JPH0243689B2 - GARASUHATSU HOTAINOSEIZOHOHO - Google Patents

GARASUHATSU HOTAINOSEIZOHOHO

Info

Publication number
JPH0243689B2
JPH0243689B2 JP4358983A JP4358983A JPH0243689B2 JP H0243689 B2 JPH0243689 B2 JP H0243689B2 JP 4358983 A JP4358983 A JP 4358983A JP 4358983 A JP4358983 A JP 4358983A JP H0243689 B2 JPH0243689 B2 JP H0243689B2
Authority
JP
Japan
Prior art keywords
glass
foam
mixture
powder
organic structure
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 - Lifetime
Application number
JP4358983A
Other languages
Japanese (ja)
Other versions
JPS59169943A (en
Inventor
Hiroaki Hayashi
Kazuhiro Fukumoto
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.)
Toyota Central R&D Labs Inc
Original Assignee
Toyota Central R&D Labs Inc
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 Toyota Central R&D Labs Inc filed Critical Toyota Central R&D Labs Inc
Priority to JP4358983A priority Critical patent/JPH0243689B2/en
Publication of JPS59169943A publication Critical patent/JPS59169943A/en
Publication of JPH0243689B2 publication Critical patent/JPH0243689B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/14Other self-supporting filtering material ; Other filtering material
    • B01D39/20Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
    • B01D39/2068Other inorganic materials, e.g. ceramics
    • B01D39/2093Ceramic foam

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Glass Compositions (AREA)
  • Surface Treatment Of Glass (AREA)

Description

【発明の詳細な説明】 本発明は、ガラス発泡体の製造方法の改良に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a method for manufacturing glass foam.

従来のガラス発泡体の製造方法は、ガラス発泡
剤を含むガラス微粉末を発泡金型内に入れ、ガラ
ス粉末の軟化点以上に加熱し、かつ加熱によりガ
ラス発泡剤を発泡させて、ガラス発泡体を製造し
ている。この従来の製造方法においては、加熱に
より、原料粉末が発泡体になる際に、金型内で体
積膨張が生じる。このため、成形品の上方角部の
成形が不揃いになり、また、金型が変形するため
一定形状のガラス発泡体を製造するのが困難であ
つた。
The conventional method for manufacturing glass foam is to place fine glass powder containing a glass foaming agent into a foaming mold, heat it above the softening point of the glass powder, and foam the glass foaming agent by heating to form a glass foam. is manufactured. In this conventional manufacturing method, when the raw material powder is turned into a foam by heating, volumetric expansion occurs within the mold. As a result, the upper corners of the molded product are not formed uniformly, and the mold is deformed, making it difficult to manufacture a glass foam having a constant shape.

それ故、直方体形状のガラス発泡体を製造する
に際しては、比較的大きいガラス発泡体を製造
し、発泡体の上下面あるいは側面部を切り取り直
方体形状の発泡体としていた。しかし、この方法
による場合には、多量の切り屑が発生し、収率が
悪いといつた問題点があつた。
Therefore, when manufacturing a rectangular parallelepiped-shaped glass foam, a relatively large glass foam is manufactured, and the upper and lower surfaces or side portions of the foam are cut off to obtain a rectangular parallelepiped-shaped foam. However, when using this method, there were problems in that a large amount of chips were generated and the yield was poor.

また、従来のガラス発泡体の製造方法において
は金型内で大きな膨張が生じるために、ガラス発
泡体に歪が発生し、得られる成形品にクラツクが
発生しやすい等の問題点があつた。さらに、金型
が酸化腐食されるという問題もあつた。
In addition, in the conventional method for manufacturing glass foam, large expansion occurs within the mold, which causes distortion in the glass foam, resulting in problems such as the tendency for cracks to occur in the resulting molded product. Furthermore, there was also the problem that the mold was oxidized and corroded.

本発明は、かかる従来技術の問題点を解消し、
歪等の欠陥が存在しないガラス発泡体を簡単に製
造する方法を提供しようとするものである。
The present invention solves the problems of the prior art,
The present invention aims to provide a method for easily manufacturing a glass foam free of defects such as distortion.

すなわち、本発明は、内部に空孔を有する有機
質構造体の骨格に、ガラス粉末と発泡剤とから成
る混合物を付着せしめて予備成形体を形成せしめ
る第一工程と、これらを加熱して上記骨格を除去
すると共に上記混合物から成り連通気孔を有する
中間成形体を形成せしめる第二工程と、更にこれ
らを高温に加熱して上記混合物を発泡せしめる第
三工程よりなることを特徴とするガラス発泡体の
製造方法にある。
That is, the present invention includes a first step of attaching a mixture of glass powder and a foaming agent to the skeleton of an organic structure having pores inside to form a preform, and heating the mixture to form the skeleton. A second step of removing the above mixture and forming an intermediate formed body having continuous pores, and a third step of heating the above mixture to a high temperature to foam the mixture. It's in the manufacturing method.

本発明方法によれば、ガラス発泡体を製造する
工程で、発泡剤による体積膨張を中間成形体の内
部に含有する気泡により吸収するため、歪のない
ガラス発泡体を製造することができる。それ故、
最初の有機質構造体とほぼ同一の形状、大きさの
ガラス発泡体を製造することができ、初期の段階
からガラス発泡体の形状を定めることができる。
また、そのため、所望形状のガラス発泡体を形成
するために切り捨てるべき部分が非常に少なくな
り、収率が向上する。また、成形を行うための金
型を特別に使用する必要はなく、製造が簡単であ
る。また、金型を用いることによつて起こる歪や
割れ等の欠陥が存在しないガラス発泡体を得るこ
とができる。更に、有機質構造体に付着させるガ
ラス粉末と発泡剤との混合物の量により、ガラス
発泡体の内部に小さな独立気泡あるいは連通気泡
のどちらをも選択的に形成することができる。し
かも、その独立気泡は、全体に均質で多数形成さ
れており、機械的強度及び断熱特性にすぐれたも
のにすることができ、一方、連通気泡を含有した
ガラス発泡体においても、均一の大きさの気泡を
形成しているため、フイルター、吸音材等に使用
することができる。
According to the method of the present invention, in the step of manufacturing a glass foam, the volumetric expansion caused by the blowing agent is absorbed by the air bubbles contained inside the intermediate molded body, so that a glass foam without distortion can be manufactured. Therefore,
It is possible to produce a glass foam having almost the same shape and size as the initial organic structure, and the shape of the glass foam can be determined from an early stage.
Also, therefore, the portion that must be cut off to form a glass foam of a desired shape is significantly reduced, improving yield. In addition, there is no need to use a special mold for molding, and manufacturing is simple. Further, a glass foam can be obtained that is free from defects such as distortion and cracks caused by using a mold. Further, depending on the amount of the mixture of glass powder and blowing agent deposited on the organic structure, either small closed cells or open cells can be selectively formed inside the glass foam. Moreover, the closed cells are homogeneous throughout and are formed in large numbers, making it possible to create products with excellent mechanical strength and heat insulation properties. Because it forms bubbles, it can be used in filters, sound absorbing materials, etc.

本発明方法において、第一工程で使用する内部
に空孔を有する有機質構造体としては、ポリウレ
タンフオーム、ポリスチレンフオーム、ポリエチ
レンフオーム等の発泡状態の有機物質、或いはへ
ちまややしのみ等の綿状構造で内部に多数の空孔
を有する有機質体がある。上記有機質構造体は、
ガラス粉末と発泡剤との混合物をその骨格に付着
させる際に、容易にその内部に該混合物を浸透さ
せ、含浸させうるものを用いる。その意味で、上
記ポリウレタンフオーム等の発泡体はセル膜の存
在しない構造のものが好ましい。また、上記有機
質構造体は上記混合物の含浸の際、収縮あるいは
膨潤等の形状の変化を起こさない構造のものが好
ましい。
In the method of the present invention, the organic structure having pores inside used in the first step may be a foamed organic material such as polyurethane foam, polystyrene foam, polyethylene foam, or a cotton-like structure such as loofah or palm chisel. There is an organic body with many pores inside. The above organic structure is
When adhering a mixture of glass powder and a blowing agent to the skeleton, a material that can be easily penetrated and impregnated with the mixture is used. In this sense, it is preferable that the foam such as the polyurethane foam has a structure in which no cell membrane is present. Further, the organic structure preferably has a structure that does not cause changes in shape such as shrinkage or swelling when impregnated with the mixture.

また、ガラス粉末としては、通常のソーダ石灰
ガラス、ほう酸ガラスその他種々のガラスの粉末
を使用する。発泡剤としては、ガラス粉末の軟化
温度以上に加熱することにより、熱分解を起こ
し、炭酸ガス、酸素等の気体を発生する。炭酸カ
ルシウム、ドロマイト等の無機化合物あるいはガ
ラスの軟化温度以上で燃焼して炭酸ガス等を発生
するカーボン粉末等を使用する。
Further, as the glass powder, ordinary soda lime glass, boric acid glass, and various other glass powders are used. As a blowing agent, when heated above the softening temperature of glass powder, it causes thermal decomposition and generates gases such as carbon dioxide and oxygen. Inorganic compounds such as calcium carbonate and dolomite, or carbon powder that burns at a temperature higher than the softening temperature of glass and generates carbon dioxide gas, etc., are used.

次に、これらガラス粉末と発泡剤とを混合す
る。この混合に当つては、その混合物の前記骨格
への付着性の向上及び付着量の増加を図るため、
粘着剤として、水ガラス、ポリビニールアルコー
ル、酢酸ビニルエマルジヨン、カルボキシメチル
セルロース(CMC)等の有機粘着剤、エポキシ
樹脂等の反応性接着剤をも併用することができ
る。
Next, these glass powders and a foaming agent are mixed. In this mixing, in order to improve the adhesion of the mixture to the skeleton and increase the amount of adhesion,
As the adhesive, organic adhesives such as water glass, polyvinyl alcohol, vinyl acetate emulsion, carboxymethyl cellulose (CMC), and reactive adhesives such as epoxy resins can also be used.

本発明の第一工程である有機質構造体の骨格に
前記混合物を付着させる方法としては、例えば、
発泡剤とガラス粉末と、水ガラス等の粘着剤とを
混合してスラリーを作り、このスラリー中に、ポ
リウレタンフオーム等の有機質構造体を浸漬した
後、取り出し乾燥する。これにより、上記ガラス
粉末と発泡剤との混合物を有機質構造体に均一に
含浸させた予備成形体を形成する。
The method of attaching the mixture to the skeleton of the organic structure, which is the first step of the present invention, includes, for example,
A foaming agent, glass powder, and an adhesive such as water glass are mixed to form a slurry, and an organic structure such as polyurethane foam is immersed in this slurry, then taken out and dried. As a result, a preformed body is formed in which the organic structure is uniformly impregnated with the mixture of the glass powder and the blowing agent.

この場合、ガラス粉末と発泡剤との混合割合
は、ガラス粉末100重量部に対して発泡剤1ない
し10重量部の範囲が好ましい。この発泡剤が、こ
の範囲以下では、発泡剤を発泡させる加熱工程に
おいて、気泡発生が充分に起こらず、成形体の断
熱特性が低くなる傾向がある。一方、この範囲以
上では、気泡が発生しすぎて、成形体の形状がゆ
がみ、しかも機械的強度が低下する傾向にある。
In this case, the mixing ratio of the glass powder and the blowing agent is preferably in the range of 1 to 10 parts by weight of the blowing agent per 100 parts by weight of the glass powder. If the blowing agent is below this range, bubbles will not be sufficiently generated in the heating step for foaming the blowing agent, and the heat insulation properties of the molded article will tend to deteriorate. On the other hand, above this range, too many bubbles are generated, the shape of the molded article is distorted, and the mechanical strength tends to decrease.

また、水ガラス等の粘着剤の添加量はガラス粉
末100重量部に対して1ないし10重量部が好まし
い。水ガラス等の粘着剤がこの範囲以下では、ス
ラリーの粘度が低く、逆に、この範囲以上では粘
度が高くなり、いずれの場合も有機質構造体への
付着作業がやりにくくなる。
Further, the amount of the adhesive such as water glass added is preferably 1 to 10 parts by weight per 100 parts by weight of the glass powder. If the adhesive such as water glass is below this range, the viscosity of the slurry will be low, whereas if it is above this range, the viscosity will be high, and in either case, it will be difficult to attach the slurry to the organic structure.

さらに、有機質構造体へ前記混合物を付着させ
る割合は、例えば、有機質構造体100重量部に対
して、該混合物400ないし1200重量部の範囲が好
ましい。混合物がこの範囲以上の場合には、有機
質構造体により形成される連通気孔が少なく、発
泡剤による発泡工程での発泡ガラスの体積増加を
吸収することが困難となり、成形体の外観上の体
積が増加し、ガラス発泡体の形状のゆがみ、歪が
生じてくる。一方、この範囲以下では、成形体中
に大きな気泡が残留することになり、械械的強
度、断熱特性が低下する。
Further, the proportion of the mixture to be adhered to the organic structure is preferably in the range of 400 to 1200 parts by weight, for example, per 100 parts by weight of the organic structure. If the mixture exceeds this range, there will be fewer continuous pores formed by the organic structure, making it difficult to absorb the volume increase of foamed glass during the foaming process using a foaming agent, and the apparent volume of the molded product will increase. As a result, the shape of the glass foam becomes distorted and distorted. On the other hand, below this range, large bubbles will remain in the molded product, resulting in a decrease in mechanical strength and heat insulation properties.

上記以外に前記混合物を有機質構造体に付着さ
せる方法としては、網目の非常に細かいポリウレ
タンフオーム等の有機質構造体の空隙に該混合物
を埋め込んで成形体を形成する方法、あるいは、
有機質構造体を酢酸ビニルエマルジヨン等の接着
剤で湿めらせて混合物の粉末を付着させて成形体
とする方法もある。
In addition to the above methods, methods for attaching the mixture to an organic structure include a method of embedding the mixture into the voids of an organic structure such as polyurethane foam with a very fine mesh to form a molded body;
There is also a method of moistening an organic structure with an adhesive such as vinyl acetate emulsion and attaching powder of the mixture to form a molded body.

なお、上記のように形成された有機質構造体に
付着した余分のガラス粉末と発泡剤とのスラリー
の除去には、遠心分離法、圧力エアー吹付法、真
空吸引法等により行うことができる。
Note that the slurry of excess glass powder and foaming agent adhering to the organic structure formed as described above can be removed by a centrifugation method, a pressurized air blowing method, a vacuum suction method, or the like.

次に、第二工程においては、有機質構造体の分
解温度以上、例えば、ポリウレタンフオームの場
合には、250℃程度に加熱し、有機質構造体とし
てのポリウレタンフオームを熱分解除去する。こ
れによつて前記混合物から構成され、その内部に
多数の連通気孔を有する中間成形体が形成され
る。
Next, in the second step, the organic structure is heated to a temperature higher than the decomposition temperature of the organic structure, for example, about 250° C. in the case of polyurethane foam, and the polyurethane foam as the organic structure is thermally decomposed and removed. As a result, an intermediate molded body made of the mixture and having a large number of communicating holes therein is formed.

次に、第三工程においては、上記中間成形体を
第二工程より高い温度に加熱し、中間成形体を構
成するガラス粉末を軟化させると共に発泡剤を発
泡させる。この際、発泡剤は分解して気体を発生
し、軟化したガラス中に多数の気泡を生成する。
しかして、この発泡の際に、ガラス気泡は上記第
二工程で形成した連通気孔の内部を埋める。ま
た、この際、第一工程で付着させたガラス粉末の
量が多い場合には、ガラスの体積膨張が大きく、
連通気孔のほとんどを埋めて、小さな独立気泡を
形成する。一方、ガラス粉末の量が少ない場合に
は、連通気孔が残留する。
Next, in the third step, the intermediate molded body is heated to a higher temperature than in the second step to soften the glass powder constituting the intermediate molded body and foam the foaming agent. At this time, the blowing agent decomposes and generates gas, creating a large number of bubbles in the softened glass.
During this foaming, the glass bubbles fill the inside of the continuous holes formed in the second step. In addition, at this time, if the amount of glass powder deposited in the first step is large, the volumetric expansion of the glass will be large;
Fill most of the open pores and form small closed cells. On the other hand, when the amount of glass powder is small, communicating holes remain.

なお、本発明の第三工程での加熱方法について
は、従来のガラス発泡体を製造する加熱方法と同
様な方法で行う。例えば、ソーダ石灰ガラスをガ
ラス粉末として使用する場合には、650ないし800
℃の温度で加熱し、その後徐冷し、室温まだ冷却
してガラス発泡体を製造する。
The heating method in the third step of the present invention is the same as the heating method used to manufacture conventional glass foams. For example, when using soda-lime glass as glass powder, 650 to 800
The glass foam is produced by heating at a temperature of °C, then slowly cooling, and still cooling to room temperature.

本発明の第三工程において、ガラスの体積増加
のほとんどは、中間成形体の連通気孔により吸収
されるため、ガラス発泡体の外観上の形状の変化
が生じない。
In the third step of the present invention, most of the increase in the volume of the glass is absorbed by the continuous pores of the intermediate formed body, so that no change in the external shape of the glass foam occurs.

なお、本発明においては金型を使用することな
くガラス発泡体を製造することができるが、必要
に応じて金型を使用することもできる。
Note that in the present invention, a glass foam can be manufactured without using a mold, but a mold can also be used if necessary.

以下、本発明の実施例を説明する。 Examples of the present invention will be described below.

実施例 1 通常のソーダ石灰ガラスを粗砕してガラス粉末
とした。このガラス粉末100重量部と、発泡剤と
してのドロマイト5重量部とを加え、更に微粉砕
混合し、原料粉末混合体を製造した。この粉末混
合体105重量部に1%ポリビニールアルコール水
溶液100重量部、水ガラス(JIS3部)5重量部を
加えて撹拌し、混合物としてのスラリーを調製し
た。
Example 1 Ordinary soda-lime glass was crushed into glass powder. 100 parts by weight of this glass powder and 5 parts by weight of dolomite as a foaming agent were added and further pulverized and mixed to produce a raw material powder mixture. To 105 parts by weight of this powder mixture, 100 parts by weight of a 1% polyvinyl alcohol aqueous solution and 5 parts by weight of water glass (JIS 3 parts) were added and stirred to prepare a slurry as a mixture.

一方、内部に空孔を有する有機質構造体とし
て、第1図に示すような端面を有するセル膜の存
在しないポリウレタンフオーム(セル数13個/25
mm)を用い、このポリウレタンフオームに上記ス
ラリーを含浸させ、余分なスラリーを除去した
後、乾燥させた。この操作を5回繰り返し、その
後、室温で約24時間乾燥した。更に、その後、こ
のものを80℃で乾燥し、縦×横×高さが10×10×
3cmの予備成形体を得た。次に、この予備成形体
をセラミツク板上に置き、ガス炉内に挿入し、
徐々に昇温して、350℃とし、ポリウレタンフオ
ームを分解除去することにより、ガラス粉末と発
泡剤から成る混合物で構成された空隙率の大きい
中間成形体とした。その後、同じガス炉内で更に
750℃まで加熱、1時間保持し、ガラスを発泡さ
せた。その後徐冷し、本発明におけるガラス発泡
体を得た。このガラス発泡体の断面図を第2図に
示す。なお、同図において、斜線部分はガラス発
泡部分、実線で囲まれた部分は、気泡であり、点
線内は、中間成形体の連通気孔跡である。このガ
ラス発泡体の寸法は、縦×横×高さが11×11×
3.5cmであつた。この寸法は加熱前の予備成形体
の寸法とほぼ同じであつた。また、このガラス発
泡体は0.3〜1.5mm程度の独立気泡がほぼ内部まで
均一に分散した独立気泡のガラス発泡体であつ
た。なお、このガラス発泡体の嵩密度は0.15g/
cm3であつた。
On the other hand, as an organic structure having internal pores, polyurethane foam (13 cells/25
The polyurethane foam was impregnated with the above slurry using a polyurethane foam (mm), and after removing excess slurry, it was dried. This operation was repeated 5 times, and then dried at room temperature for about 24 hours. Furthermore, after that, this thing was dried at 80℃, and the length x width x height was 10 x 10 x
A 3 cm preform was obtained. Next, this preform is placed on a ceramic plate and inserted into a gas furnace.
The temperature was gradually raised to 350° C., and the polyurethane foam was decomposed and removed, thereby producing an intermediate molded body with a large porosity composed of a mixture of glass powder and a blowing agent. Then, in the same gas furnace,
The glass was heated to 750°C and held for 1 hour to foam the glass. Thereafter, it was slowly cooled to obtain a glass foam according to the present invention. A cross-sectional view of this glass foam is shown in FIG. In the figure, the shaded area is the glass foamed area, the area surrounded by the solid line is the air bubbles, and the area inside the dotted line is the remains of the continuous holes in the intermediate molded body. The dimensions of this glass foam are length x width x height 11 x 11 x
It was 3.5cm. This dimension was approximately the same as the dimension of the preform before heating. Further, this glass foam was a closed cell glass foam in which closed cells of about 0.3 to 1.5 mm were uniformly dispersed almost to the inside. The bulk density of this glass foam is 0.15g/
It was warm at cm3 .

実施例 2 セル膜の存在しないポリウレタンフオームに混
合物としてのスラリーを含浸させ、余分なスラリ
ーを除去して、乾燥させる工程を3回行う以外は
実施例1と同様にして本発明にかかるガラス発泡
体を製造した。このガラス発泡体の寸法は、縦×
横×高さが10.5×10.5×3.3cmであつた。
Example 2 A glass foam according to the present invention was produced in the same manner as in Example 1, except that the steps of impregnating a polyurethane foam without a cell membrane with a slurry mixture, removing excess slurry, and drying were performed three times. was manufactured. The dimensions of this glass foam are length x
The width x height was 10.5 x 10.5 x 3.3 cm.

この寸法は加熱前の成形体に比べてほぼ等しか
つた。また、このガラス発泡体は、0.5〜1.5mm程
度の連通気泡がほぼ内部まで均一に分散したガラ
ス発泡体であつた。また、このガラス発泡体の嵩
密度は0.12g/cm3であつた。
This dimension was almost the same as that of the molded product before heating. Further, this glass foam had open cells of about 0.5 to 1.5 mm uniformly dispersed almost to the inside. Moreover, the bulk density of this glass foam was 0.12 g/cm 3 .

この様にガラス発泡体が実施例1で得られたも
のと異なり、連通気泡を有し、嵩密度が低いとい
うことは、前記スラリーの含浸回数が実施例1の
場合よりも少なかつたためである。
The reason why the glass foam differs from that obtained in Example 1 in that it has open cells and has a low bulk density is because the number of times the slurry was impregnated was smaller than in Example 1. .

実施例 3 実施例1と同様にガラス粉末と発泡剤の粉末混
合体105重量部に2%ポリビニールアルコール水
溶液40重量部および水ガラス(JIS3号)5重量部
を加えて撹拌し、スラリーを調製した。このスラ
リーを実施例1と同様の構造、大きさで、セル数
のみ8個/25mmと異なるセル膜の存在しないポリ
ウレタンフオームに含浸させ、余分なスラリーを
除去した後、乾燥させた。この操作を4回繰り返
して、予備成形体を得た。この成形体の寸法は、
縦×横×高さが10×10×3cmであつた。これ以降
の工程は、実施例1と同様にしてガラス発泡体を
製造した。このガラス発泡体の寸法は、縦×横×
高さが10.5×10.5×3.5cmであり、加熱工程前の予
備成形体の寸法に比べてほぼ等しかつた。また、
このガラス発泡体は、0.5〜1mm程度の連通気泡
がほぼ内部まで均一に分散したガラス発泡体であ
つた。なお、このガラス発泡体の嵩密度は0.18
g/cm3であつた。
Example 3 In the same manner as in Example 1, 40 parts by weight of a 2% polyvinyl alcohol aqueous solution and 5 parts by weight of water glass (JIS No. 3) were added to 105 parts by weight of a powder mixture of glass powder and blowing agent and stirred to prepare a slurry. did. This slurry was impregnated into a polyurethane foam having the same structure and size as in Example 1, except for the number of cells (8 cells/25 mm) and no cell membrane, and after removing excess slurry, it was dried. This operation was repeated four times to obtain a preform. The dimensions of this molded body are
The length x width x height was 10 x 10 x 3 cm. The subsequent steps were the same as in Example 1 to produce a glass foam. The dimensions of this glass foam are length x width x
The height was 10.5 x 10.5 x 3.5 cm, which was approximately equal to the dimensions of the preform before the heating process. Also,
This glass foam was a glass foam in which open cells of about 0.5 to 1 mm were uniformly dispersed almost throughout the interior. The bulk density of this glass foam is 0.18
g/ cm3 .

実施例 4 セル膜の存在しないポリウレタンフオームに混
合物としてのスラリーを含浸させ、余分なスラリ
ーを除去して、乾燥させる工程を7回行う以外
は、実施例3と同様にして本発明にかかるガラス
発泡体を製造した。このガラス発泡体の寸法は、
縦×横×高さが11×11×3.5cmであり、加熱前の
予備成形体に比べてほぼ等しかつた。また、この
ガラス発泡体は、1mm程度の独立気泡がほぼ内部
まで均一に分散したガラス発泡体であつた。ま
た、このガラス発泡体の嵩密度は、0.20g/cm3
あつた。
Example 4 Glass foam according to the present invention was produced in the same manner as in Example 3, except that the steps of impregnating a polyurethane foam without a cell membrane with the slurry as a mixture, removing excess slurry, and drying were carried out seven times. manufactured the body. The dimensions of this glass foam are:
The length x width x height was 11 x 11 x 3.5 cm, which were almost the same as those of the preform before heating. Further, this glass foam had closed cells of about 1 mm uniformly dispersed almost inside. Further, the bulk density of this glass foam was 0.20 g/cm 3 .

この様にガラス発泡体が実施例3で得られたも
のと異なり、独立気泡を有し、嵩密度が高いとい
うことは、前記スラリーの含浸回数が実施例3の
場合よりも多かつたためである。
The reason why the glass foam differs from that obtained in Example 3 in that it has closed cells and has a high bulk density is because the number of times the slurry was impregnated was greater than in Example 3. .

実施例 5 実施例1と同様のガラス粉末と発泡剤の混合体
粉末に2%ポリビニールアルコール水溶液35重量
部および水ガラス(JIS3号)5重量部を加えて撹
拌し、スラリーを調製した。内部に空孔を有する
有機質発泡体として、軟質ウレタンフオーム(密
度0.02g/cm3セル数30個/25mm)を用いて、上記
スラリーを該軟質ウレタンフオームに含浸させ、
軟質ウレタンフオームの隙間に埋め込んだ後、乾
燥させて、実施例1と同じ寸法の予備成形体を製
造した。これ以降のガラス発泡体を製造する工程
は、実施例1と同様にして行なつた。得られたガ
ラス発泡体の寸法は、縦×横×高さが11×11×
3.5cmであり、加熱工程前の予備成形体の寸法に
比べてほぼ等しかつた。また、このガラス発泡体
は0.5〜1mm程度の独立気泡が、ほぼ内部まで均
一に分散したガラス発泡体であつた。なお、この
ガラス発泡体の嵩密度は0.21g/cm3であつた。
Example 5 35 parts by weight of a 2% aqueous polyvinyl alcohol solution and 5 parts by weight of water glass (JIS No. 3) were added to the same powder mixture of glass powder and blowing agent as in Example 1 and stirred to prepare a slurry. Using a soft urethane foam (density 0.02 g/cm 3 cells/25 mm) as an organic foam having pores inside, the above slurry is impregnated into the soft urethane foam,
After filling the gap between the soft urethane foam, it was dried to produce a preform having the same dimensions as in Example 1. The subsequent steps for manufacturing the glass foam were carried out in the same manner as in Example 1. The dimensions of the obtained glass foam are 11 x 11 x length x width x height.
The size was 3.5 cm, which was almost equal to the size of the preform before the heating process. Further, this glass foam had closed cells of about 0.5 to 1 mm uniformly dispersed almost throughout the interior. The bulk density of this glass foam was 0.21 g/cm 3 .

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

図は、本発明の実施例を示し、第1図は実施例
1におけるセル膜の存在しないポリウレタンフオ
ームの端面、第2図は実施例1で得られたガラス
発泡体の断面を示す。 1……ポリウレタンフオームの骨格、2……空
孔、3……ガラス発泡部、4……中間成形体の連
通気孔跡。
The figures show examples of the present invention; FIG. 1 shows an end face of a polyurethane foam without a cell membrane in Example 1, and FIG. 2 shows a cross section of the glass foam obtained in Example 1. 1... Skeleton of polyurethane foam, 2... Holes, 3... Glass foam portion, 4... Traces of continuous holes in intermediate molded body.

Claims (1)

【特許請求の範囲】[Claims] 1 内部に空孔を有する有機質構造体の骨格に、
ガラス粉末と発泡剤とから成る混合物を付着せし
めて予備成形体を形成せしめる第1工程と、これ
らを加熱して上記骨格を除去すると共に上記混合
物から成り連通気孔を有する中間成形体を形成せ
しめる第二工程と、更にこれらを高温に加熱して
上記混合物を発泡せしめる第三工程とよりなるこ
とを特徴とするガラス発泡体の製造方法。
1 In the skeleton of an organic structure that has pores inside,
A first step of adhering a mixture of glass powder and a foaming agent to form a preform, and a second step of heating them to remove the skeleton and forming an intermediate molded object made of the mixture and having continuous holes. A method for producing a glass foam, comprising two steps and a third step of foaming the mixture by heating these steps to a high temperature.
JP4358983A 1983-03-16 1983-03-16 GARASUHATSU HOTAINOSEIZOHOHO Expired - Lifetime JPH0243689B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4358983A JPH0243689B2 (en) 1983-03-16 1983-03-16 GARASUHATSU HOTAINOSEIZOHOHO

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4358983A JPH0243689B2 (en) 1983-03-16 1983-03-16 GARASUHATSU HOTAINOSEIZOHOHO

Publications (2)

Publication Number Publication Date
JPS59169943A JPS59169943A (en) 1984-09-26
JPH0243689B2 true JPH0243689B2 (en) 1990-10-01

Family

ID=12667972

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4358983A Expired - Lifetime JPH0243689B2 (en) 1983-03-16 1983-03-16 GARASUHATSU HOTAINOSEIZOHOHO

Country Status (1)

Country Link
JP (1) JPH0243689B2 (en)

Also Published As

Publication number Publication date
JPS59169943A (en) 1984-09-26

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