of samples fired at 0°C, no abnormalities were observed at the bonding interface between the solid electrolyte and the electrodes. However, in the samples that were not impregnated, part of the electrodes peeled off or microscopic particles formed on the electrodes. Occasionally cracks were observed.
It can also be seen that the fine particle impregnation and calcination treatment has a remarkable effect on the densification of the solid electrolyte membrane.

以上の実施例で(L  固体電解質としてYSZ(イツ
トリア安定化ジルコニア)を用いた力交 これに限定す
るものではなLl  溶射に用いるYSZ粉末の粒径、
含浸用YSZ微粒子の粒径も適宜設定できる。含浸には
水溶液を用いた力文 粒子の分散状態を調整するために
添加剤を用いてもよく、溶媒も水辺外のものを用いるこ
とができ屯 含浸も多様な方法を用い得氏 焼成条件も
自由に設定可能である。ま瓢 固体電解質の多孔質膜に
はプラズマ溶射膜を用いた力文 他の方式の溶射で作製
した膜でもよく、さらにスラリーコーティング等他の方
法で作製した多孔質焦 あるいは多孔質焼結体にも同様
に適用できるものである。
In the above examples (L) Force exchange using YSZ (Ittria stabilized zirconia) as a solid electrolyte, but not limited to this, L) Particle size of YSZ powder used for thermal spraying,
The particle size of the YSZ fine particles for impregnation can also be set appropriately. For impregnation, an aqueous solution is used. Additives may be used to adjust the dispersion state of the particles, and solvents that are not available near water can be used. Impregnation can also be done using a variety of methods. Can be set freely. The porous membrane of the solid electrolyte may be a plasma-sprayed membrane, or it may be a membrane made by other methods of thermal spraying, and it may also be a porous sintered body or a porous sintered body made by other methods such as slurry coating. is also applicable in the same way.

発明の効果 本発明により、簡単な方法により多孔質固体電解質膜の
緻密化を行うことができ、信頼度の高い電気化学デバイ
スを得ることができも
Effects of the Invention According to the present invention, a porous solid electrolyte membrane can be densified by a simple method, and a highly reliable electrochemical device can be obtained.

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

第1図は本発明の一実施例の作製方法を用いた緻密膜作
製の過程を示す断面は 第2図は作製された緻密膜の断
面図である。 l・・固体電解質粒子(多孔質膜骨格)、 2・・固体
電解質微粒子(含浸材)、 2′・・焼結微粒子息3・
・重態 4・・基体 5・・電極
FIG. 1 is a cross-sectional view showing the process of producing a dense film using a production method according to an embodiment of the present invention. FIG. 2 is a cross-sectional view of the produced dense film. l...Solid electrolyte particles (porous membrane skeleton), 2...Solid electrolyte fine particles (impregnating material), 2'...Sintered fine particles 3.
・Severe condition 4..Substrate 5..Electrode

Claims (1)

【特許請求の範囲】[Claims] 多孔質状態の固体電解質膜にあらかじめ固体電解質微粒
子を均一に分散させて調製した溶液を含浸し焼成して固
体電解質膜を緻密化させることを特徴とする固体電解質
膜の作製方法。
A method for producing a solid electrolyte membrane, which comprises impregnating a porous solid electrolyte membrane with a solution prepared by uniformly dispersing solid electrolyte fine particles in advance and baking the membrane to densify the solid electrolyte membrane.
JP1342645A 1989-12-28 1989-12-28 Manufacture of solid electrolyte membrane Pending JPH03203166A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1342645A JPH03203166A (en) 1989-12-28 1989-12-28 Manufacture of solid electrolyte membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1342645A JPH03203166A (en) 1989-12-28 1989-12-28 Manufacture of solid electrolyte membrane

Publications (1)

Publication Number Publication Date
JPH03203166A true JPH03203166A (en) 1991-09-04

Family

ID=18355383

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1342645A Pending JPH03203166A (en) 1989-12-28 1989-12-28 Manufacture of solid electrolyte membrane

Country Status (1)

Country Link
JP (1) JPH03203166A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997034333A1 (en) * 1996-03-11 1997-09-18 Forschungszentrum Jülich GmbH Coating of porous electrodes with thin electrolyte layers

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63128566A (en) * 1986-11-18 1988-06-01 Mitsubishi Heavy Ind Ltd Solid electrolyte fuel cell and its manufacturing method
JPH02220361A (en) * 1989-02-20 1990-09-03 Mitsubishi Heavy Ind Ltd Cylindrical solid electrolyte fuel cell

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63128566A (en) * 1986-11-18 1988-06-01 Mitsubishi Heavy Ind Ltd Solid electrolyte fuel cell and its manufacturing method
JPH02220361A (en) * 1989-02-20 1990-09-03 Mitsubishi Heavy Ind Ltd Cylindrical solid electrolyte fuel cell

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997034333A1 (en) * 1996-03-11 1997-09-18 Forschungszentrum Jülich GmbH Coating of porous electrodes with thin electrolyte layers

Similar Documents

Publication Publication Date Title
KR101183774B1 (en) Manufacturing method and current collector
US5629103A (en) High-temperature fuel cell with improved solid-electrolyte/electrode interface and method of producing the interface
WO1992010862A1 (en) Method for manufacturing solid-state electrolytic fuel cell
US5277995A (en) Electrode and method of interconnection sintering on an electrode of an electrochemical cell
JPH04215254A (en) Method for forming electrodes in solid oxide electrochemical cells
JP2000200614A (en) Electrode of solid oxide fuel cell and method of manufacturing the same
WO2006092912A1 (en) Solid oxide type fuel battery cell and process for producing the same
US5141825A (en) Method of making a cermet fuel electrode containing an inert additive
CN111505084B (en) Sensing element and preparation method thereof
JPH03203166A (en) Manufacture of solid electrolyte membrane
JP3643006B2 (en) Solid oxide fuel cell cell
JP2848551B2 (en) Method for producing electrolyte membrane for solid oxide fuel cell
JP2001118590A (en) High conductivity solid electrolyte film and method for manufacturing the same
JP2000012042A (en) Cermet electrode with increased active sites and method for manufacturing the cermet electrode
CN210982309U (en) Novel ceramic catalytic electrode, sensing element and oxygen sensor
US20060172166A1 (en) Solid-oxide fuel cell and method for producing the same
JPH06283178A (en) Manufacture of electrolytic film for solid electrolytic fuel cell
JP3050328B2 (en) Method for manufacturing solid electrolyte fuel cell
JPH0714594A (en) Method for integrally forming electrode and electrolyte membrane of solid oxide fuel cell
JP3050331B2 (en) Method for manufacturing solid electrolyte fuel cell
JPH0272558A (en) Manufacture of fuel cell electrode
JPH05198305A (en) Manufacture of solid electrolyte fuel cell
JPH04355058A (en) Solid electrolyte fuel cell and manufacture thereof
RU2432230C9 (en) Integrated coaxial tubes
JPH08133739A (en) Production of zirconia film