JPH07101740A - Production of porous glass ceramic - Google Patents
Production of porous glass ceramicInfo
- Publication number
- JPH07101740A JPH07101740A JP5267894A JP26789493A JPH07101740A JP H07101740 A JPH07101740 A JP H07101740A JP 5267894 A JP5267894 A JP 5267894A JP 26789493 A JP26789493 A JP 26789493A JP H07101740 A JPH07101740 A JP H07101740A
- Authority
- JP
- Japan
- Prior art keywords
- glass
- treated
- carbon
- glass powder
- 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
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Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は、例えば吸着材、触媒
の担体、電子部品の基板、高周波用磁器コンデンサの誘
電体材料等に使用することができる多孔質ガラスセラミ
ックの製造方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a porous glass ceramic which can be used, for example, as an adsorbent, a catalyst carrier, a substrate for electronic parts, a dielectric material for high frequency porcelain capacitors and the like. .
【0002】[0002]
【従来の技術】従来、次のような多孔質セラミックの製
造方法が知られている。2. Description of the Related Art Conventionally, the following methods for producing porous ceramics are known.
【0003】まず、無機粉末に有機バインダを加えてこ
れらを十分に混合し、無機粉末と有機バインダが均一に
混合した後、更に粒径50〜60μm程度の小さな有機
樹脂球を多数加えて混合し、有機樹脂球を均一に分散さ
せる。First, an organic binder is added to an inorganic powder to thoroughly mix them, and the inorganic powder and the organic binder are uniformly mixed, and then a large number of small organic resin spheres having a particle diameter of about 50 to 60 μm are added and mixed. , Evenly disperse the organic resin spheres.
【0004】次に、この有機樹脂球を分散させた混合物
を所定の形状に成形し、この成形物を300〜400℃
程度の温度で焼成する。この焼成によって成形物中の有
機樹脂球は有機バインダとともに焼失し、有機樹脂球が
焼失した後に多数の空孔が形成される。Next, the mixture in which the organic resin spheres are dispersed is molded into a predetermined shape, and the molded product is heated to 300 to 400 ° C.
Bake at moderate temperature. By this firing, the organic resin spheres in the molded product are burnt out together with the organic binder, and a large number of pores are formed after the organic resin spheres are burnt out.
【0005】次に、この多数の空孔が形成された成形物
を1000〜1300℃程度の温度で焼成する。この焼
成によって無機粉末は焼結し、成形物は多孔質セラミッ
クとなる。Next, the molded product having a large number of pores is fired at a temperature of about 1000 to 1300 ° C. By this firing, the inorganic powder is sintered and the molded product becomes a porous ceramic.
【0006】[0006]
【発明が解決しようとする課題】しかし、この方法は、
無機粉末及び有機バインダを混合した後、更に有機樹脂
球を加えて混合する必要があり、しかも有機樹脂球は無
機粉末と比重がかなり相違するので均一に混合し難く、
従って、この有機樹脂球の混合のために手間がかかると
いう問題があった。However, this method is
After mixing the inorganic powder and the organic binder, it is necessary to further add and mix the organic resin spheres, and since the organic resin spheres have a considerably different specific gravity from the inorganic powder, it is difficult to mix them uniformly.
Therefore, there is a problem that it takes time to mix the organic resin balls.
【0007】また、この方法は、有機樹脂球の比重が無
機粉末とかなり相違するので、有機樹脂球を均一に分散
させることが非常に難しく、しかも時間の経過とともに
有機樹脂球が片寄り易く、従って、空孔を均一に分散さ
せた多孔質セラミックを製造することが難しいという問
題があった。In this method, since the specific gravity of the organic resin spheres is considerably different from that of the inorganic powder, it is very difficult to uniformly disperse the organic resin spheres, and moreover, the organic resin spheres tend to shift over time, Therefore, there is a problem that it is difficult to manufacture a porous ceramic in which pores are uniformly dispersed.
【0008】更に、この方法は、空孔を形成させるため
に多量の有機樹脂球を必要とするので、この有機樹脂球
の費用のために製造コストが高くなるという問題があっ
た。Further, this method has a problem that a large amount of organic resin spheres are required to form pores, so that the manufacturing cost is increased due to the cost of the organic resin spheres.
【0009】この発明は、多数の空孔が均一に分散した
多孔質ガラスセラミックを低コストで効率的に製造する
ことができる多孔質ガラスセラミックの製造方法を提供
することを目的とする。An object of the present invention is to provide a method for producing a porous glass-ceramic, which can efficiently produce a porous glass-ceramic in which a large number of pores are uniformly dispersed at low cost.
【0010】[0010]
【課題を解決するための手段】この発明に係る多孔質ガ
ラスセラミックの製造方法は、少なくともガラス粉末と
有機バインダとからなる被処理物をこのガラス粉末が軟
化する温度まで加熱する工程と、この加熱された被処理
物を酸化性雰囲気中においてこのガラス粉末が多孔質化
する温度まで更に加熱する工程とを有するものである。A method for producing a porous glass ceramic according to the present invention comprises a step of heating an object to be treated consisting of at least a glass powder and an organic binder to a temperature at which the glass powder softens, and the heating step. And further heating the treated material in an oxidizing atmosphere to a temperature at which the glass powder becomes porous.
【0011】ここで、ガラス粉末の種類は問わないが、
軟化温度が500〜800℃と、低いものが好ましい。
また、被処理物はガラス粉末と有機バインダだけで形成
されていてもよいし、これら以外の成分が含まれていて
もよい。更に、被処理物は成形されていてもよいし、成
形されていなくてもよい。Here, the glass powder may be of any type,
It is preferable that the softening temperature is as low as 500 to 800 ° C.
Further, the object to be treated may be formed only by the glass powder and the organic binder, or may contain components other than these. Furthermore, the object to be treated may or may not be molded.
【0012】被処理物をこのガラス粉末が軟化する温度
まで加熱する工程は、被処理物中に含有されている有機
バインダを分解・炭化させてガラス粉末中にカーボンと
して残留させる工程と、この残留させたカーボンを軟化
したガラスに包み込ませる工程とに分けて考えることが
できる。The step of heating the object to be treated to a temperature at which the glass powder softens is a step of decomposing and carbonizing the organic binder contained in the object to be left in the glass powder as carbon, and the residual It can be considered separately as a step of wrapping the carbon thus made in a softened glass.
【0013】被処理物中に含有されている有機バインダ
を分解・炭化させ、ガラス粉末中にカーボンとして残留
させるための加熱の条件としては、加熱温度250〜3
50℃、加熱時間1〜2時間が好ましい。The heating conditions for decomposing and carbonizing the organic binder contained in the object to be treated and leaving it as carbon in the glass powder are heating temperatures of 250 to 3
The heating time is preferably 50 ° C. and the heating time is 1 to 2 hours.
【0014】また、被処理物中に含有されている有機バ
インダを分解・炭化させ、ガラス粉末中にカーボンとし
て残留させる工程と、この残留させたカーボンを軟化し
たガラスに包み込ませる工程は、大気中で行なってもよ
いが、N2 、Arガス等の非酸化性雰囲気中で行なう
か、真空中で行なうのが好ましい。Further, the steps of decomposing and carbonizing the organic binder contained in the object to be treated and leaving it as carbon in the glass powder and the step of wrapping the remaining carbon in the softened glass are carried out in the atmosphere. However, it is preferably performed in a non-oxidizing atmosphere such as N 2 or Ar gas or in vacuum.
【0015】ガラスが軟化する温度まで300℃/時間
以上の昇温速度で加熱すれば、被処理物中の有機バイン
ダを分解させる工程と、この分解によって形成されたカ
ーボンを軟化したガラスに包み込ませる工程を一度の加
熱で行なわせることができる。If the glass is heated to a temperature at which it softens at a heating rate of 300 ° C./hour or more, the step of decomposing the organic binder in the object to be treated and the carbon formed by this decomposition are wrapped in the softened glass. The process can be performed with a single heating.
【0016】[0016]
【作用】請求項1記載の発明においては、被処理物をガ
ラスが軟化する温度まで加熱すると、有機バインダが分
解してその一部が炭化し、この炭化して形成されたカー
ボンが軟化したガラスに包み込まれる。このガラスを酸
化性雰囲気中において更に高温に加熱すると、ガラスに
包み込まれたカーボンが燃焼してガス化し、このガスに
よってガラスが発泡する。In the invention according to claim 1, when the object to be treated is heated to a temperature at which the glass is softened, the organic binder is decomposed and a part thereof is carbonized, and the carbon formed by the carbonization is softened glass. Wrapped in. When this glass is heated to a higher temperature in an oxidizing atmosphere, the carbon wrapped in the glass burns and gasifies, and this gas causes the glass to foam.
【0017】また、請求項2記載の発明においては、ガ
ラスが軟化するまでの加熱を非酸化性雰囲気(N2 、A
r等)中又は真空中で行なうので、ガラス粉末中に残留
するカーボンが多くなり、ガラスに包み込まれるカーボ
ンの量が増加する。According to the second aspect of the invention, heating until the glass softens is performed in a non-oxidizing atmosphere (N 2 , A).
r)) or in vacuum, the amount of carbon remaining in the glass powder increases and the amount of carbon wrapped in the glass increases.
【0018】また、請求項3記載の発明においては、ガ
ラスが軟化するまでの熱処理の昇温速度を300℃/時
間より大きくしたので、ガラス粉末中に残留するカーボ
ンが多くなり、ガラスに包み込まれるカーボンの量が増
加する。Further, in the invention of claim 3, since the temperature rising rate of the heat treatment until the glass is softened is set to be higher than 300 ° C./hour, a large amount of carbon remains in the glass powder and is wrapped in the glass. The amount of carbon increases.
【0019】[0019]
実施例1 まず、ガラス粉末50重量部に有機バインダ3重量部を
加え、これらをらいかい機により十分に混合した。ここ
で、ガラス粉末としてはNa2 O・B2 O3 ・SiO2
系のホウケイ酸ガラス粉末(平均粒径0.5μm)を使
用し、有機バインダとしてポリビニルアルコール(PV
A)を使用した。Example 1 First, 3 parts by weight of an organic binder was added to 50 parts by weight of glass powder, and these were thoroughly mixed by a mulcher. Here, as the glass powder, Na 2 O · B 2 O 3 · SiO 2 is used.
-Based borosilicate glass powder (average particle size 0.5 μm) is used, and polyvinyl alcohol (PV
A) was used.
【0020】次に、らいかい機によって得られた混合物
を造粒機で粒状に造粒し、この粒状に造粒した所定量の
混合物を成形機の型内に入れ、直径9.95mm、厚さ
0.50mmの円板状に成形した。Next, the mixture obtained by the ladle mill is granulated by the granulator, and a predetermined amount of the granulated mixture is put into the mold of the molding machine, and the diameter is 9.95 mm, and the thickness is It was formed into a disk shape having a thickness of 0.50 mm.
【0021】次に、この円板状の成形物を大気中におい
て280〜300℃で2時間加熱した。有機バインダは
この加熱によって分解するとともに燃焼し、少量の炭素
成分(カーボン)を残して消失(脱バインダ)した。成
形物中に残っている残留カーボンの量を測定したとこ
ろ、3.0重量%以下であった。Next, the disk-shaped molded product was heated in the atmosphere at 280 to 300 ° C. for 2 hours. The organic binder was decomposed and burned by this heating, and a small amount of carbon component (carbon) remained and disappeared (debinding). When the amount of residual carbon remaining in the molded product was measured, it was 3.0% by weight or less.
【0022】更に、この成形物を800℃で0.5時間
加熱した。この加熱により成形物を構成しているガラス
は軟化し、この軟化したガラスに残留カーボンが包み込
まれる。Further, this molded product was heated at 800 ° C. for 0.5 hour. By this heating, the glass constituting the molded product is softened, and residual carbon is wrapped in the softened glass.
【0023】次に、この成形物を1000℃まで0.4
時間かけて加熱昇温させたところ、ガラスに包み込まれ
ていたカーボンが酸化してCO2 ガスとなり、このCO
2 ガスにより被処理物中に多数の気泡が形成され、被処
理物は多孔質ガラスセラミックとなった。Next, this molded product was heated to 1000 ° C. to 0.4
When the temperature was raised by heating over time, the carbon encased in the glass was oxidized and turned into CO 2 gas.
A large number of bubbles were formed in the object to be processed by the two gases, and the object became a porous glass ceramic.
【0024】ここで、この多孔質ガラスセラミックの気
孔率を調べたところ、20〜40%であった。また、気
孔の分散状態を調べたところ、均一になっていた。When the porosity of this porous glass-ceramic was examined, it was 20-40%. Moreover, when the dispersed state of the pores was examined, it was found to be uniform.
【0025】実施例2 非酸化性ガス(N2 、Ar等)雰囲気中において280
〜350℃で2時間加熱して脱バインダを行なった以外
は実施例1と同様の条件で実験をした。この実験におい
て、脱カーボン後に被処理物中に残っていた残留カーボ
ンは5%以下であった。また、最終的に得られた多孔質
ガラスセラミックの気孔率は30〜40%であった。更
に、気孔の分散状態を調べたところ、均一になってい
た。Example 2 280 in an atmosphere of non-oxidizing gas (N 2 , Ar, etc.)
An experiment was conducted under the same conditions as in Example 1 except that the binder was removed by heating at ˜350 ° C. for 2 hours. In this experiment, the residual carbon remaining in the object to be treated after decarbonization was 5% or less. The porosity of the finally obtained porous glass ceramic was 30 to 40%. Furthermore, when the dispersed state of the pores was examined, it was found to be uniform.
【0026】この実験においては、被処理物を非酸化性
ガス雰囲気中において加熱するので、残留カーボンが多
くなり、ガラスに多量のカーボンが包み込まれ、気孔率
が高くなるものと思われる。In this experiment, since the object to be treated is heated in a non-oxidizing gas atmosphere, it is considered that the residual carbon is increased and the glass is encased with a large amount of carbon, and the porosity is increased.
【0027】実施例3 低い温度で脱バインダを行なわせず、なるべく速い昇温
速度(>300℃/H)で混合物を加熱して混合物を構
成しているガラスを軟化させた以外は実施例1と同様の
条件で実験をした。この実験において得られた得られた
多孔質ガラスセラミックの気孔率は10〜30%であっ
た。また、気孔の分散状態を調べたところ、均一になっ
ていた。Example 3 Example 1 was repeated except that the binder was not removed at a low temperature and the glass constituting the mixture was softened by heating the mixture at a temperature rising rate (> 300 ° C./H) as high as possible. An experiment was conducted under the same conditions as. The porosity of the obtained porous glass-ceramic obtained in this experiment was 10 to 30%. Moreover, when the dispersed state of the pores was examined, it was found to be uniform.
【0028】この実験においては、被処理物を昇温させ
る速度が早いので、十分な脱バインダが行なわれず、残
留カーボンが多くなり、ガラスに多量のカーボンが包み
込まれるので、気孔率が高くなるものと思われる。In this experiment, since the rate of raising the temperature of the object to be treated is high, sufficient binder removal is not performed, the amount of residual carbon increases, and a large amount of carbon is included in the glass, resulting in a high porosity. I think that the.
【0029】[0029]
【発明の効果】請求項1記載の発明によれば、被処理物
に有機樹脂球を混合しなくてもガラスを多孔質にするこ
とができるので、ガラス粉末とは比重の異なる有機樹脂
球を均一に混合する手間が不要になり、従って、多孔質
ガラスセラミックを容易に製造することができるという
効果がある。According to the invention of claim 1, the glass can be made porous without mixing the organic resin spheres with the object to be treated, so that the organic resin spheres having a specific gravity different from that of the glass powder are used. This eliminates the need for uniform mixing, and therefore the porous glass ceramic can be easily manufactured.
【0030】また、請求項1記載の発明によれば、ガラ
スに包み込まれたカーボンを燃焼させてガス化させ、こ
のガスによってガラスを発泡させるので、多数の気孔が
均一に分散した多孔質ガラスセラミックを製造すること
ができるという効果がある。According to the first aspect of the present invention, the carbon wrapped in the glass is burned to be gasified, and the glass is foamed by this gas. Therefore, a large number of pores are dispersed uniformly in the porous glass ceramic. Has the effect that it can be manufactured.
【0031】また、請求項2記載の発明によれば、ガラ
ス粉末中に残留するカーボンが多くなり、ガラスに包み
込まれるカーボンの量が増加するので、気孔率の大きい
多孔質ガラスセラミックを製造することができるという
効果がある。According to the second aspect of the present invention, the amount of carbon remaining in the glass powder increases and the amount of carbon encased in the glass increases, so that a porous glass ceramic having a high porosity can be manufactured. There is an effect that can be.
【0032】また、請求項3記載の発明によれば、ガラ
ス粉末中に残留するカーボンが多くなり、ガラスに包み
込まれるカーボンの量が増加するので、気孔率の大きい
多孔質ガラスセラミックを製造することができるという
効果がある。According to the third aspect of the present invention, since the amount of carbon remaining in the glass powder increases and the amount of carbon encapsulated in the glass increases, it is possible to manufacture a porous glass ceramic having a high porosity. There is an effect that can be.
フロントページの続き (72)発明者 鳥羽 利一 東京都台東区上野6丁目16番20号 太陽誘 電株式会社内 (72)発明者 成田 直人 東京都台東区上野6丁目16番20号 太陽誘 電株式会社内Front page continued (72) Inventor Riichi Toba 6-16-20 Ueno Taito-ku, Tokyo 6-16-20 Ueno Solar Incorporated (72) Inventor Naoto Narita 6-16-20 Ueno Taito-ku, Tokyo Solar Induction Within the corporation
Claims (3)
からなる被処理物をこのガラス粉末が軟化する温度まで
加熱する工程と、この加熱された被処理物を酸化性雰囲
気中においてこのガラス粉末が多孔質化する温度まで更
に加熱する工程とを有することを特徴とする多孔質ガラ
スセラミックの製造方法。1. A step of heating an object to be treated comprising at least glass powder and an organic binder to a temperature at which the glass powder softens, and the heated object to be treated is porous in an oxidizing atmosphere. And a step of further heating to a temperature at which the porous glass-ceramic is produced.
空中においてガラス粉末が軟化する温度まで加熱するこ
とを特徴とする請求項1記載の多孔質ガラスセラミック
の製造方法。2. The method for producing a porous glass ceramic according to claim 1, wherein the object to be treated is heated in a non-oxidizing atmosphere or in vacuum to a temperature at which the glass powder softens.
る温度まで、300℃/時間より大きい昇温速度で加熱
することを特徴とする請求項1記載の多孔質ガラスセラ
ミックの製造方法。3. The method for producing a porous glass ceramic according to claim 1, wherein the object to be treated is heated to a temperature at which the glass powder is softened at a temperature rising rate higher than 300 ° C./hour.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5267894A JPH07101740A (en) | 1993-09-30 | 1993-09-30 | Production of porous glass ceramic |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5267894A JPH07101740A (en) | 1993-09-30 | 1993-09-30 | Production of porous glass ceramic |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH07101740A true JPH07101740A (en) | 1995-04-18 |
Family
ID=17451105
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5267894A Pending JPH07101740A (en) | 1993-09-30 | 1993-09-30 | Production of porous glass ceramic |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07101740A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6762925B2 (en) | 2002-04-01 | 2004-07-13 | Murata Manufacturing Co., Ltd. | Ceramic electronic component and method for making the same |
JP2012013438A (en) * | 2010-06-29 | 2012-01-19 | Nusac Inc | Sintered glass granule and manufacturing method thereof |
-
1993
- 1993-09-30 JP JP5267894A patent/JPH07101740A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6762925B2 (en) | 2002-04-01 | 2004-07-13 | Murata Manufacturing Co., Ltd. | Ceramic electronic component and method for making the same |
JP2012013438A (en) * | 2010-06-29 | 2012-01-19 | Nusac Inc | Sintered glass granule and manufacturing method thereof |
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