JPH04114981A - Sintered multilayer composite ceramics and production thereof - Google Patents

Sintered multilayer composite ceramics and production thereof

Info

Publication number
JPH04114981A
JPH04114981A JP23159290A JP23159290A JPH04114981A JP H04114981 A JPH04114981 A JP H04114981A JP 23159290 A JP23159290 A JP 23159290A JP 23159290 A JP23159290 A JP 23159290A JP H04114981 A JPH04114981 A JP H04114981A
Authority
JP
Japan
Prior art keywords
layer
sintered body
porous
inorganic colloid
ceramic layer
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
JP23159290A
Other languages
Japanese (ja)
Inventor
Nobuyuki Asaoka
浅岡伸之
Kazunobu Ogawa
和伸 小川
Takeshi Sato
武 佐藤
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 Materials Corp
Original Assignee
Mitsubishi Materials Corp
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 Materials Corp filed Critical Mitsubishi Materials Corp
Priority to JP23159290A priority Critical patent/JPH04114981A/en
Publication of JPH04114981A publication Critical patent/JPH04114981A/en
Pending legal-status Critical Current

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  • Laminated Bodies (AREA)
  • Porous Artificial Stone Or Porous Ceramic Products (AREA)

Abstract

PURPOSE:To obtain the subject sintered material having improved mechanical strength without causing cracking, etc., by introducing inorganic colloid particles into open pores of a laminated and sintered material composed of a porous ceramic layer having open pores and a ceramic layer having dense texture and integrally sintering the layers. CONSTITUTION:A green sheet (A) for forming a dense layer is produced by drying a formed layer of a slurry for dense layer composed of (a) an inorganic colloid liquid containing water as dispersion medium, (b) a sintering assistant and (c) a water-soluble binder. Separately, a green sheet (B) for porous layer is produced by drying the formed layer of a slurry for porous layer composed of the component (a), the component (b) and the component (c), wherein the content of the component (b) is smaller than the content in the sheet A or the component (b) is absent in the sheet B. The green sheet A is bonded to one or both surfaces of the sheet B with an adhesive and the laminate is baked at 1000-1600 deg.C to obtain a sintered laminate of a porous ceramic layer and a dense ceramic layer. An inorganic colloid liquid (d) different from the component (a) is introduced into the porous ceramic layer of the sintered product, subjected to hydrothermal treatment and cooled to deposit the inorganic colloid particle (C) in the open pores of the porous ceramic layer. The product is baked again to obtain the objective sintered material.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明はグリーンシート多層積層法により製造される、
異種セラミック原料からなる多層セラミック複合焼結体
に関する。更に詳しくは触媒担体又はフィルタとして有
用な多層セラミック複合焼結体及びその製造方法に関す
るものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention is manufactured by a green sheet multilayer lamination method.
This invention relates to a multilayer ceramic composite sintered body made of different ceramic raw materials. More specifically, the present invention relates to a multilayer ceramic composite sintered body useful as a catalyst carrier or filter, and a method for manufacturing the same.

[従来の技術] 従来、異種セラミック原料からなる多層のセラミック複
合焼結体を製造する場合には、予め異種のセラミック成
形体を各別に製造し、次いでこれらの異種セラミック成
形体を熱プレス又はラミネート等により積層して複合一
体化した後、焼成して多層セラミック複合焼結体を得て
いる。
[Prior Art] Conventionally, when manufacturing a multilayered ceramic composite sintered body made of different types of ceramic raw materials, different types of ceramic molded bodies are manufactured separately, and then these different types of ceramic molded bodies are hot-pressed or laminated. After laminating them to form a composite body, they are fired to obtain a multilayer ceramic composite sintered body.

[発明が解決しようとする課題] しかし、セラミック成形体は原料が異なると、焼結温度
、熱膨張係数、焼成収縮等がそれぞれ異なり、積層状態
で焼成したときに焼結体の層間にクラック、反り、剥離
等の欠陥が生じ易い問題点があった。
[Problems to be Solved by the Invention] However, the sintering temperature, thermal expansion coefficient, firing shrinkage, etc. of ceramic molded bodies differ depending on the raw materials, and when fired in a laminated state, cracks may occur between the layers of the sintered body. There was a problem that defects such as warping and peeling were likely to occur.

本発明の目的は、積層状態で焼成したときに焼結体の層
間にクラック、反り、剥離等の欠陥を生じることなく、
しかも機械的強度が高い多層セラミック複合焼結体及び
その製造方法を提供することにある。
The purpose of the present invention is to prevent defects such as cracks, warping, and peeling between the layers of the sintered body when fired in a laminated state.
Moreover, it is an object of the present invention to provide a multilayer ceramic composite sintered body having high mechanical strength and a method for manufacturing the same.

[課題を解決するための手段] 」二記目的を達成するために、本発明の多層セラミック
複合焼結体は、多孔質セラミック層の両面又は片面に前
記多孔質セラミック層と同種のセラミック原料からなる
緻密質セラミック層が積層されて一体的に焼結され、前
記多孔質セラミック層に開気孔が形成された積層焼結体
を支持体とする多層セラミック焼結体であって、前記セ
ラミック層と異種のセラミック原料からなる無機コロイ
ド粒子が前記開気孔に導入されかつ前記多孔質セラミッ
ク層と一体的に焼結されたことを特徴とする。
[Means for Solving the Problems] In order to achieve the second object, the multilayer ceramic composite sintered body of the present invention has a porous ceramic layer made of the same type of ceramic raw material as the porous ceramic layer on both or one side of the porous ceramic layer. A multilayer ceramic sintered body is a multilayered ceramic sintered body in which dense ceramic layers are laminated and integrally sintered, and the porous ceramic layer has open pores formed therein as a support. It is characterized in that inorganic colloidal particles made of different types of ceramic raw materials are introduced into the open pores and sintered integrally with the porous ceramic layer.

また本発明の多層セラミック複合焼結体の製造方法では
、先ず水を分散媒とした第1無機コロイド液に第1焼結
助剤と第1水溶性バインダを添加混合して緻密質層用ス
ラリーを調製し、この緻密質層用スラリーを成膜乾燥し
て緻密質層用グリーンシートを成形する。次いで水を分
散媒とし、前記第1無機コロイド液と同種の第2無機コ
ロイド液に焼結助剤を添加しないか又は前記第1焼結助
を 剤より少量の第2焼結助剤と第2水溶性バインダを添加
混合して多孔質層用スラリーを調製し、この多孔質層用
スラリーを成膜乾燥して多孔質層用グリーンシートを成
形する。次に前記多孔質層用グリーンシートの両面又は
片面に前記緻密質層用グリーンシートを接着剤により接
着し、前記接着したグリーン成形体を1000〜160
0℃で焼成して積層焼結体を形成する。続いて水を分散
媒とし、前記第1及び第2無機コロイド液と異種の第3
無機コロイド液を前記積層焼結体の多孔質セラミック層
に導入し、前記第3無機コロイド液を水熱処理した後、
冷却して前記多孔質セラミック層の開気孔に無機コロイ
ド粒子を析出させる。更に前記無機コロイド粒子の析出
した積層焼結体を再度焼成する。
In addition, in the method for manufacturing a multilayer ceramic composite sintered body of the present invention, first, a first sintering aid and a first water-soluble binder are added and mixed to a first inorganic colloid liquid using water as a dispersion medium to form a slurry for a dense layer. This slurry for dense layer is formed into a film and dried to form a green sheet for dense layer. Next, water is used as a dispersion medium, and a second inorganic colloid liquid of the same type as the first inorganic colloid liquid is mixed with no sintering aid or a second sintering aid in a smaller amount than the first sintering aid. 2 A water-soluble binder is added and mixed to prepare a slurry for a porous layer, and this slurry for a porous layer is formed into a film and dried to form a green sheet for a porous layer. Next, the dense layer green sheet is adhered to both sides or one side of the porous layer green sheet with an adhesive, and the adhered green molded body is
A laminated sintered body is formed by firing at 0°C. Next, using water as a dispersion medium, a third inorganic colloid liquid different from the first and second inorganic colloid liquids is added.
After introducing an inorganic colloid liquid into the porous ceramic layer of the laminated sintered body and hydrothermally treating the third inorganic colloid liquid,
By cooling, inorganic colloid particles are precipitated in the open pores of the porous ceramic layer. Furthermore, the laminated sintered body in which the inorganic colloid particles have been precipitated is fired again.

緻密質層用スラリーの主成分である第1無機コロイド液
、多孔質層用スラリーの主成分である第2無機コロイド
液、及び多孔質セラミック層に導入する第8無機コロイ
ド液は、ともに金属アルコキシドを加水分解し、その加
水分解生成物を解膠処理して得られる粒径が数10〜1
000人の微細なコロイド粒子の無機コロイド液が好ま
しい。
The first inorganic colloid liquid, which is the main component of the slurry for the dense layer, the second inorganic colloid liquid, which is the main component of the slurry for the porous layer, and the eighth inorganic colloid liquid, which is introduced into the porous ceramic layer, are all metal alkoxides. The particle size obtained by hydrolyzing and peptizing the hydrolyzed product is several 10 to 1.
Inorganic colloidal liquids with 0,000 microscopic colloidal particles are preferred.

上記無機コロイド液としては、アルミナゾル、シリカゾ
ル、TiO□ゾル、ZrO□ゾル等が挙げられる。
Examples of the inorganic colloid liquid include alumina sol, silica sol, TiO□ sol, ZrO□ sol, and the like.

緻密質層用スラリーと多孔質層用スラリーの調製方法の
相違点は、前者に焼結助剤が無機コロイド液100重量
%に対して0.5〜10重量%含まれるのに対して、後
者にはセラミック層の気孔率を増大させるために焼結助
剤が全く含まれないか或いは前者より少量の焼結助剤が
含まれるところにある。この焼結助剤としては、二酸化
けい素、酸化マグネシウム、酸化カルシウム、酢酸マグ
ネシウム、二酸化チタン等が挙げられる。酸化マグネシ
ウム及び二酸化けい素の添加系では酸化カルシウムを少
なくとも0.1重量%添加することが好ましい。
The difference between the preparation methods of the slurry for dense layers and the slurry for porous layers is that the former contains 0.5 to 10% by weight of the sintering aid based on 100% by weight of the inorganic colloid liquid, while the latter In order to increase the porosity of the ceramic layer, either no sintering aid is included or a smaller amount of sintering aid is included. Examples of the sintering aid include silicon dioxide, magnesium oxide, calcium oxide, magnesium acetate, and titanium dioxide. In the addition system of magnesium oxide and silicon dioxide, it is preferable to add at least 0.1% by weight of calcium oxide.

水溶性バインダは緻密質層用スラリー及び多孔質層用ス
ラリーにおいて、ともに無機コロイド液の固形分に対し
て10〜80重量%添加される。
The water-soluble binder is added in an amount of 10 to 80% by weight based on the solid content of the inorganic colloid liquid in both the dense layer slurry and the porous layer slurry.

このバインダは焼結時の脱バインダによりセラミック層
に気孔を生じ易いため、気孔率を減少させる場合には上
記範囲で少なめに無機コロイド液に添加される。水溶性
バインダとしてはポリビニルアルコール、水溶性アクリ
ル等が挙げられる。緻密質層用スラリーに含まれるバイ
ンダは多孔質層用スラリーに含まれるバインダと異なっ
てもよい。
Since this binder tends to generate pores in the ceramic layer due to removal of the binder during sintering, in order to reduce the porosity, it is added to the inorganic colloid liquid in a small amount within the above range. Examples of water-soluble binders include polyvinyl alcohol and water-soluble acrylic. The binder contained in the slurry for the dense layer may be different from the binder contained in the slurry for the porous layer.

緻密質層用スラリー及び多孔質層用スラリーを成膜する
方法としては、ドクターブレード法、押出し成形法、ロ
ール圧延法、泥しよう鋳込み法等があるが、成形歪が少
なく成形体の平滑度が良好なドクターブレード法が好ま
しい。多孔質層用スラリーを成膜するときに、このスラ
リーにアンモニア、或いはアミン類のアルカリ物質を添
加してスラリー中にゲルを生成させ、気孔率を増大させ
ることもできる。
Methods for forming dense layer slurry and porous layer slurry include the doctor blade method, extrusion molding method, roll rolling method, and slurry casting method, but these methods have low molding distortion and smoothness of the molded product. A good doctor blade method is preferred. When forming a slurry for a porous layer, ammonia or an alkaline substance such as amines may be added to the slurry to form a gel in the slurry, thereby increasing the porosity.

緻密質層用のスラリー及び多孔質層用のスラリーを成膜
後、30〜95℃でそれぞれ乾燥して緻密質層用グリー
ンシート及び多孔質層用グリーンシートを成形する。緻
密質層用グリーンシートには後述する多孔質セラミック
層への無機コロイド液の導入を容易にするために孔径6
0〜100μmの通孔を設けてもよい。
After forming the slurry for the dense layer and the slurry for the porous layer, they are dried at 30 to 95°C, respectively, to form a green sheet for the dense layer and a green sheet for the porous layer. The green sheet for the dense layer has pores with a diameter of 6 to facilitate the introduction of the inorganic colloid liquid into the porous ceramic layer, which will be described later.
A through hole of 0 to 100 μm may be provided.

次いで多孔質層用グリーンシートの両面又は片面に接着
剤を塗布し、0〜70℃の温度で5〜200 kg/c
m2の圧力で多孔質層用グリーンシートと緻密質層用グ
リーンシートを接着し積層する。
Next, an adhesive is applied to both sides or one side of the green sheet for the porous layer, and the adhesive is applied at a temperature of 0 to 70°C at a rate of 5 to 200 kg/c.
The green sheet for the porous layer and the green sheet for the dense layer are adhered and laminated under a pressure of m2.

必要に応じて巻取り機構付きのラミネート装置により両
グリーンシートを互いに接着しながら巻取っテモよい。
If necessary, both green sheets can be rolled up while being adhered to each other using a laminating device with a winding mechanism.

この接着剤としては、セルロース誘導体、アクリル系エ
マルジョン、酢酸ビニルエマルジョン等の水系接着剤又
はアクリル系樹脂、ブチラール系樹脂、ビニール系樹脂
等の非水系接着剤を用いることができる。
As this adhesive, an aqueous adhesive such as a cellulose derivative, an acrylic emulsion, or a vinyl acetate emulsion, or a non-aqueous adhesive such as an acrylic resin, a butyral resin, or a vinyl resin can be used.

これらの積層数は1枚の多孔質層用グリーンシートの片
面に1枚の緻密質層用グリーンシートを重ね合わせて積
層する2層以外に、複合焼結体の用途、サイズ等に応じ
て緻密質層と多孔質層とを交互に重ね合わせた3層以上
にすることもてきる。
In addition to the two layers in which one green sheet for a dense layer is laminated on one side of one green sheet for a porous layer, the number of laminated layers varies depending on the use, size, etc. of the composite sintered body. It is also possible to have three or more layers in which a solid layer and a porous layer are alternately stacked.

グリーンシートを積層した後、所定の寸法に切断し、焼
成炉に入れて焼成する。巻取られて円柱状に成形された
グリーン成形体は所定の長さに切断され、巻取り芯を抜
いてできた中心孔の部分に緻密質層用のスラリーを充填
し、30〜95℃でこのスラリーを乾燥した後、焼成炉
に入れて焼成する。
After the green sheets are laminated, they are cut into predetermined dimensions, placed in a firing furnace, and fired. The green compact that was wound up and formed into a cylindrical shape was cut into a predetermined length, the central hole created by removing the winding core was filled with a slurry for a dense layer, and the material was heated at 30 to 95°C. After drying this slurry, it is placed in a kiln and fired.

焼成は目的とする気孔率を得るために1000〜160
0℃の温度範囲で、1〜2時間、大気圧下で行われる。
Firing is performed at a temperature of 1000 to 160 to obtain the desired porosity.
It is carried out at a temperature range of 0° C. for 1 to 2 hours under atmospheric pressure.

焼成温度が高まる程、また焼成時間が長くなる程、気孔
率は減少する。1000℃未満であると緻密質セラミッ
ク層の気孔率が増大し、1600℃を越えると多孔質セ
ラミック層の気孔率が減少して本発明の目的が達成され
ない。
The higher the firing temperature and the longer the firing time, the lower the porosity. If the temperature is less than 1,000°C, the porosity of the dense ceramic layer increases, and if it exceeds 1,600°C, the porosity of the porous ceramic layer decreases, making it impossible to achieve the object of the present invention.

本発明の多層セラミック複合焼結体は焼結助剤の添加量
又は焼成温度に応じて、多孔質セラミック層の気孔率が
20〜60%の範囲に、また緻密質セラミック層の気孔
率が0.01〜5%の範囲に制御されて作られる。
In the multilayer ceramic composite sintered body of the present invention, the porosity of the porous ceramic layer is in the range of 20 to 60%, and the porosity of the dense ceramic layer is 0%, depending on the amount of sintering aid added or the firing temperature. The content is controlled within the range of .01 to 5%.

上記焼成で得られた積層焼結体の多孔質セラミック層に
は開気孔が形成される。ここで開気孔とは閉気孔とは異
なり、焼結体の一端から他端まで連続した空隙であって
流体が通過可能な微細な孔をいう。
Open pores are formed in the porous ceramic layer of the laminated sintered body obtained by the above firing. Here, open pores are different from closed pores and refer to fine pores that are continuous from one end of the sintered body to the other and allow fluid to pass through.

次に積層焼結体を支持体として、この多孔質セラミック
層に水を分散媒とする第3無機コロイド液を導入する。
Next, using the laminated sintered body as a support, a third inorganic colloid liquid containing water as a dispersion medium is introduced into the porous ceramic layer.

この導入方法には次の2つの方法が代表的である。即ち
、第1の導入方法は、金属アルコキシドを加水分解し、
この加水分解生成物を解膠処理して得られる無機コロイ
ド液を容器に入れた後に、この液中に前記積層焼結体を
浸漬して無機コロイド液を多孔質セラミック層に導入す
る方法である。
The following two methods are typical for this introduction method. That is, the first introduction method is to hydrolyze a metal alkoxide,
In this method, an inorganic colloid liquid obtained by peptizing this hydrolyzed product is placed in a container, and then the laminated sintered body is immersed in this liquid to introduce the inorganic colloid liquid into the porous ceramic layer. .

また第2の導入方法は、前記積層焼結体を容器内の水に
浸漬し、次いで金属アルコキシドを入れこの水により金
属アルコキシドを加水分解した後、加水分解生成物を解
膠処理して無機コロイド液を多孔質セラミック層に導入
する方法である。
The second introduction method is to immerse the laminated sintered body in water in a container, then add metal alkoxide, hydrolyze the metal alkoxide with this water, and then peptize the hydrolysis product to form an inorganic colloid. This method involves introducing a liquid into a porous ceramic layer.

上記方法により積層焼結体の多孔質セラミック層の開気
孔に粒径が数10〜1000への微細な無機コロイド粒
子が導入される。このコロイド粒径を調整することによ
り、開気孔を所望の細孔径とすることができる。コロイ
ド粒径の調整方法としては、例えば解膠処理した無機コ
ロイド液を水熱処理する方法が挙げられる。この水熱処
理前にコロイド液に更にカルボン酸を添加しておくと、
より一層容易に粒径を調整することができる。水熱処理
後、冷却することにより開気孔に無機コロイド粒子が析
出する。無機コロイド粒子としては、アルミナ(A交2
03)、二酸化チタン(T102) 、ジルコニア(Z
rO2)、酸化マグネシウム(Mg0)、チタン酸バリ
ウム(BaTi0s)等が挙げられる。
By the above method, fine inorganic colloid particles having a particle size of several tens to a thousand are introduced into the open pores of the porous ceramic layer of the laminated sintered body. By adjusting the colloid particle size, the open pores can have a desired pore size. A method for adjusting the colloid particle size includes, for example, a method of hydrothermally treating a peptized inorganic colloid liquid. If carboxylic acid is further added to the colloidal liquid before this hydrothermal treatment,
Particle size can be adjusted even more easily. After the hydrothermal treatment, inorganic colloid particles are precipitated in the open pores by cooling. As the inorganic colloid particles, alumina (A
03), titanium dioxide (T102), zirconia (Z
rO2), magnesium oxide (Mg0), barium titanate (BaTi0s), and the like.

析出した無機コロイド粒子はその粒径に応じて多孔質セ
ラミック層の開気孔の細孔径を小さくする。オートクレ
ーブ内で無機コロイド液の水熱処理及び冷却処理を行う
と、コロイド粒子の粒成長及び析出の速度を速めること
ができ好ましい。
The precipitated inorganic colloid particles reduce the pore size of the open pores of the porous ceramic layer according to their particle size. Hydrothermal treatment and cooling treatment of the inorganic colloidal liquid in an autoclave is preferred because it can speed up the growth and precipitation of colloidal particles.

積層焼結体を容器から取出して無機コロイド液の水分を
脱離する。この水分の脱離は大気圧下又は減圧下、積層
焼結体を風乾又は温風乾燥することにより行う。乾燥に
よりコロイド液がゲル化しこの状態で積層焼結体を再度
900〜1300 ’C13〜5時間、大気圧下で焼成
する。この結果、開気孔に析出された無機コロイド粒子
が積層焼結体に担持され一体化する。
The laminated sintered body is taken out from the container and the water content of the inorganic colloid liquid is removed. This moisture removal is performed by air drying or hot air drying the laminated sintered body under atmospheric pressure or reduced pressure. The colloidal liquid is gelled by drying, and in this state, the laminated sintered body is fired again at 900-1300'C for 13-5 hours under atmospheric pressure. As a result, the inorganic colloid particles deposited in the open pores are supported and integrated into the laminated sintered body.

第1図に本発明の多層セラミック複合焼結体の製造工程
図を示す。第2図に板状に焼結した5層のセラミック複
合焼結体10を示し、第3図に円柱状に焼結した多層セ
ラミック複合焼結体20を示す。10a及び20aは流
体通路となる多孔質セラミック層、10b及び20bは
緻密質セラミック層、11は緻密質セラミック層10b
に形成された通孔である。
FIG. 1 shows a manufacturing process diagram of the multilayer ceramic composite sintered body of the present invention. FIG. 2 shows a five-layer ceramic composite sintered body 10 sintered into a plate shape, and FIG. 3 shows a multilayer ceramic composite sintered body 20 sintered into a columnar shape. 10a and 20a are porous ceramic layers serving as fluid passages, 10b and 20b are dense ceramic layers, and 11 is a dense ceramic layer 10b.
It is a through hole formed in.

[発明の効果コ 以上述べたように、本発明の多層セラミック複合焼結体
は、グリーンシート多層積層法により多孔質セラミック
層の両面又は片面に緻密質セラミック層を積層して一体
的に焼結した後、前記セラミック層と異種の無機コロイ
ド粒子を多孔質セラミック層の開気孔に導入して多孔質
セラミック層と一体的に焼結するため、積層状態で焼成
したときに焼結体の層間にクラック、反り、剥離等の欠
陥を生じることがない。
[Effects of the Invention] As described above, the multilayer ceramic composite sintered body of the present invention is produced by laminating dense ceramic layers on both sides or one side of a porous ceramic layer by the green sheet multilayer lamination method and sintering them integrally. After that, inorganic colloid particles of a different kind from the ceramic layer are introduced into the open pores of the porous ceramic layer and sintered integrally with the porous ceramic layer. No defects such as cracks, warping, or peeling occur.

特に、緻密質セラミック層が補強材となって機械的強度
を高くするともに、多孔質セラミック層により比表面積
及び気孔容積がそれぞれ大きくなる。
In particular, the dense ceramic layer acts as a reinforcing material to increase mechanical strength, and the porous ceramic layer increases the specific surface area and pore volume.

また、多孔質セラミック層の開気孔に導入されてこの多
孔質セラミック層と一体的に焼結する無機コロイド粒子
の粒径に応じて支持体である積層焼結体の細孔径を任意
に調整することができる。
Further, the pore size of the laminated sintered body serving as the support is arbitrarily adjusted according to the particle size of the inorganic colloid particles introduced into the open pores of the porous ceramic layer and sintered integrally with the porous ceramic layer. be able to.

更に、無機コロイド粒子のもつ物性と支持体である積層
焼結体の多孔質セラミック層のもつ物性を複合すること
ができる。このため多孔質セラミック層に導入する無機
コロイド粒子を選択することにより、本発明の多層セラ
ミック複合焼結体を触媒担体又はフィルタとして利用す
ることができる。
Furthermore, the physical properties of the inorganic colloid particles and the physical properties of the porous ceramic layer of the laminated sintered body serving as the support can be combined. Therefore, by selecting the inorganic colloid particles to be introduced into the porous ceramic layer, the multilayer ceramic composite sintered body of the present invention can be used as a catalyst carrier or a filter.

[実施例] 次に本発明の実施例を詳しく説明する。[Example] Next, embodiments of the present invention will be described in detail.

〈実施例1〉 アルミニウムイソプロポキシド[A Q (C3H70
) 3]を加水分解してベーマイト[A Q OOH]
を生成させ、これにpH2〜4に調整した水を加えて解
膠し、粒径が数10〜1000への微細なコロイド粒子
が分散したアルミナ濃度5重量%の安定な擬ベーマイト
ゾルを得た。
<Example 1> Aluminum isopropoxide [A Q (C3H70
) 3] to produce boehmite [A Q OOH]
was produced and peptized by adding water adjusted to pH 2 to 4 to obtain a stable pseudo-boehmite sol with an alumina concentration of 5% by weight in which fine colloidal particles with a particle size of several 10 to 1000 were dispersed. .

緻密質層用スラリーを調製するために、このゾルに焼結
助剤としてシリカコロイド、酢酸マグネシウム、酢酸カ
ルシウムを、更に水溶性バインダとしてポリビニルアル
コールを添加した。これらの焼結助剤は緻密質アルミナ
層に焼結したときの組成比が A、Q208:5iOz:MgO:Ca0=92: 7
: 2: 1になるようにそれぞれ添加した。またバイ
ンダはこの固形分に対して40重量%添加混合した。こ
れにより固形分が4重量%のスラリーを調製した。
In order to prepare a slurry for a dense layer, silica colloid, magnesium acetate, and calcium acetate were added as sintering aids to this sol, and polyvinyl alcohol was further added as a water-soluble binder. These sintering aids have a composition ratio of A, Q208:5iOz:MgO:Ca0=92:7 when sintered into a dense alumina layer.
: 2:1. The binder was added in an amount of 40% by weight based on the solid content. As a result, a slurry having a solid content of 4% by weight was prepared.

このスラリーを移動担体である高密度ポリエチレンテー
プ上にドクターブレード法により厚さ約0.4mmにな
るようにコーティングした後、乾燥し、スラリーの分散
媒である水を脱離させて厚さ約20μmの緻密層用グリ
ーンシートを得た。緻密質層用グリーンシートには直径
100μmの通孔を1平方cm当り9個穿設した。
This slurry is coated onto a high-density polyethylene tape, which is a moving carrier, to a thickness of approximately 0.4 mm using a doctor blade method, and then dried to remove water, which is a dispersion medium of the slurry, to a thickness of approximately 20 μm. A green sheet for dense layer was obtained. Nine holes with a diameter of 100 μm were bored per 1 square cm in the green sheet for the dense layer.

一方、多孔化し易くするために焼結助剤を添加しない以
外は上記と同様にして厚さ約60μmの多孔質層用グリ
ーンシートを得た。
On the other hand, a green sheet for a porous layer having a thickness of about 60 μm was obtained in the same manner as above except that no sintering aid was added to facilitate porosity.

第2図に示すように、緻密質層用グリーンシートの両面
に多孔質層用グリーンシートを接着し、これらの多孔質
層用グリーンシートの外面に更に緻密質層用グリーンシ
ートを接着して、5層のグリーン成形体を得た。接着剤
には1%濃度のポリビニルブチラールのイソプロピルア
ルコール溶液を用いた。
As shown in FIG. 2, green sheets for a porous layer are adhered to both sides of green sheets for a dense layer, and green sheets for a dense layer are further adhered to the outer surfaces of these green sheets for a porous layer. A 5-layer green molded body was obtained. An isopropyl alcohol solution of polyvinyl butyral with a concentration of 1% was used as the adhesive.

次にこの5層のグリーン成形体を焼成炉に入れ1300
 ’Cで1時間、大気圧下で焼成し5層の積層焼結体を
得た。多孔質アルミナ層の細孔径分布及び気孔率を調べ
るため、多孔質層用グリーンシートだけを1000℃、
1200°C,1300℃、14000C,1500°
Cでそれぞれ1時間、大気圧下で焼成した。その結果を
第4図及び第5図に示す。第4図より焼成温度が130
0℃以上になると、細孔容積が0 、1 c+r+37
g以」二でしかも細孔径が250Å以上になり、150
0℃になると細孔容積が0 、2 cm’/g以」二で
しかも細孔径が750〜1250人の範囲に極めて多く
分布することが判った。また第5図より多孔質アルミナ
層の細孔容積は0.2〜0.4 cm37gの範囲に、
気孔率は40〜60%の範囲にそれぞれあり、焼成温度
の上昇とともに細孔容積及び気孔率は小さくなることが
判った。
Next, this 5-layer green molded body was placed in a firing furnace for 1300
It was fired for 1 hour at C. under atmospheric pressure to obtain a 5-layer laminated sintered body. In order to investigate the pore size distribution and porosity of the porous alumina layer, only the green sheet for the porous layer was heated at 1000°C.
1200°C, 1300°C, 14000°C, 1500°
C. for 1 hour each under atmospheric pressure. The results are shown in FIGS. 4 and 5. From Figure 4, the firing temperature is 130
At temperatures above 0°C, the pore volume becomes 0,1 c+r+37
In addition, the pore diameter is 250 Å or more, and 150 Å or more.
It was found that at 0°C, the pore volume was 0.2 cm'/g or more, and the pore diameters were extremely distributed in the range of 750 to 1250 cm'/g. Also, from Figure 5, the pore volume of the porous alumina layer is in the range of 0.2 to 0.4 cm37g,
It was found that the porosity was in the range of 40 to 60%, and the pore volume and porosity decreased as the firing temperature increased.

一方、前記5層の積層焼結体を水を貯えたオートクレー
ブ内に入れ、水に浸漬した。次いでこの水にチタニウム
アルコキシドを添加してチタニウムアルコキシドを加水
分解しゾルを生成させた。
On the other hand, the five-layered laminated sintered body was placed in an autoclave containing water and immersed in water. Next, titanium alkoxide was added to this water to hydrolyze the titanium alkoxide to produce a sol.

このゾルに解膠剤として硝酸を添加混合した。これらの
添加割合は水/アルコキシドがモル比で100であって
、硝酸/アルコキシドかモル比で0.1であった。これ
によりゾルが多孔質アルミナ層の開気孔に導入された。
Nitric acid was added and mixed as a deflocculant to this sol. The molar ratio of water/alkoxide was 100, and the molar ratio of nitric acid/alkoxide was 0.1. This introduced the sol into the open pores of the porous alumina layer.

オートクレーブ内で室温のゾルを水熱処理温度である1
50’Cまで毎分5℃の割合で昇温した。
Hydrothermally treat the sol at room temperature in an autoclave at a temperature of 1
The temperature was increased to 50'C at a rate of 5°C per minute.

150℃に達したところで加熱を止め、3時間維持した
。続いて150℃から100 ’Cまで毎分5℃の割合
で降温し、開気孔内にチタニウムコロイド粒子を析出さ
せた。
Heating was stopped when the temperature reached 150°C and maintained for 3 hours. Subsequently, the temperature was lowered from 150°C to 100'C at a rate of 5°C per minute to precipitate titanium colloid particles within the open pores.

オートクレーブから積層焼結体を取出し、風乾してゾル
をゲル化した後、再度積層焼結体を900℃で3時間、
大気圧下で焼成した。二酸化チタンが多孔質アルミナ層
に担持された5層のセラミック複合焼結体が得られた。
The laminated sintered body was removed from the autoclave, air-dried to gel the sol, and then the laminated sintered body was heated again at 900°C for 3 hours.
Fired under atmospheric pressure. A five-layer ceramic composite sintered body in which titanium dioxide was supported on a porous alumina layer was obtained.

第6図はこの多孔質セラミック層の断面の粒子構造を主
に示すために35oO倍に拡大した電子顕微鏡写真図で
ある。第6図より多孔質セラミック層と緻密質セラミッ
ク層の間にはクラック、剥離等の欠陥は一切見られなか
った。この焼結体の曲げ強度は40kgf/mm2であ
った。
FIG. 6 is an electron micrograph enlarged 350 times to mainly show the grain structure of the cross section of this porous ceramic layer. From FIG. 6, no defects such as cracks or peeling were observed between the porous ceramic layer and the dense ceramic layer. The bending strength of this sintered body was 40 kgf/mm2.

単層の緻密質焼結シート及び二酸化チタンが担持された
単層の多孔質焼結シートの気孔率を調べたところ、それ
ぞれ0.5%及び50%であった。
The porosity of the single-layer dense sintered sheet and the single-layer porous sintered sheet supporting titanium dioxide was examined and found to be 0.5% and 50%, respectively.

このことから5層のセラミック複合焼結体のうち緻密質
セラミック層の気孔率も0.5%と類推され、多孔質セ
ラミック層の気孔率も50%と類推される。また5層の
セラミック複合焼結体全体の気孔率は33%であった。
From this, the porosity of the dense ceramic layer of the five-layer ceramic composite sintered body is estimated to be 0.5%, and the porosity of the porous ceramic layer is also estimated to be 50%. The porosity of the entire five-layer ceramic composite sintered body was 33%.

〈実施例2〉 試薬酢酸マグネシウム7gを水10gに溶解した高濃度
の酢酸マグネシウム水溶液を作成し、この溶液中に実施
例1で得られた5層の積層焼結体を浸漬した。上記水溶
液から積層焼結体を取出し風乾した後、900℃で3時
間、大気圧下で焼成したところ、酸化マグネシウムが多
孔質セラミック層に担持された5層のセラミック複合焼
結体が得られた。
<Example 2> A highly concentrated aqueous magnesium acetate solution was prepared by dissolving 7 g of reagent magnesium acetate in 10 g of water, and the five-layer sintered body obtained in Example 1 was immersed in this solution. The laminated sintered body was taken out from the aqueous solution, air-dried, and then fired at 900°C for 3 hours under atmospheric pressure, resulting in a 5-layer ceramic composite sintered body in which magnesium oxide was supported on the porous ceramic layer. .

第7図はこの多孔質セラミック層の断面の粒子構造を主
に示すために3500倍に拡大した電子顕微鏡写真図で
ある。
FIG. 7 is an electron micrograph enlarged 3500 times to mainly show the grain structure of the cross section of this porous ceramic layer.

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

第1図は本発明の多層セラミック複合焼結体の製造工程
図。 第2図は焼結した5層のセラミック複合焼結体の斜視図
。 第3図は焼結した円柱状のセラミック複合焼結体の斜視
図。 第4図は無機コロイド粒子が開気孔に導入される前の多
孔質焼結シートの焼成温度による細孔径分布と細孔容積
の変化を示す図。 第5図は多孔質焼結シートの焼成温度による細孔容積及
び気孔率の変化を示す図。 第6図及び第7図は多層セラミック複合焼結体の多孔質
アルミナ層の断面の粒子構造を主に示す電子顕微鏡写真
図である。 10.20:セラミック複合焼結体、 10a、20a:多孔質アルミナ層、 10b、20b:緻密質アルミナ層、 11:通孔。
FIG. 1 is a manufacturing process diagram of the multilayer ceramic composite sintered body of the present invention. FIG. 2 is a perspective view of a sintered five-layer ceramic composite sintered body. FIG. 3 is a perspective view of a sintered cylindrical ceramic composite sintered body. FIG. 4 is a diagram showing changes in pore size distribution and pore volume depending on the firing temperature of the porous sintered sheet before inorganic colloid particles are introduced into the open pores. FIG. 5 is a diagram showing changes in pore volume and porosity depending on the firing temperature of a porous sintered sheet. FIGS. 6 and 7 are electron micrographs mainly showing the particle structure of the cross section of the porous alumina layer of the multilayer ceramic composite sintered body. 10.20: Ceramic composite sintered body, 10a, 20a: Porous alumina layer, 10b, 20b: Dense alumina layer, 11: Through hole.

Claims (1)

【特許請求の範囲】 1)多孔質セラミック層の両面又は片面に前記多孔質セ
ラミック層と同種のセラミック原料からなる緻密質セラ
ミック層が積層されて一体的に焼結され、前記多孔質セ
ラミック層に開気孔が形成された積層焼結体を支持体と
する多層セラミック焼結体であって、 前記セラミック層と異種のセラミック原料からなる無機
コロイド粒子が前記開気孔に導入されかつ前記多孔質セ
ラミック層と一体的に焼結されたことを特徴とする多層
セラミック複合焼結体。 2)多孔質セラミック層の気孔率が20〜60%の範囲
にあり、緻密質セラミック層の気孔率が0.01〜5%
の範囲にある請求項1記載の多層セラミック複合焼結体
。 3)緻密質セラミック層に多孔質セラミック層の開気孔
に連通する通孔が設けられた請求項1又は2記載の多層
セラミック複合焼結体。 4)水を分散媒とした第1無機コロイド液に第1焼結助
剤と第1水溶性バインダを添加混合して緻密質層用スラ
リーを調製し、 この緻密質層用スラリーを成膜乾燥して緻密質層用グリ
ーンシートを成形し、 水を分散媒とし、前記第1無機コロイド液と同種の第2
無機コロイド液に焼結助剤を添加しないか又は前記第1
焼結助剤より少量の第2焼結助剤と第2水溶性バインダ
を添加混合して多孔質層用スラリーを調製し、 この多孔質層用スラリーを成膜乾燥して多孔質層用グリ
ーンシートを成形し、 前記多孔質層用グリーンシートの両面又は片面に前記緻
密質層用グリーンシートを接着剤により接着し、 前記接着したグリーン成形体を1000〜1600℃で
焼成して積層焼結体を形成し、水を分散媒とし、前記第
1及び第2無機コロイド液と異種の第3無機コロイド液
を前記積層焼結体の多孔質セラミック層に導入し、 前記第3無機コロイド液を水熱処理した後、冷却して前
記多孔質セラミック層の開気孔に無機コロイド粒子を析
出させ、 前記無機コロイド粒子の析出した積層焼結体を再度焼成
する多層セラミック複合焼結体の製造方法。 5)第1、第2又は第3無機コロイド液のいずれか1種
又は2種以上が金属アルコキシドを加水分解した後、こ
の加水分解生成物を解膠処理して得られる無機コロイド
液である請求項4記載の多層セラミック複合焼結体の製
造方法。 6)第3無機コロイド液の水熱処理がオートクレーブ内
で行われる請求項4記載の多層セラミック複合焼結体の
製造方法。
[Claims] 1) A dense ceramic layer made of the same type of ceramic raw material as the porous ceramic layer is laminated on both sides or one side of the porous ceramic layer and is integrally sintered, and the porous ceramic layer A multilayer ceramic sintered body using a laminated sintered body in which open pores are formed as a support, wherein inorganic colloid particles made of a ceramic raw material different from the ceramic layer are introduced into the open pores, and the porous ceramic layer A multilayer ceramic composite sintered body characterized by being integrally sintered with. 2) The porosity of the porous ceramic layer is in the range of 20 to 60%, and the porosity of the dense ceramic layer is 0.01 to 5%.
The multilayer ceramic composite sintered body according to claim 1, which falls within the range of . 3) The multilayer ceramic composite sintered body according to claim 1 or 2, wherein the dense ceramic layer is provided with through holes communicating with the open pores of the porous ceramic layer. 4) Prepare a slurry for a dense layer by adding and mixing a first sintering aid and a first water-soluble binder to a first inorganic colloid liquid using water as a dispersion medium, and form and dry this slurry for a dense layer. A green sheet for a dense layer is formed using water as a dispersion medium, and a second inorganic colloid liquid of the same type as the first inorganic colloid liquid is formed.
No sintering aid is added to the inorganic colloid liquid, or the first
A slurry for the porous layer is prepared by adding and mixing a second sintering aid and a second water-soluble binder in a smaller amount than the sintering aid, and this slurry for the porous layer is formed and dried to form a green for the porous layer. A sheet is formed, the dense layer green sheet is adhered to both sides or one side of the porous layer green sheet with an adhesive, and the adhered green molded body is fired at 1000 to 1600°C to obtain a laminated sintered body. and introducing a third inorganic colloid liquid different from the first and second inorganic colloid liquids into the porous ceramic layer of the laminated sintered body, using water as a dispersion medium, and introducing the third inorganic colloid liquid into the porous ceramic layer of the laminated sintered body. A method for producing a multilayer ceramic composite sintered body, which comprises heat-treating, cooling, precipitating inorganic colloid particles in the open pores of the porous ceramic layer, and firing the laminated sintered body in which the inorganic colloid particles have been precipitated again. 5) A claim that any one or more of the first, second, or third inorganic colloid liquid is an inorganic colloid liquid obtained by hydrolyzing a metal alkoxide and then peptizing the hydrolysis product. Item 4. A method for producing a multilayer ceramic composite sintered body according to Item 4. 6) The method for producing a multilayer ceramic composite sintered body according to claim 4, wherein the hydrothermal treatment of the third inorganic colloid liquid is performed in an autoclave.
JP23159290A 1990-08-31 1990-08-31 Sintered multilayer composite ceramics and production thereof Pending JPH04114981A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23159290A JPH04114981A (en) 1990-08-31 1990-08-31 Sintered multilayer composite ceramics and production thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23159290A JPH04114981A (en) 1990-08-31 1990-08-31 Sintered multilayer composite ceramics and production thereof

Publications (1)

Publication Number Publication Date
JPH04114981A true JPH04114981A (en) 1992-04-15

Family

ID=16925936

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23159290A Pending JPH04114981A (en) 1990-08-31 1990-08-31 Sintered multilayer composite ceramics and production thereof

Country Status (1)

Country Link
JP (1) JPH04114981A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0517261A (en) * 1991-07-05 1993-01-26 Kikusui Kagaku Kogyo Kk Laminated porous ceramic fired body

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0517261A (en) * 1991-07-05 1993-01-26 Kikusui Kagaku Kogyo Kk Laminated porous ceramic fired body

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