JPH0216252B2 - - Google Patents
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- Publication number
- JPH0216252B2 JPH0216252B2 JP57209015A JP20901582A JPH0216252B2 JP H0216252 B2 JPH0216252 B2 JP H0216252B2 JP 57209015 A JP57209015 A JP 57209015A JP 20901582 A JP20901582 A JP 20901582A JP H0216252 B2 JPH0216252 B2 JP H0216252B2
- Authority
- JP
- Japan
- Prior art keywords
- glass
- foam
- agent
- foaming
- cell
- 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
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C11/00—Multi-cellular glass ; Porous or hollow glass or glass particles
- C03C11/007—Foam glass, e.g. obtained by incorporating a blowing agent and heating
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Producing Shaped Articles From Materials (AREA)
- Glass Compositions (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。このため、例えば直方体形状のガラス発泡
体を製造するに当り、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を製造していた。このた
め、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。又、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体積の膨張が生じ
るために、ガラス発泡体に歪が発生し、このため
に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。また、従来の製造方法は金型を
必要とするため上記歪が特に大きかつた。さらに
金型の酸化という問題もあつた。 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. For this reason, for example, in manufacturing a rectangular parallelepiped-shaped glass foam, a relatively large glass foam is manufactured, and the top and bottom surfaces or side portions of the foam are cut to produce a rectangular parallelepiped-shaped foam. As a result, a large amount of chips were generated, resulting in a problem of poor yield. In addition, in the conventional glass foam production method, a large volume expansion occurs within the mold, which causes distortion in the glass foam, which causes problems such as cracks in the resulting molded product. The point was hot. Further, since the conventional manufacturing method requires a mold, the above-mentioned distortion is particularly large. There was also the problem of oxidation of the mold.
本発明は、上記した問題点のないガラス発泡体
の製造方法を提供するものである。即ち、本発明
のガラス発泡体の製造方法は、ガラス発泡剤とガ
ラス粉末と気泡構成剤とを用い、該気泡構成剤を
消失させることにより内部に該ガラス発泡剤によ
り膨脹する体積を吸収する多数の気泡を含むグリ
ーンコンパクトを作製する予備成形工程と、該グ
リーンコンパクトを加熱し、該ガラス発泡剤を発
泡させて該グリーンコンパクトの外形形状を大き
く変化させることなくガラス発泡体を形成する発
泡工程とからなることを特徴とする。 The present invention provides a method for manufacturing a glass foam that does not have the above-mentioned problems. That is, the method for producing a glass foam of the present invention uses a glass foaming agent, a glass powder, and a cell structuring agent, and by causing the cell structuring agent to disappear, there is a large number of foams that absorb the volume expanded by the glass foaming agent. a preforming step of producing a green compact containing air bubbles, and a foaming step of heating the green compact and foaming the glass foaming agent to form a glass foam without significantly changing the external shape of the green compact. It is characterized by consisting of.
本発明のガラス発泡体の製造方法においては、
ガラス発泡剤とガラス粉末とで構成されたグリー
ンコンパクト中に気泡構成剤を消失させて形成し
た多数の気泡を含有する。そして、このグリーン
コンパクトを加熱することによりグリーンコンパ
クトを構成するガラス粉末が軟化すると共にガラ
ス発泡剤が分解して、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。この気泡により
見掛けの体積が増大したガラスは、グリーンコン
パクト中の多数の気泡を埋める。これにより、グ
リーンコンパクトの外形寸法を大きく変化するこ
となく、全体が均質で小さな独立気泡を多く持つ
ガラス発泡体となるものである。 In the method for manufacturing a glass foam of the present invention,
A green compact composed of a glass foaming agent and glass powder contains a large number of cells formed by eliminating the cell forming agent. By heating this green compact, the glass powder constituting the green compact is softened and the glass foaming agent is decomposed to generate gas and generate a large number of bubbles in the softened glass. The glass, whose apparent volume has increased due to the air bubbles, fills the many air bubbles in the green compact. As a result, the green compact becomes a glass foam that is homogeneous as a whole and has many small closed cells, without significantly changing the external dimensions of the green compact.
本発明の内部に多数の気泡を含み、ガラス発泡
剤とガラス粉末とで構成されたグリーンコンパク
トを製造する方法は、例えばガラス発泡剤とガラ
ス粉末との混合粉末と、水ガラス等の粘着剤およ
び水でスラリーを作り、このスラリー中に、気泡
構成剤としてポリスチレンビーズ発泡体等の発泡
ビーズを混入し、発泡ビーズが均一に分散したガ
ラス発泡剤とガラス粉末との成形体を作る。 The method of manufacturing a green compact containing a large number of air bubbles inside and composed of a glass foaming agent and a glass powder includes, for example, a mixed powder of a glass foaming agent and a glass powder, an adhesive such as water glass, and an adhesive such as water glass. A slurry is made with water, and foamed beads such as foamed polystyrene beads are mixed into this slurry as a cell structuring agent to form a molded body of a glass foaming agent and glass powder in which the foamed beads are uniformly dispersed.
この場合、ガラス発泡剤の混合割合は、ガラス
粉末100重量部に対して1〜10重量部の範囲が好
ましい。ガラス発泡剤がこの範囲以下では、次の
加熱工程において、気泡発生が充分に起らず、成
形体の断熱特性が低くなる傾向にある。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。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1〜10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、いずれの場合も注型等の作業が
やりにくくなる。 In this case, the mixing ratio of the glass blowing agent is preferably in the range of 1 to 10 parts by weight per 100 parts by weight of the glass powder. If the glass blowing agent is below this range, bubbles will not be sufficiently generated in the next heating step, and the heat insulating 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. 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 is low; on the other hand, above this range, the viscosity becomes high, and in either case, operations such as casting become difficult.
さらに気泡構成剤の混合割合は、ガラス粉末
100重量部に対して、2〜12重量部の範囲が好ま
しい。この混合割合が2重量部未満の場合には、
該発泡ビーズ気泡構成剤により形成される気泡が
少なく、発泡工程における発泡ガラスの体積増加
を吸収することが困難となる傾向にある。その結
果、ガラス発泡体の体積が増加するとともに、形
状のゆがみが大きくなる。混合割合が12重量部以
上の場合には、成形体中に大きな気泡が残溜し、
機械的強度、断熱特性が低下しやすい。 Furthermore, the mixing ratio of the cell structuring agent is
The range of 2 to 12 parts by weight per 100 parts by weight is preferred. If this mixing ratio is less than 2 parts by weight,
There are few bubbles formed by the foamed bead cell structuring agent, and it tends to be difficult to absorb the volume increase of the foamed glass in the foaming process. As a result, the volume of the glass foam increases and the shape becomes more distorted. If the mixing ratio is 12 parts by weight or more, large air bubbles will remain in the molded product.
Mechanical strength and heat insulation properties tend to decrease.
その後該成形体を気泡構成剤の分解温度以上、
例えば、ポリスチレン発泡ビーズの場合250℃程
度に加熱し、気泡構成剤としてのポリスチレン発
泡ビーズを分解除去する。気泡構成剤を消失させ
てガラス発泡剤とガラス粉末とで構成され、その
内部に多数の気泡を含有するグリーンコンパクト
とすることができる。尚、この方法においては、
気泡構成として、ポリスチレン発泡ビーズ以外に
粒状の発泡体例えば、ポリエチレン発泡体ビー
ズ、ポリウレタン発泡体小片等を使用できる。そ
の他特殊な場合には、もみ殻、パン屑等の有機質
を気泡構成剤として使用することができる。又、
ガラス発泡剤を含むガラス粉末の結合剤として
は、水ガラス以外に、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
ローズ(C.M.C)等の有機粘着剤、エポキシ樹脂
等の反応性接着剤を使用することができる。 Thereafter, the molded body is heated at a temperature higher than the decomposition temperature of the cell structuring agent.
For example, in the case of polystyrene foam beads, it is heated to about 250°C to decompose and remove the polystyrene foam beads as a cell structuring agent. By eliminating the cell forming agent, a green compact can be obtained which is composed of a glass blowing agent and glass powder and contains a large number of cells inside. Furthermore, in this method,
In addition to polystyrene foam beads, granular foams such as polyethylene foam beads, polyurethane foam pieces, etc. can be used as the cell structure. In other special cases, organic substances such as rice husks and bread crumbs can be used as a cell structuring agent. or,
In addition to water glass, polyvinyl alcohol,
Organic adhesives such as vinyl acetate emulsion, carboxymethyl cellulose (CMC), and reactive adhesives such as epoxy resins can be used.
グリーンコンパクトの他の製造方法としては、
プラスチツクスの押し出し発泡成形体の製造方法
のように、ガラス発泡剤とガラス粉末とを含む樹
脂押し出し成形体を気泡構成剤としての有機発泡
剤で発泡させ、内部に多数の気泡を含む発泡成形
体を製造し、その後、この成形体を加熱等の脱脂
工程により、樹脂を除き内部に多数の気泡を含む
ガラス発泡剤とガラス粉末とで構成されたグリー
ンコンパクトとすることができる。 Other methods of manufacturing green compacts include:
Like the manufacturing method of plastic extrusion foam molded products, a resin extrusion molded product containing a glass foaming agent and glass powder is foamed with an organic foaming agent as a cell structuring agent, thereby producing a foam molded product containing a large number of cells inside. is produced, and then this molded body is subjected to a degreasing process such as heating to remove the resin and form a green compact composed of a glass foaming agent containing many air bubbles inside and glass powder.
本発明でガラス発泡剤とは、ガラス粉末の軟化
温度で分解して炭酸ガス、酸素等を発生する炭酸
カルシウム、ドロマイト、等の無機化合物あるい
は、ガラスの軟化温度で燃焼して炭酸ガス等を発
生するカーボン粉末等を意味する。又、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ことが
できる。 In the present invention, a glass blowing agent is an inorganic compound such as calcium carbonate or dolomite that decomposes at the softening temperature of glass powder to generate carbon dioxide gas, oxygen, etc., or an inorganic compound such as calcium carbonate or dolomite that is combusted at the softening temperature of glass and generates carbon dioxide gas, etc. carbon powder, etc. Further, as the glass powder, ordinary soda lime glass, boric acid glass, and various other glass powders can be used.
ガラス発泡体を製造する工程は、上記のように
して得られたグリーンコンパクトをより高い温度
に加熱し、グリーンコンパクトを構成するガラス
粉末を軟化させるとともにガラス発泡剤を分解さ
せ発生するガスにより軟化したガラスを発泡さ
せ、ガラス粉末どうしを固着すると共に内部に微
細な気泡を含むガラス発泡体とするものである。
このとき発泡に伴ない、ガラスの見掛け体積は大
きくなり、グリーンコンパクトが有していた気泡
を埋めるので、ガラス発泡体の体積はグリーンコ
ンパクトのそれと比べてほとんど増加しない。 In the process of manufacturing glass foam, the green compact obtained as described above is heated to a higher temperature to soften the glass powder that makes up the green compact, and the glass foaming agent is decomposed and softened by the gas generated. This method involves foaming glass, fixing glass powder together, and creating a glass foam containing fine air bubbles inside.
At this time, as the foaming occurs, the apparent volume of the glass increases and fills the air bubbles contained in the green compact, so the volume of the glass foam hardly increases compared to that of the green compact.
尚、本発明で使用するガラス発泡剤及びガラス
粉末、更には、ガラス発泡体の加熱工程は、従来
のガラス発泡剤、ガラス粉末、加熱工程と、同一
でそのまま従来のものおよび方法を使用すること
ができる。具体的には、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、650〜800℃加熱
し、その後徐冷し、室温まで冷却してガラス発泡
体を製造する。 The glass blowing agent and glass powder used in the present invention, as well as the heating process for the glass foam, are the same as the conventional glass blowing agent, glass powder, and heating process, and conventional methods and methods can be used as they are. Can be done. Specifically, when soda lime glass is used as a glass powder, it is heated to 650 to 800°C, then gradually cooled, and then cooled to room temperature to produce a glass foam.
本発明の製造方法においては、ガラス発泡体を
製造するのに、金型を必要としない。尚、用途に
応じては金型を使用することもできる。かつ、ガ
ラス発泡体成形工程時のみかけ(外観上)の膨脹
は大きくない。このため、グリーンコンパクトと
ほぼ同一形状、大きさのガラス発泡体を製造する
ことができる。従つて、所定形状のガラス発泡体
を製造するために切り捨てるべき部分が非常に少
くなり収率が向上する。又、ガラス発泡体の製造
に当り、金型を使用しなくてもよいため、金型を
用いることによるガラス発泡体の割れ、あるい
は、金型の酸化、消耗といつた問題がなくなり、
製品の収率の向上、コストダウンが図られる。 In the manufacturing method of the present invention, no mold is required to manufacture the glass foam. Note that a mold can also be used depending on the purpose. Moreover, the apparent expansion (in terms of appearance) during the glass foam molding process is not large. Therefore, a glass foam having substantially the same shape and size as the green compact can be manufactured. Therefore, in order to produce a glass foam of a predetermined shape, the portion that must be cut away is greatly reduced, and the yield is improved. In addition, since there is no need to use a mold when manufacturing the glass foam, problems such as cracking of the glass foam, oxidation, and wear and tear of the mold due to the use of a mold are eliminated.
Improved product yield and reduced costs.
以下、実施例を説明する。 Examples will be described below.
実施例 1
通常のソーダ石灰ガラス廃品を洗浄乾燥し、こ
れを粗砕してガラス粉末とした。この、ガラス粉
末100重量部とガラス発泡剤としてドロマイト5
部を加え、更に微粉砕混合し、350メツシユ(網
目寸法44μm)全通となるような原料粉末混合体
を製造した。この混合体粉末に水50重量部、水ガ
ラス(JIS3号)5重量部、ポリビニールアルコー
ル5重量部を加えて攪拌し、スラリーを調製し
た。このスラリーに気泡構成剤として発泡ポリス
チレンビーズ(粒径約1ミリ見掛け密度0.048
g/c.c.)を3.6重量部加え十分に混練した。これ
を縦×横×高さが16×4×4cmの内寸法の凹部を
持つ金型に流し込み、室温で約24時間乾燥固化
し、縦×横×高さ=16×4×4cmの直方体状の成
形体を得た。更にその後、その成形体を乾燥機に
入れ、80℃で3時間乾燥した。次にこの成形体を
セラミツク板上に置き、ガス炉内に挿入し、1時
間に250℃の割合で加熱して、350℃とし、気泡構
成剤としての発泡ポリスチレンビーズを分解除去
することにより、ガラス発泡剤とガラス粉末とか
ら成り、内部に気泡を有するグリーンコンパクト
を得た。その後、同じガス炉中で1時間当り、
250℃の加熱速度で、750℃まで加熱し、1時間保
持後、1時間当り、30℃の冷却速度で徐冷し、本
発明におけるガラス発泡体を製造した。このガラ
ス発泡体の縦×横×高さが17.5×5×5.5cmであ
つた。これらの寸法は、グリーンコンパクトの寸
法に比べて、ほぼ等しかつた。又、このガラス発
泡体は0.5〜2mm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。このガラス発泡体の嵩密度は、0.114g/cm3
であり、圧縮強度は、8.1Kg/cm2(試料3個の平
均値)であつた。Example 1 Ordinary soda-lime glass waste was washed and dried, and it was coarsely crushed to obtain glass powder. 100 parts by weight of this glass powder and dolomite 5 as a glass foaming agent.
The mixture was further finely pulverized and mixed to produce a raw material powder mixture having a total mesh size of 350 meshes (mesh size 44 μm). To this powder mixture, 50 parts by weight of water, 5 parts by weight of water glass (JIS No. 3), and 5 parts by weight of polyvinyl alcohol were added and stirred to prepare a slurry. Add foamed polystyrene beads (particle size: approx. 1mm, apparent density: 0.048) to this slurry as a cell structuring agent.
3.6 parts by weight of (g/cc) were added and thoroughly kneaded. Pour this into a mold with a concave part with internal dimensions of 16 x 4 x 4 cm (length x width x height), dry and solidify at room temperature for about 24 hours, and form a rectangular parallelepiped with length x width x height = 16 x 4 x 4 cm. A molded body was obtained. Thereafter, the molded body was placed in a dryer and dried at 80°C for 3 hours. Next, this molded body was placed on a ceramic plate, inserted into a gas furnace, heated at a rate of 250°C per hour to 350°C, and the foamed polystyrene beads as a cell structuring agent were decomposed and removed. A green compact made of a glass blowing agent and glass powder and having air bubbles inside was obtained. After that, per hour in the same gas furnace,
The glass foam of the present invention was produced by heating to 750°C at a heating rate of 250°C, holding for 1 hour, and then slowly cooling at a cooling rate of 30°C per hour. The length x width x height of this glass foam was 17.5 x 5 x 5.5 cm. These dimensions were approximately equal compared to the dimensions of the green compact. Further, this glass foam was a closed cell glass foam in which closed cells of about 0.5 to 2 mm were uniformly dispersed almost throughout the interior. The bulk density of this glass foam is 0.114g/cm 3
The compressive strength was 8.1 Kg/cm 2 (average value of 3 samples).
実施例 2
実施例1のポリビニルアルコール5重量部に対
して、本実施例では、ポリビニルアルコールを
2.5重量部とし、更に実施例1の発泡ポリスチレ
ンビーズ3.6重量部に対して本実施例では、4.8重
量部とし、その他は、実施例1と全く同様にして
ガラス発泡体を製造した。得られたガラス発泡体
の寸法は、縦×横×高さが17×4.5×5cmでグリ
ーンコンパクトの寸法とほぼ同じであつた。又、
このガラス発泡体の内部には、0.3〜1.5mm程度の
独立気泡が内部までほぼ均一に分散していた。
又、本実施例のガラス発泡体の嵩密度は0.187
g/cm3、圧縮強度は25.7Kg/cm2(試料3個の平均
値)であつた。Example 2 In this example, polyvinyl alcohol was added to 5 parts by weight of polyvinyl alcohol in Example 1.
A glass foam was produced in exactly the same manner as in Example 1 except that the amount was 2.5 parts by weight, and 4.8 parts by weight in this example compared to 3.6 parts by weight of expanded polystyrene beads in Example 1. The dimensions of the obtained glass foam were 17 cm x 4.5 cm x 5 cm (length x width x height), which were almost the same as the dimensions of the green compact. or,
Closed cells of about 0.3 to 1.5 mm were almost uniformly dispersed inside this glass foam.
In addition, the bulk density of the glass foam of this example is 0.187
g/cm 3 , and the compressive strength was 25.7 Kg/cm 2 (average value of 3 samples).
実施例 3
実施例1のポリビニールアルコール5重量部に
対して、本実施例では、ポリビニールアルコール
1重量部、発泡ポリスチレンビーズ3.6重量部に
対して6重量部とし、他は実施例1と全く同様に
して、ガラス発泡体を製造した。得られたガラス
発泡体は、0.2〜1.2mmの独立気泡が均一に分散し
たものであつた。又、このガラス発泡体の嵩密度
は、0.203g/cm3であり、圧縮強度は、37.9Kg/
cm2(試料3個の平均値)であつた。Example 3 In this example, 1 part by weight of polyvinyl alcohol was added to 5 parts by weight of polyvinyl alcohol in Example 1, 6 parts by weight was added to 3.6 parts by weight of expanded polystyrene beads, and the other parts were the same as in Example 1. A glass foam was produced in the same manner. The obtained glass foam had closed cells of 0.2 to 1.2 mm uniformly dispersed therein. In addition, the bulk density of this glass foam is 0.203g/ cm3 , and the compressive strength is 37.9Kg/cm3.
cm 2 (average value of 3 samples).
実施例 4
実施例1のポリビニルアルコール5重量部に代
えて、酢酸ビニルエマルジヨン5.5重量部さらに、
ポリスチレンビーズ3.6重量部に対して、ポリス
チレンビーズ4.8重量部とし、他は実施例1と全
く同一にしてガラス発泡体を製造した。得られた
ガラス発泡体は、直径0.5〜2mmの独立気泡で、
ほぼ全体に均一に分散したものであつた。又、こ
のガラス発泡体の嵩密度は0.108g/cm3であり、
圧縮強度は、9.9Kg/cm2(試料3個の平均値)で
あつた。Example 4 In place of 5 parts by weight of polyvinyl alcohol in Example 1, 5.5 parts by weight of vinyl acetate emulsion,
A glass foam was produced in the same manner as in Example 1 except that 4.8 parts by weight of polystyrene beads were added to 3.6 parts by weight of polystyrene beads. The obtained glass foam has closed cells with a diameter of 0.5 to 2 mm.
It was dispersed almost uniformly throughout. In addition, the bulk density of this glass foam is 0.108 g/cm 3 ,
The compressive strength was 9.9 Kg/cm 2 (average value of 3 samples).
実施例 5
ホウ硅酸ガラス廃品を洗浄乾燥し、これを粗砕
してガラス粉末とした。このガラス粉末100重量
部とガラス発泡剤として炭酸カルシウム5重量部
を加えたのち、更に微紛砕、混合し、日本工業規
格標準篩350メツシユ(44μm)全通となるような
原料粉末混合体を製造した。この粉末混合体にガ
ラス粉末100重量部に体して水50重量部、水ガラ
ス(JIS3号)5重量部、カルボキシメチルセルロ
ース1重量部を加えて攪拌し、スラリーを調製し
た。このスラリーに気泡構成剤として発泡ポリス
チレンビーズ(粒径約1ミリ)をガラス粉末100
重量部に対して4.8重量部を加え十分に混練した。
これを縦×横×高さが16×4×4cmの内寸法を持
つ金型に流し込み、室温で約24時間乾燥、固化せ
しめ、縦×横×高さが16×4×4cmの直方体の成
形体を得た。更に、その後、該成形体を乾燥機に
入れ80℃で3時間乾燥した。次にこの成形体をセ
ラミツク板上に置き、ガス炉内に挿入し、1時間
に250℃の割合で加熱して、350℃とし、発泡ポリ
スチンビーズを分解除去し、ガラス発泡剤とガラ
ス粉末とよりなる成形体を得た。その後、更に1
時間当たり250℃の加熱速度で750℃まで加熱し5
分保持した後、1時間当たり30℃の冷却速度で徐
冷し、本発明におけ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17×5
×4.5cmであつた。この形状は成形体の寸法とほ
ぼ同一であつた。又、このガラス発泡体内部には
0.5〜1mm程度の独立気泡が均一に分散していた。
なお、このガラス発泡体の嵩密度は、0.199g/
cm3であり、圧縮強度は26.4Kg/cm2(試料3個の平
均値)であつた。従来のものより低密度、高強度
であつた。Example 5 Borosilicate glass waste was washed and dried, and it was coarsely crushed to obtain glass powder. After adding 100 parts by weight of this glass powder and 5 parts by weight of calcium carbonate as a glass foaming agent, they are further finely pulverized and mixed to obtain a raw material powder mixture that can pass through a Japanese Industrial Standards standard sieve of 350 mesh (44 μm). Manufactured. To this powder mixture, 100 parts by weight of glass powder, 50 parts by weight of water, 5 parts by weight of water glass (JIS No. 3), and 1 part by weight of carboxymethyl cellulose were added and stirred to prepare a slurry. Add 100% glass powder to this slurry and add expanded polystyrene beads (particle size: approx. 1mm) as a cell structuring agent.
4.8 parts by weight were added to the parts by weight and thoroughly kneaded.
Pour this into a mold with internal dimensions of 16 x 4 x 4 cm (length x width x height), dry and solidify at room temperature for about 24 hours, and form a rectangular parallelepiped with length x width x height of 16 x 4 x 4 cm. I got a body. Furthermore, after that, the molded body was placed in a dryer and dried at 80°C for 3 hours. Next, this molded body was placed on a ceramic plate, inserted into a gas furnace, heated at a rate of 250°C per hour to 350°C, the foamed polystine beads were decomposed and removed, and the glass foaming agent and glass powder were removed. A molded body was obtained. After that, 1 more
Heat to 750℃ at a heating rate of 250℃ per hour.
After being held for several minutes, it was slowly cooled at a cooling rate of 30° C. per hour to produce the glass foam of the present invention.
The dimensions of this glass foam are length x width x height 17 x 5
It was 4.5cm long. This shape was almost the same as the dimensions of the compact. Also, inside this glass foam,
Closed cells of about 0.5 to 1 mm were uniformly dispersed.
The bulk density of this glass foam is 0.199g/
cm 3 and the compressive strength was 26.4 Kg/cm 2 (average value of 3 samples). It had lower density and higher strength than the conventional one.
実施例 6
ソーゾ硅酸ガラス廃品を洗浄乾燥し、これを粗
砕してガラス粉末とした。このガラス粉末100重
量部とガラス発泡剤としてドロマイトを5重量部
加え、更に、微紛砕混合し、日本工業規格篩350
メツシユ(44μm)全通となるような原料粉末混
合体を製造した。この混合体粉末に水50重量部、
ポリビニルアルコール1部を加えて攪拌し、スラ
リーを調製した。このスラリーに気泡構成剤とし
て発泡ポリスチレンビーズ(粒径約1ミリ)6重
量部を加え十分に混練した。これを縦×横×高さ
が16×4×4cmの内寸法を持つ金型に流し込み、
室温で約24時間乾燥、固化し、縦×横×高さが16
×4×4cmの直方体の成形体を得た。更に、その
後、その成形体を乾燥機に入れ、80℃で3時間乾
燥した。次にこの成形体をセラミツク板上に置
き、ガス炉内に挿入し、1時間に250℃の割合で
加熱して、350℃とし、気泡構成剤としての発泡
ポリスチレンビーズを分解除去し、ガラス発泡剤
とガラス粉末とよりなる成形体を得た。その後、
同じガス炉内で1時間当たり250℃の加熱速度で
600℃まで加熱し、その温度で10分間保持した後、
1時間当たり30℃の冷却温度で徐冷し、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×高さがそれぞれ17×5×5cmであつた。この
寸法は成形体の寸法とほぼ等しかつた。又、この
ガラス発泡体内部には0.5〜1mm程度の独立気泡
が均一に分散していた。なお、このガラス発泡体
の嵩密度は0.201g/cm3であり、圧縮試験による
強度は28.5Kg/cm2(試料3個の平均値)であつ
た。Example 6 Sozo silicate glass waste was washed and dried, and it was crushed into glass powder. 100 parts by weight of this glass powder and 5 parts by weight of dolomite as a glass foaming agent were added, further finely pulverized and mixed, and passed through a Japanese Industrial Standard sieve 350.
A raw material powder mixture was produced that had a mesh size (44 μm). Add 50 parts by weight of water to this powder mixture.
1 part of polyvinyl alcohol was added and stirred to prepare a slurry. To this slurry, 6 parts by weight of expanded polystyrene beads (particle size: about 1 mm) were added as a cell structuring agent and thoroughly kneaded. Pour this into a mold with internal dimensions of 16 x 4 x 4 cm (length x width x height).
It dries and solidifies at room temperature for about 24 hours, and measures 16 mm in length x width x height.
A rectangular molded body measuring 4 cm x 4 cm was obtained. Furthermore, after that, the molded body was placed in a dryer and dried at 80°C for 3 hours. Next, this molded body was placed on a ceramic plate, inserted into a gas furnace, heated at a rate of 250°C per hour to 350°C, the foamed polystyrene beads as a cell structuring agent were decomposed and removed, and the glass foam was formed. A molded body consisting of the agent and glass powder was obtained. after that,
At a heating rate of 250 °C per hour in the same gas furnace
After heating to 600℃ and holding at that temperature for 10 minutes,
A glass foam was produced by slow cooling at a cooling temperature of 30°C per hour. The dimensions of this glass foam are length x
The width and height were 17 x 5 x 5 cm, respectively. This dimension was approximately equal to the dimension of the molded body. Moreover, closed cells of about 0.5 to 1 mm were uniformly dispersed inside this glass foam. The bulk density of this glass foam was 0.201 g/cm 3 , and the strength in the compression test was 28.5 Kg/cm 2 (average value of 3 samples).
Claims (1)
用い、該気泡構成剤を消失させることにより内部
に該ガラス発泡剤により膨脹する体積を吸収する
多数の気泡を含むグリーンコンパクトを作製する
予備成形工程と、 該グリーンコンパクトを加熱し、該ガラス発泡
剤を発泡させて該グリーンコンパクトの外形形状
を大きく変化させることなくガラス発泡体を形成
する発泡工程とからなることを特徴とするガラス
発泡体の製造方法。 2 前記予備成形工程は、ガラス発泡剤とガラス
粉末と結合剤を混合してスラリーを調製するスラ
リー工程と、該スラリーに気泡構成剤を混合して
該気泡構成剤が均一に分散した成形体を調製する
成形工程と、該成形体中の該気泡構成剤を消失さ
せる気泡形成工程とからなることを特徴とする特
許請求の範囲第1項記載のガラス発泡体の製造方
法。 3 前記予備成形工程は、ガラス発泡剤とガラス
粉末と発泡を含む樹脂との混合物を押出して押出
し成形体を形成する成形工程と、該押出し成形体
を有機発泡剤からなる気泡構成剤により発泡させ
内部に多数の気泡を形成する気泡形成工程と、気
泡を形成した成形体中の樹脂を除去する脱脂工程
とからなることを特徴とする特許請求の範囲第1
項記載のガラス発泡体の製造方法。[Claims] 1. A green compact that uses a glass foaming agent, glass powder, and a cell structuring agent, and contains a large number of cells that absorb the volume expanded by the glass foaming agent when the cell structuring agent disappears. and a foaming step of heating the green compact and foaming the glass foaming agent to form a glass foam without significantly changing the external shape of the green compact. A method for producing glass foam. 2 The preforming step includes a slurry step in which a glass foaming agent, glass powder, and a binder are mixed to prepare a slurry, and a cell structuring agent is mixed in the slurry to form a molded body in which the cell structuring agent is uniformly dispersed. 2. The method for producing a glass foam according to claim 1, comprising a forming step for preparing the foam and a cell forming step for eliminating the cell structuring agent in the molded object. 3. The preforming step includes a molding step of extruding a mixture of a glass blowing agent, glass powder, and a resin containing foam to form an extruded body, and a forming step of forming an extruded body by foaming the extruded body with a cell forming agent made of an organic blowing agent. Claim 1, characterized in that it consists of a bubble forming step of forming a large number of bubbles inside, and a degreasing step of removing the resin in the molded body in which the bubbles have been formed.
A method for producing a glass foam as described in Section 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20901582A JPS59102827A (en) | 1982-11-29 | 1982-11-29 | Glass foam manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20901582A JPS59102827A (en) | 1982-11-29 | 1982-11-29 | Glass foam manufacturing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59102827A JPS59102827A (en) | 1984-06-14 |
| JPH0216252B2 true JPH0216252B2 (en) | 1990-04-16 |
Family
ID=16565853
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20901582A Granted JPS59102827A (en) | 1982-11-29 | 1982-11-29 | Glass foam manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59102827A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2022102389A1 (en) | 2020-11-12 | 2022-05-19 | サンリット・シードリングス株式会社 | Plant seedling, seedling cultivation method, culture soil, and method of growing plant |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100733543B1 (en) | 2005-12-22 | 2007-06-29 | 재단법인 포항산업과학연구원 | Light insulation material manufacturing method using glass powder |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS52123412A (en) * | 1976-04-08 | 1977-10-17 | Toyoda Chuo Kenkyusho Kk | Method of glass foam |
| JPS577576A (en) * | 1980-06-16 | 1982-01-14 | Fujitsu Ltd | Method of measuring moving velocity by ultrasonic wave |
-
1982
- 1982-11-29 JP JP20901582A patent/JPS59102827A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2022102389A1 (en) | 2020-11-12 | 2022-05-19 | サンリット・シードリングス株式会社 | Plant seedling, seedling cultivation method, culture soil, and method of growing plant |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59102827A (en) | 1984-06-14 |
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