JPS5833805B2 - Continuous manufacturing method for glass fiber reinforced cement products - Google Patents

Continuous manufacturing method for glass fiber reinforced cement products

Info

Publication number
JPS5833805B2
JPS5833805B2 JP9253576A JP9253576A JPS5833805B2 JP S5833805 B2 JPS5833805 B2 JP S5833805B2 JP 9253576 A JP9253576 A JP 9253576A JP 9253576 A JP9253576 A JP 9253576A JP S5833805 B2 JPS5833805 B2 JP S5833805B2
Authority
JP
Japan
Prior art keywords
cement
slurry
glass fiber
fiber reinforced
reinforced cement
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
Application number
JP9253576A
Other languages
Japanese (ja)
Other versions
JPS5325619A (en
Inventor
健一 松井
京治 政元
保 赤坂
孝 曾田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Electric Works Co Ltd
Original Assignee
Matsushita Electric Works Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Works Ltd filed Critical Matsushita Electric Works Ltd
Priority to JP9253576A priority Critical patent/JPS5833805B2/en
Publication of JPS5325619A publication Critical patent/JPS5325619A/en
Publication of JPS5833805B2 publication Critical patent/JPS5833805B2/en
Expired legal-status Critical Current

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  • Curing Cements, Concrete, And Artificial Stone (AREA)

Description

【発明の詳細な説明】 本発明は、予めガラス繊維1を水酸化アル□ニウム又は
活性アルミナの少なくとも一方とセメント及び水と混合
分散せしめ、この繊維混入のスラリー2を多数の線状突
起3を有する回転ロール4にて連続移行している搬送シ
ート5上に飛散さぞてセメントマツトロを形威し所定厚
みに調整したのち、温度70〜180℃、湿度90〜1
00係の高温多湿の雰囲気下で養生することを特徴とす
るガラス繊維強化セメント製品の連続製造法に係り、そ
の目的とするところはガラス繊維による補強効果が高く
またセメントアルカリによる強度劣化が少ない上に連続
製造が容易に行なえるガラス繊維強化セメント製品の連
続製造法を提供するにある。
DETAILED DESCRIPTION OF THE INVENTION In the present invention, glass fibers 1 are mixed and dispersed in advance with at least one of aluminum hydroxide or activated alumina, cement, and water, and this fiber-containing slurry 2 is mixed with a large number of linear protrusions 3. Scattered onto the conveying sheet 5 that is continuously transferred by the rotating roll 4, the cement maturo is shaped and adjusted to a predetermined thickness, and then heated at a temperature of 70 to 180°C and a humidity of 90 to 1.
This is a continuous manufacturing method for glass fiber reinforced cement products, which is characterized by curing in a high temperature and humid atmosphere of 0.00 C. The purpose is to achieve a high reinforcing effect with glass fibers, less strength deterioration due to cement alkali, and The object of the present invention is to provide a continuous manufacturing method for glass fiber reinforced cement products that can be easily manufactured continuously.

従来、繊維強化セメント製品としてはパルプセメント板
、アスベストセメント板等が大量に製造され、その製造
方法も乾式、湿式等様々な方法で連続的にしかも合理的
に製造されていたが、最近特に注目を集めがいるのがガ
ラス繊維強化セメント製品である。
Traditionally, fiber-reinforced cement products such as pulp cement boards and asbestos cement boards have been manufactured in large quantities, and they have been manufactured continuously and rationally using various methods such as dry and wet methods, but recently, they have received particular attention. Glass fiber reinforced cement products are the most popular.

ガラス繊維強化セメント製品はその優れた機械的強度に
於いて有意性が認められている他、資源的にも天然に産
するアスベストのように資源の枯渇、品質のばらつきの
問題がなく、また一方、アスベストで問題にされている
公害の問題もないので、最近特に注目を集めているので
ある。
Glass fiber reinforced cement products are recognized for their excellent mechanical strength, and in terms of resources, unlike naturally occurring asbestos, there are no problems of resource depletion or quality variations; However, it has been attracting a lot of attention recently because it does not have the pollution problems associated with asbestos.

ところがガラス繊維がこのような有意性を有しているに
もかかわらず、未だセメント補強材として実用に供する
に至っていない原因には、筐ぜガラス繊維そのものがア
ルカリに侵蝕され易く、セメント製品に用いた場合、セ
メント硬化時にセメントから多量に析出してくる消石灰
により経時的に侵され、その補強効果が著しく減少する
ことと、もう1つは製造に関しその補強効果を充分に活
かし、しかも連続的に合理的に製造する方法が未だ開発
されていないからである。
However, despite the significance of glass fiber, it has not yet been put to practical use as a cement reinforcing material. If the cement hardens, it will be attacked over time by the slaked lime that precipitates in large quantities from the cement, and its reinforcing effect will significantly decrease. This is because a rational manufacturing method has not yet been developed.

このような上記の欠点を改良せんがために、例えばアル
カリによる侵蝕防止の手段として耐アルカリ性ガラス繊
維が開発されているが、それも普通ガラス繊維に比べ経
時的劣化が少ないだけであり、また會だ充分なものは開
発されておらず、また製造法に関しても連続して移行し
ているフェルト上にセメント、ガラス繊維等を固形原料
のまま散布し、それに水を散布してローラを経る方法、
又はセメントをスラリーとしそのスラリーとガラス繊維
とを同時に散布しなからローラを経て連続的にガラス繊
維強化セメント製品を製造する方法が提唱されているが
、これらの方法ではガラス繊維とセメントマトリックス
との馴じみ、即ち密着性が充分でなく、補強効果を充分
に発揮させることができなかった。
In order to improve the above-mentioned drawbacks, alkali-resistant glass fibers have been developed, for example, as a means of preventing corrosion by alkalis, but they only deteriorate less over time than ordinary glass fibers, and they also However, a satisfactory method has not yet been developed, and the manufacturing method is also undergoing continuous changes.
Alternatively, a method has been proposed in which cement is slurried and the slurry and glass fibers are simultaneously dispersed and then passed through rollers to continuously manufacture glass fiber reinforced cement products. The adhesion, that is, the adhesion was insufficient, and the reinforcing effect could not be fully exhibited.

本発明はとうした従来の欠点を改良せんがためになされ
たものであって、以下添付図に基づいて詳細に説明する
The present invention has been made to improve these conventional drawbacks, and will be described in detail below with reference to the accompanying drawings.

本発明はまず予めE−ガラス、C−ガラス等の普通のガ
ラス繊維1を繊維の切断が生じないように水酸化アルミ
ニウム或いは活性アル□すの少なくとも0万と水及び必
要とあらばその他の補強剤、充填剤、無機塩等に混入分
散せしめてガラス繊維含有のスラリー2を調整する。
In the present invention, ordinary glass fibers 1 such as E-glass and C-glass are first coated with at least 0,000 yen of aluminum hydroxide or activated aluminum, water, and other reinforcements if necessary to prevent the fibers from being cut. A glass fiber-containing slurry 2 is prepared by mixing and dispersing the slurry in agents, fillers, inorganic salts, etc.

ここでこの繊維混入のスラリー2の濃度は通常固形分百
分率で30〜60係が使用される。
Here, the concentration of the fiber-containing slurry 2 is usually 30 to 60 in solids percentage.

これは濃度が30%以下では飛散効果が悪くなり、筐た
混合スラリーと飛散スラリーとの組成が変わることもあ
り、また60係以上ではスラリーの流動性が失なわれ、
スラリー飛散装置内でスラリーレベルが不均一になり、
均一な厚みのセメント板が得られないからである。
This is because if the concentration is less than 30%, the scattering effect will be poor, and the composition of the mixed slurry in the casing and the scattered slurry may change, and if the concentration is more than 60%, the fluidity of the slurry will be lost.
The slurry level becomes uneven in the slurry scattering device,
This is because a cement board with a uniform thickness cannot be obtained.

またスラリー中の組成について説明すると、混入するガ
ラス繊維の配合量は七メン) 100重量部(以下部と
する)に対して30部以下が製造的には好まし0配合量
であり、その繊維の形もワール状でも2インチ以下のチ
ョップトストランド状でも良い。
In addition, to explain the composition of the slurry, the amount of glass fiber mixed in is 30 parts or less per 100 parts by weight (hereinafter referred to as parts), which is preferably 0 for manufacturing purposes, and the amount of glass fiber mixed in is 0. The shape may be a whirl shape or a chopped strand shape of 2 inches or less.

また補強材としてアスベスト繊維等を併用しても良い。Furthermore, asbestos fibers or the like may be used in combination as a reinforcing material.

用いるセメントの種類も特に限定するものではなく、普
通ポルトランドセメント、アルミナセメント、シリカセ
メント等を用い得る。
The type of cement used is not particularly limited either, and ordinary portland cement, alumina cement, silica cement, etc. can be used.

アルカリ固定、密着性増強の目的で添加する水酸化アル
ミニウム或いは活性アルミナの配合量も特に限定はしな
いが、普通ポルトランドセメントの場合であると、セメ
ント100部に対し5〜40部用いるのが好ましい。
The amount of aluminum hydroxide or activated alumina added for the purpose of fixing alkali and enhancing adhesion is not particularly limited, but in the case of ordinary Portland cement, it is preferably used in an amount of 5 to 40 parts per 100 parts of cement.

これは5部以下ではその効果が小さく、40部以上用い
てもその効果はもう上限でありむしろセメント成分が減
るために強度低下があり、あまり好ましくないからであ
る。
This is because the effect is small if it is less than 5 parts, and if it is used in excess of 40 parts, the effect is already at its upper limit and the strength decreases because the cement component is reduced, which is not very preferable.

またその粒径は150μ以下のものが、Ca(CH)2
固定の効果が犬であるので好ましい。
In addition, those with a particle size of 150μ or less are Ca(CH)2
Preferable because the fixed effect is dog.

更に必要に応じて加える無機塩はセメント水硬時に生成
するCa(CH)2と無定形シリカとの反応を促進する
効果があるものであって、アルカリ金属のハロゲン化物
、炭酸アルカリ、アルカリ土類金属の・・ロゲン化物、
水ガラスからなる群から選ばれた1種又は2種以上が用
いられるものであり、その使用量は例えばNaC2,或
いはCaCl2であればセメント100部に対し3部以
下でその効果を発揮する。
Furthermore, inorganic salts added as necessary have the effect of promoting the reaction between Ca(CH)2 generated during cement hydraulic hardening and amorphous silica, and include alkali metal halides, alkali carbonates, and alkaline earth salts. Metal...logenides,
One or more types selected from the group consisting of water glasses are used, and the amount used is, for example, NaC2 or CaCl2, 3 parts or less per 100 parts of cement to achieve its effect.

しかして上述のように調製されたガラス繊維含有のスラ
リー2は任意の手段、例えば第1図のように供給パイプ
1にて飛散装置の第1貯部8に送られ、オーバーフロー
して第2貯部9に供給される。
The glass fiber-containing slurry 2 prepared as described above is then fed to the first reservoir 8 of the scattering device by any means, for example the supply pipe 1 as shown in FIG. 9.

第2貯部9には多数の線状突起3を有する回転ロール4
がスラリー2の液面に下部が浸漬され上部に邪魔板10
が侵入する如く設けられて、回転ロール4が回転すると
この回転ロール4に付着したガラス繊維含有のスラリー
2が邪魔板10と回転ロール40回転力により飛散して
、移動するフェルト、金網等の搬送シート5上に載置さ
れる。
A rotating roll 4 having a large number of linear protrusions 3 is provided in the second storage part 9.
The bottom part is immersed in the liquid level of slurry 2, and the baffle plate 10 is placed in the top part.
When the rotary roll 4 rotates, the glass fiber-containing slurry 2 adhering to the rotary roll 4 is scattered by the rotational force of the baffle plate 10 and the rotary roll 40, and the conveyance of moving felt, wire mesh, etc. It is placed on the sheet 5.

ここでスラリー2の飛散量はスラリー2内に浸漬してい
る線状突起3の長さと回転数及び邪魔板10の線状突起
3内への侵入度及び搬送シート5の速度で決定される。
Here, the amount of scattering of the slurry 2 is determined by the length and rotational speed of the linear protrusions 3 immersed in the slurry 2, the degree of penetration of the baffle plate 10 into the linear protrusions 3, and the speed of the conveyance sheet 5.

線状突起3の形状、種類は特に限定するものでなく、要
は原料のスラリー2を回転ロール4の回転時にすくい上
げ、回転ロール4の回転力と、邪魔板10の力で飛散さ
せることが可能であればよい。
The shape and type of the linear protrusions 3 are not particularly limited; in short, it is possible to scoop up the raw material slurry 2 when the rotating roll 4 rotates and scatter it using the rotational force of the rotating roll 4 and the force of the baffle plate 10. That's fine.

したがって通常、線状突起3の材質は金属(例えばステ
ンレスなど)又はナイロン等が用いられ、またその形状
は0.1〜2.0閣の径の針状物を用いる。
Therefore, the material of the linear protrusion 3 is usually metal (for example, stainless steel) or nylon, and the linear protrusion 3 is shaped like a needle with a diameter of 0.1 to 2.0 mm.

また飛散装置までのスラリーの輸送方法は特に限定しな
いが、通常 状のところを流し移送するのが好ましい。
The method of transporting the slurry to the scattering device is not particularly limited, but it is preferable to transport the slurry by flowing it in a normal state.

飛散したスラリーを受はマットを形成する移動式の搬送
シート5は普通一般のコンベアを用い、その上にフェル
ト又は網目の小さい金網を張ったものであればよい。
The movable conveyance sheet 5 for receiving the scattered slurry and forming a mat may be a general conveyor, and a sheet of felt or a small wire mesh stretched over the conveyor may be used.

昔た飛散して層状となったスラリーの流れ防止のために
フェルトの裏面にサクションボックス11を設置して吸
引脱水する方法又は上部に脱水用ロールを設けて絞る方
法等がとられる。
In order to prevent the slurry that has been scattered and formed into a layer from flowing, a suction box 11 is installed on the back of the felt to perform suction dewatering, or a dewatering roll is installed on the top of the felt to squeeze it out.

次いで一対のならしロール13にてゼメントマット6を
一定の厚みに調整する。
Next, the cement mat 6 is adjusted to a constant thickness using a pair of leveling rolls 13.

この場合、セメントマツトロの厚みを厚くする場合には
第2図のように複数個の飛散装置を列設したり、或いは
第3図のようにメーキングロール12に巻付けて一定の
厚さに達した時点でカッティングするようにすることも
できる。
In this case, if you want to increase the thickness of the cement matsuro, you can install multiple scattering devices in a row as shown in Figure 2, or wrap it around a making roll 12 as shown in Figure 3 to keep it at a constant thickness. It is also possible to cut when the target is reached.

以上で得られたガラス繊維強化セメン・トシートをその
ま普あるいは加圧、打ち抜き等により所定の寸法、形に
し、その後70〜180℃、好ましくは80〜100℃
の高温でかつ90〜100%の多湿下で2〜50時間湿
熱養生を行なって製品が得られる。
The glass fiber-reinforced cement sheet obtained above is made into a predetermined size and shape as is or by pressurization, punching, etc., and then heated to a temperature of 70 to 180°C, preferably 80 to 100°C.
The product is obtained by performing moist heat curing for 2 to 50 hours at a high temperature of 90% to 100% and high humidity of 90% to 100%.

ここで養生の湿度を70−180℃としたのは70℃以
下ではセメント水硬時に析出したCa、CH2の活性ア
ルミナ又は水酸化アル□ニウムによる固定が充分に行な
われず、筐た180℃以上ではセメント硬化物が熱劣化
しやすいために不都合であり、また養生を多湿下で行な
うのはセメントの水硬反応をスムーズに行なわせるため
である。
The reason why the curing humidity was set at 70-180℃ is that below 70℃, Ca and CH2 precipitated during cement hydraulic hardening are not sufficiently fixed by activated alumina or aluminum hydroxide. This is inconvenient because the hardened cement product is susceptible to thermal deterioration, and the reason why curing is performed under high humidity is to allow the hydraulic reaction of the cement to occur smoothly.

本発明にあっては上述のように予めガラス繊維をセメン
トと水に混入して分散ぞしめガラス繊維混入セメントス
ラリーを調製しているからガラス繊維とセメントマトリ
ックスとの馴じみ、即ち密着性が良好となるものであり
、しかもスラリー中に活性アルミナ又は水酸化アル□ニ
ウムノ少すくとも一方を配合し高温多湿下での養生に供
しているからセメント硬化時に析出してくる消石灰を固
定し、セメント製品そのものの中性化をはかり、ガラス
繊維のアルカリによる侵蝕を防止するばかりでなく、活
性アル□す又は水酸化アルミニウムの少なくとも一方を
配合したことにより生成する生成物の働きでガラス表面
とセメントマツトロとの馴じみを更に強いものにするこ
とができるものであって、ガラス繊維の強度の劣化を防
止しかつガラス繊維とセメントマトリックスとの密着性
を向上させて長期に亘りガラス繊維による大きな補強効
果を確実に発揮せしめ得る利点がある。
In the present invention, as described above, glass fibers are mixed in cement and water in advance and dispersed to prepare a glass fiber-containing cement slurry, so that the glass fibers and the cement matrix are compatible, that is, have good adhesion. Moreover, since the slurry contains at least one of activated alumina or aluminum hydroxide and is cured under high temperature and humidity, the slaked lime that precipitates during cement hardening is fixed, and cement products are produced. This not only neutralizes glass fibers and prevents them from being corroded by alkali, but also strengthens the glass surface and cement matte coating by the action of the products produced by blending at least one of activated aluminum and aluminum hydroxide. It prevents the deterioration of the strength of the glass fibers and improves the adhesion between the glass fibers and the cement matrix, resulting in a large reinforcing effect by the glass fibers over a long period of time. This has the advantage of ensuring that the

またガラス繊維混入スラリーを多数の線状突起を有する
回転式ロールにて飛散させることにより繊維混入スラリ
ーの組成を混練時と変えることなく、しかも連続的に移
行している搬送シート上に均一に散布することが可能と
なったので、長期的に強度の安定したしかも板厚の選択
も自由な連続的かつ合理的ガラス繊維強化セメント製品
の製造法を提供し得る利点がある。
In addition, by scattering the glass fiber-mixed slurry with a rotating roll having many linear protrusions, the composition of the fiber-mixed slurry does not change from that during kneading, and moreover, it is evenly distributed on the continuously moving conveyor sheet. This has the advantage of providing a continuous and rational manufacturing method for glass fiber-reinforced cement products that have stable strength over a long period of time and also allow for free selection of plate thickness.

またこの際線状突起を有する回転ロールの回転力により
スラリーを飛散サセて搬送シート上に敷き詰めるために
ガラス繊維の方向性に偏りがなくなり強度的にばらつき
の少ないガラス繊維強化セメント製品を得ることができ
るものであり、この製造方法で得られたセメント製品は
長期間高強度を維持したしかもセメント製品にありがち
な白化現象、即ちエフロレッセンスの発生を防止したす
ぐれた強化セメント製品がある。
In addition, since the slurry is scattered and spread on the conveying sheet by the rotational force of a rotating roll having linear protrusions, there is no bias in the directionality of the glass fibers, making it possible to obtain glass fiber reinforced cement products with less variation in strength. The cement products obtained by this manufacturing method maintain high strength for a long period of time, and are excellent reinforced cement products that prevent the occurrence of whitening phenomenon, that is, efflorescence, which is common in cement products.

以下本発明を実施は基づいて具体的に説明する。The present invention will be specifically explained below based on its implementation.

実施例1〜4及び比較例 第3図に示した装置で下表に示した配合組成のガラス繊
維含有のスラリーを散布し、板厚が6關のシートをメー
キングロールに巻きとった。
Examples 1 to 4 and Comparative Examples A glass fiber-containing slurry having the composition shown in the table below was spread using the apparatus shown in FIG. 3, and a sheet having a thickness of 6 mm was wound onto a making roll.

この時使用した装置の回転ロールの線状突起は直径が0
.5mmのステンレス製針金を使用し、その回転ロール
は直径が200mm、スラリー液筒への侵入深さが15
mm、邪魔板への侵入深さが5閣、回転数が150 r
pmであり、また下部移動コンベアにエルトを使用し、
コンベアスピードを20m/分、サクションボックスで
の減圧度を30 K9/crAとした。
The linear protrusion of the rotating roll of the device used at this time had a diameter of 0.
.. A 5mm stainless steel wire is used, and the rotating roll has a diameter of 200mm and a penetration depth of 15mm into the slurry cylinder.
mm, penetration depth into the baffle plate is 5 mm, rotation speed is 150 r
pm, and also uses Elt for the lower moving conveyor,
The conveyor speed was 20 m/min, and the degree of vacuum in the suction box was 30 K9/crA.

こうしてメーキングロールに巻き取ったものを20 K
g/crrfで加圧成形したのち、80℃で36時間湿
熱養生を行なった。
The material wound on the making roll in this way is 20K.
After pressure molding at g/crrf, moist heat curing was performed at 80° C. for 36 hours.

尚、比較例については自然養生を3週間行なった。In addition, for the comparative example, natural curing was performed for 3 weeks.

それぞれの硬化シートについて曲げ強度と衝撃強度の経
時変化を調べたところ、各々第4図、第5図に示す結果
が得られた。
When the bending strength and impact strength of each cured sheet were examined for changes over time, the results shown in FIGS. 4 and 5, respectively, were obtained.

曾た同時に屋外にこの実施例1〜4及び比較例による5
試料を曝露し、エフロレッセンスの発生状況も調べた。
At the same time, these Examples 1 to 4 and Comparative Example 5 were placed outdoors.
The samples were exposed and the occurrence of efflorescence was also investigated.

その結果、比較例については約1箇月で白化したのに対
し、実施例1〜4はいずれも2年経過したのちも未だエ
フロレッセンスの現象ばみられないものであった。
As a result, whitening occurred in the comparative example in about one month, whereas no efflorescence phenomenon was observed in any of Examples 1 to 4 even after two years had passed.

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

第1図は本発明のスラリー飛散工程の一実施例の概略断
面図、第2図は同上工程の他の実施例の概略断面図、第
3図は同上のメーキングロールへの取き取り工程の斜視
図、第4図と第5図は本発明の実施例1〜4及び比較例
により得られた製品の曲げ強度及びシャルピー衝撃強度
の経時変化特性図であって、1はガラス繊維、2ぽスラ
リー、3は線状突起、4は回転ロール、5は搬送シート
、6はセメントマットを示す。
Fig. 1 is a schematic sectional view of one embodiment of the slurry scattering process of the present invention, Fig. 2 is a schematic sectional view of another embodiment of the same process, and Fig. 3 is a schematic sectional view of another embodiment of the slurry scattering process of the present invention. The perspective view and FIGS. 4 and 5 are graphs showing the temporal change characteristics of the bending strength and Charpy impact strength of products obtained in Examples 1 to 4 of the present invention and comparative examples, in which 1 is a glass fiber, 2 is a glass fiber, and 2 is a glass fiber. Slurry, 3 is a linear protrusion, 4 is a rotating roll, 5 is a conveyance sheet, and 6 is a cement mat.

Claims (1)

【特許請求の範囲】 1 予めガラス繊維を水酸化アルミニウム又は活性アル
ミナの少なくとも一方とセメント及び水と混合分散せし
め、この繊維混入のスラリーを多数の線状突起を有する
回転ロールにて連続移行している搬送シート上に飛散す
せてセメントマットを形成し所定厚みに調整したのち、
温度70〜180℃、湿度90〜100係の高温多湿の
雰囲気下で養生することを特徴とするガラス繊維強化セ
メント製品の連続製造法。 2 スラリーにアルカリ金属の・・ロゲン化物、炭酸ア
ルカリ、アルカリ土類金属の−・ロゲン化物、水ガラス
からなる群から選ばれた1種又は2種以上の無機塩を配
合したことを特徴とする特許請求範囲第1項記載のガラ
ス繊維強化セメント製品の連続製造法。
[Claims] 1 Glass fibers are mixed and dispersed in advance with at least one of aluminum hydroxide or activated alumina, cement and water, and this fiber-containing slurry is continuously transferred using a rotating roll having a large number of linear protrusions. After scattering onto a conveyor sheet to form a cement mat and adjusting it to a specified thickness,
A method for continuous production of glass fiber reinforced cement products, characterized by curing in a high temperature and high humidity atmosphere with a temperature of 70 to 180°C and a humidity of 90 to 100°C. 2 The slurry is characterized by containing one or more inorganic salts selected from the group consisting of alkali metal halides, alkali carbonates, alkaline earth metal halogenides, and water glass. A method for continuously manufacturing a glass fiber reinforced cement product according to claim 1.
JP9253576A 1976-07-31 1976-07-31 Continuous manufacturing method for glass fiber reinforced cement products Expired JPS5833805B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9253576A JPS5833805B2 (en) 1976-07-31 1976-07-31 Continuous manufacturing method for glass fiber reinforced cement products

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9253576A JPS5833805B2 (en) 1976-07-31 1976-07-31 Continuous manufacturing method for glass fiber reinforced cement products

Publications (2)

Publication Number Publication Date
JPS5325619A JPS5325619A (en) 1978-03-09
JPS5833805B2 true JPS5833805B2 (en) 1983-07-22

Family

ID=14057049

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9253576A Expired JPS5833805B2 (en) 1976-07-31 1976-07-31 Continuous manufacturing method for glass fiber reinforced cement products

Country Status (1)

Country Link
JP (1) JPS5833805B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
LU81915A1 (en) * 1979-11-19 1981-06-04 Lafarge Sa NEW APPLICATION OF PORTLAND CEMENTS AND THE BINDERS THUS OBTAINED
JPS58167459A (en) * 1982-03-24 1983-10-03 日本セメント株式会社 Manufacture of cement board

Also Published As

Publication number Publication date
JPS5325619A (en) 1978-03-09

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