JPS6029602B2 - Manufacturing method of glass fiber reinforced cement board - Google Patents
Manufacturing method of glass fiber reinforced cement boardInfo
- Publication number
- JPS6029602B2 JPS6029602B2 JP5018477A JP5018477A JPS6029602B2 JP S6029602 B2 JPS6029602 B2 JP S6029602B2 JP 5018477 A JP5018477 A JP 5018477A JP 5018477 A JP5018477 A JP 5018477A JP S6029602 B2 JPS6029602 B2 JP S6029602B2
- Authority
- JP
- Japan
- Prior art keywords
- cement
- slurry
- glass fiber
- fiber
- mesh
- 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
Links
- 239000004568 cement Substances 0.000 title claims description 42
- 239000003365 glass fiber Substances 0.000 title claims description 24
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- 239000002002 slurry Substances 0.000 claims description 37
- 239000000835 fiber Substances 0.000 claims description 22
- 238000000034 method Methods 0.000 claims description 17
- 239000011521 glass Substances 0.000 claims description 2
- 238000010030 laminating Methods 0.000 claims description 2
- 239000010425 asbestos Substances 0.000 description 11
- 229910052895 riebeckite Inorganic materials 0.000 description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 239000000203 mixture Substances 0.000 description 4
- 239000012779 reinforcing material Substances 0.000 description 4
- 239000003513 alkali Substances 0.000 description 3
- -1 and if necessary Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 240000002869 Tristellateia australasiae Species 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 230000005021 gait Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Landscapes
- Producing Shaped Articles From Materials (AREA)
Description
【発明の詳細な説明】
本発明はセメントが含まれないガラス繊維配合の繊維ス
ラリー1と、ガラス繊維が含まれないセメントスラリ−
2とを時間的に相前後して抄造し積層することを特徴と
するガラス繊維強化セメント板の製造方法に係り、その
目的とするところはガラス繊維を補強材として歩留りよ
く強化セメント板を得ることができるガラス繊維強化セ
メント板の製造方法を提供するにある。DETAILED DESCRIPTION OF THE INVENTION The present invention provides fiber slurry 1 containing glass fibers containing no cement, and a cement slurry containing no glass fibers.
The method for manufacturing a glass fiber reinforced cement board is characterized by paper-forming and laminating 2 and 2 sequentially in time, and its purpose is to obtain a reinforced cement board with a good yield using glass fiber as a reinforcing material. The purpose of the present invention is to provide a method for manufacturing a glass fiber reinforced cement board.
最近、ァスベストセメント板の製造に於いてアスベスト
の公害問題、資源枯渇による入手鍵等の理由によりアス
ベストの代替繊維としてガラス繊維を補強材として使用
したガラス繊維強化セメント板(CRC板)の研究、開
発がさかんであり、また将釆的にも有望であるが、その
製造方法としては通常、次のようなものがある。Recently, in the production of asbestos cement boards, research has been conducted on glass fiber reinforced cement boards (CRC boards) that use glass fiber as a reinforcing material as an alternative fiber to asbestos due to the problem of asbestos pollution and the difficulty in obtaining keys due to resource depletion. , which is currently under active development and has a promising future, is usually produced using the following methods.
(1)ダイレクトスプレー法
スプレー脱水法
(0) 法型法
(m)押出法
(N) 湿式抄造法
これらの方法の中では(1)の方法が最も広く採用され
ているが、この方法は最大の欠点として生産スピードが
遅く、生産性が上らないために大量生産に向かない点が
ある。(1) Direct spray method Spray dehydration method (0) Method method (m) Extrusion method (N) Wet papermaking method Among these methods, method (1) is the most widely adopted; The drawback is that the production speed is slow and productivity is not high, making it unsuitable for mass production.
また(0)の方法も現場作業向きではあるが、生産性が
悪く、また強度が発現しにくい等の欠点がある。(m)
の方法も生産性が低く、実用化されている例は少ない。
(W)の方法はハチェック法とも呼ばれるもので、これ
らの中では一番生産性に優れていて工場生産向きであり
、最近特に種々研究、検討されてきているが、セメント
とガラス繊維だけの配合では歩蟹り及び分散性が悪く、
抄造できない問題点がある。即ち、繊維としてGFの他
にアスベストを同時に配合し、必要であればパルプ等の
繊維を配合し、セメントと混合して抄造する。これはア
スベスト、パルプを配合することによりセメント粒子を
アスベスト、パルプの表面上に吸着させて抄造し、セメ
ントの歩留りを向上させるのであるが、この方法に於い
ては繊維が全配合の固型分に対して約1の重量%以上含
有されており、かつアスベスト単独、若しくはアスベス
ト十パルプの量が少なくとも4重量%以上含有されてい
る必要があって、アスベストを全く0にすることはでき
ない。つまり前述の如くアスベストの量が4重量%以下
になると、炉過スピードが遠く、セメントの歩留りが悪
くなるからである。本発明はかかる従釆の欠点を解消せ
んとするもので、以下添付図面に基いて詳細に説明する
。Method (0) is also suitable for on-site work, but has drawbacks such as poor productivity and difficulty in developing strength. (m)
This method also has low productivity, and there are few examples of it being put into practical use.
Method (W) is also called the Hatschek method, which has the highest productivity among these and is suitable for factory production, and has recently been studied and examined in various ways. The formulation has poor dispersibility and
There is a problem that papermaking is not possible. That is, in addition to GF, asbestos is simultaneously blended as fibers, and if necessary, fibers such as pulp are blended, and the mixture is mixed with cement to form paper. In this method, by blending asbestos and pulp, cement particles are adsorbed onto the surface of the asbestos and pulp to improve the yield of cement. It is necessary to contain at least about 1% by weight or more of asbestos alone or at least 4% by weight of asbestos pulp, and it is impossible to completely eliminate asbestos. In other words, as mentioned above, if the amount of asbestos is less than 4% by weight, the furnace overspeed will be slow and the yield of cement will be poor. The present invention aims to eliminate the drawbacks of such a conventional system, and will be described in detail below with reference to the accompanying drawings.
本発明の最大の特徴は湿式(ハチヱック)抄造装置を使
用してガラス繊維強化セメント板を製造する際に、ガラ
ス繊維とセメントをそれぞれ別個のスラリーバットで沙
上げることにある。添付図は湿式(ハチェック)抄造装
置の一例を示すもので、任意の複数個のバット3a,.
3b…のいくつかの中にガラス繊維と水及び必要に応じ
て界面活性剤が配合された液、つまり繊維スラリー1を
投入し、残りにセメントと水及びパルプ等が配合された
セメントスラリー2を投入する。図示例ではバット3a
,3b,3cの3個を用い、第1番目と第3番目のバッ
ト3a,3cに繊維スラリー1を投入すると共に第2番
目のバット3bにセメントスラリ−2を投入してある。
この際、繊維スラリーーが投入されているバット3a,
3cの抄上げシリンダ4a,4cの網目は通常のハチェ
ックマシーンで使用される50〜6oメッシュでよいが
、セメントスラリー2のバッニト3bの秒上げシリンダ
4bの網目はこれよりも細かく、80〜100メッシュ
程度の範囲とする。また繊維スラリー1の濃度(ガラス
繊維の含有量)は任意であるが、セメントスラリー2の
パルプ含有量はセメント及び繊維類の全固形分使用量1
0の重量部に対し1〜4重量部とする。更に繊維スラリ
ー1におけるガラス繊維の配合量は上記の通り任意であ
って、限定するものではないが、0.1〜5重量%程度
がよい。またガラス繊維の種類はチョップストランド、
ウ−ル状のいずれでもよく、繊維の長さも任意であるが
・チョップドストランドの場合では通常1/4〜2イン
チ程度が好ましい。また、ガラスの組成の種類も耐アル
カリガラス繊維、E−ガラス繊維、Cーガラス繊維等の
いずれでもよいが、セメントの補強材としては耐アリカ
リガラス繊維が最も好ましい。ここで上記セメントスラ
リー2に於けるパルプの含有率を1〜4重量%としたの
は、これが4%以上になると最終製品の不燃性に於いて
問題があり、また1%以下であるとセメントの歩蟹りが
極端に悪くなるからである。またセメントスラリー2用
の抄上げシリンダ4bの網目を80〜100メッシュと
したのは、100メッシュ以上の細かい網目になると、
セメントの歩留りは向上するが、炉水性が悪くなり、8
0メッシュ以下の大きな網目になると、パルプの含有率
が1〜4重量%のセメントスラリー2ではセメントの歩
留りが悪くなるからである。しかして図示例の場合では
まず第1番目のバット3a内の繊維スラリー1が抄上げ
シリンダ4aにて抄上げられ炉過されてエンドレス状の
フェルト5上に秦移り、次に第2番目のバット3b内の
セメントスラリ−2が抄上げシリンダ4bにて抄上げら
れ炉過されて前記のガラス繊維の抄上げられたウェット
マット上に秦移り、更に第3番目のバット3c内の繊維
スラリー1が抄上げシリンダ4cにて妙上げられ炉過さ
れて第2層目のセメント層の上に秦移る。The most important feature of the present invention is that when manufacturing a glass fiber reinforced cement board using a wet papermaking device, glass fibers and cement are pumped up in separate slurry vats. The attached figure shows an example of a wet (Hacheck) papermaking apparatus, in which any number of vats 3a, .
A liquid containing glass fibers, water, and a surfactant if necessary, that is, fiber slurry 1, is poured into some of 3b..., and the rest is cement slurry 2, which is a mixture of cement, water, pulp, etc. throw into. In the illustrated example, the bat 3a
, 3b, 3c are used, and the fiber slurry 1 is charged into the first and third vats 3a, 3c, and the cement slurry 2 is charged into the second vat 3b.
At this time, the vat 3a into which the fiber slurry is charged,
The mesh of the lifting cylinders 4a and 4c of 3c may be 50 to 6o mesh, which is used in a normal hacheck machine, but the mesh of the second raising cylinder 4b of the bagnit 3b of cement slurry 2 is finer than this, and is 80 to 100 mesh. The range should be about the size of a mesh. In addition, the concentration of fiber slurry 1 (glass fiber content) is arbitrary, but the pulp content of cement slurry 2 is the total solid content of cement and fibers used.
The amount is 1 to 4 parts by weight relative to 0 parts by weight. Furthermore, the blending amount of glass fibers in the fiber slurry 1 is arbitrary as described above and is not limited, but is preferably about 0.1 to 5% by weight. In addition, the types of glass fiber are chopped strand,
Any wool-like fiber may be used, and the length of the fibers may be arbitrary; however, in the case of chopped strands, the preferred length is usually about 1/4 to 2 inches. Further, the composition of the glass may be any of alkali-resistant glass fibers, E-glass fibers, C-glass fibers, etc., but alkali-resistant glass fibers are most preferred as reinforcing materials for cement. Here, the content of pulp in the cement slurry 2 is set at 1 to 4% by weight because if it exceeds 4%, there will be a problem in the non-flammability of the final product, and if it is below 1%, the content of pulp in the cement slurry 2 will be 1 to 4% by weight. This is because the gait becomes extremely poor. In addition, the reason why the mesh of the drawing cylinder 4b for the cement slurry 2 is set to 80 to 100 mesh is because the mesh is finer than 100 mesh.
Cement yield improves, but reactor water resistance deteriorates and
This is because if the mesh size is 0 mesh or less, the yield of cement will be poor in cement slurry 2 with a pulp content of 1 to 4% by weight. In the case of the illustrated example, the fiber slurry 1 in the first vat 3a is first drawn up in the drawing cylinder 4a, passed through a furnace, and transferred onto the endless felt 5, and then transferred to the second vat 3a. The cement slurry 2 in the third vat 3b is drawn up in the drawing cylinder 4b, passed through a furnace, and transferred onto the wet mat made of glass fibers, and the fiber slurry 1 in the third vat 3c is The material is polished in the papermaking cylinder 4c, passed through a furnace, and transferred onto the second cement layer.
これらの各々の秦移りの際にそれぞれコーチロール6a
,6b,6cにて加圧され、また乗移り後はサクション
ボックス7a,7b,7cにて脱水される。そして以後
は通常のハチェック抄造法と同様にメーキングロール8
に巻取り、所定の厚みになった時点で切断し、必要に応
じてプレス成形、養生等の後加工に供される。図中9は
ボトムロールである。尚、繊維スラリー1とセメントス
ラリー2の抄上げの順序及び抄上げ数は上記例以外に任
意に設定できる。本発明にあっては上記のように繊維ス
ラリーとセメントスラリーとを時間的に相前後して沙造
し積層するようにしているから、両スラリーの濃度、抄
上げシリンダの網目等を互いに他より独立して別個の最
適値に設定することができ、殊にセメントスラリーの条
件を繊維スラリーと拘りなく最適条件に容易に設定でき
るものであって、従来のようにスラス川こアスベストを
配合する必要もなく、ガラス繊維を補強材とした不燃性
の強化セメント板をセメントの歩蟹りよく連続して得る
ことができる利点がある。以下本発明を実施例に基づい
て具体的に説明する。At the time of each of these Qin transfers, the coach roll 6a
, 6b, 6c, and after transfer, water is dehydrated in suction boxes 7a, 7b, 7c. From then on, the making roll 8 is made in the same way as in the normal Hatchek papermaking method.
It is wound up, cut when it reaches a predetermined thickness, and subjected to post-processing such as press molding and curing as necessary. 9 in the figure is the bottom roll. Incidentally, the order of making up the fiber slurry 1 and the cement slurry 2 and the number of making up can be arbitrarily set other than the above example. In the present invention, as mentioned above, the fiber slurry and the cement slurry are sanded and laminated at different times, so the concentrations of the two slurries, the mesh of the sanding cylinder, etc. are different from each other. It is possible to independently set the optimum value, and in particular, it is easy to set the conditions of the cement slurry to the optimum condition regardless of the fiber slurry, and there is no need to mix asbestos in the slurry as in the past. There is an advantage that a non-combustible reinforced cement board using glass fiber as a reinforcing material can be obtained continuously at the same pace as the cement. The present invention will be specifically described below based on examples.
添付図に示すハチェック抄造機を用い、第1及び第3の
バット3a,3cに0.5重量%の耐アルカリガラス繊
維を含有しかつ界面活性剤が1%配合された水、つまり
繊維スラリ−1を投入した。Using the Hacheck paper machine shown in the attached diagram, water containing 0.5% by weight of alkali-resistant glass fibers and 1% of a surfactant, that is, fiber slurry, was added to the first and third batts 3a and 3c. -1 was inserted.
他方第2番目のバット3bには普通ボルトランドセメン
ト及びパルプの岡型分重量比が聡:2でかつ水と混合し
たスラリー濃度が10%のセメントスラリ‐2を投入し
た。またバット3a+3cの繊維スラリ−1内の抄上げ
シリンダ4a,4cの絹目を60メッシュとすると共に
、バット3bのセメントスラリー2内の抄上げシリング
4bの網目を100メッシュとした。しかして5伽/分
の抄造スピードで繊維スラリー、セメントスラリー、繊
維スラリーの順番で抄上げ積層し、メーキングロールに
巻取り、6側の厚みになったところでこれを切断し、2
日間の水中養生及び7日間の自然養生を行なってガラス
繊維強化セメント板を得た。On the other hand, in the second vat 3b, a cement slurry 2 having a weight ratio of ordinary Bortland cement and pulp of 1:2 and a slurry concentration of 10% mixed with water was charged. Further, the mesh of the papermaking cylinders 4a, 4c in the fiber slurry 1 of the vats 3a+3c was set to 60 mesh, and the mesh of the papermaking cylinder 4b in the cement slurry 2 of the vat 3b was set to 100 mesh. Then, the fiber slurry, cement slurry, and fiber slurry were laminated in this order at a papermaking speed of 5 k/min, wound on a making roll, and cut when the thickness reached the 6-side thickness.
A glass fiber reinforced cement board was obtained by curing in water for 1 day and naturally curing for 7 days.
添付図は本発明の一実施例の概略図である。 The accompanying drawings are schematic illustrations of one embodiment of the invention.
Claims (1)
ーと、ガラス繊維が含まれないセメントスラリーとを時
間的に相前後して抄造し積層することを特徴とするガラ
ス繊維強化セメント板の製造法。1. A method for manufacturing a glass fiber-reinforced cement board, which comprises forming and laminating a glass fiber-containing fiber slurry that does not contain cement and a cement slurry that does not contain glass fiber in sequence.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5018477A JPS6029602B2 (en) | 1977-04-30 | 1977-04-30 | Manufacturing method of glass fiber reinforced cement board |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5018477A JPS6029602B2 (en) | 1977-04-30 | 1977-04-30 | Manufacturing method of glass fiber reinforced cement board |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS53134816A JPS53134816A (en) | 1978-11-24 |
| JPS6029602B2 true JPS6029602B2 (en) | 1985-07-11 |
Family
ID=12852092
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5018477A Expired JPS6029602B2 (en) | 1977-04-30 | 1977-04-30 | Manufacturing method of glass fiber reinforced cement board |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6029602B2 (en) |
-
1977
- 1977-04-30 JP JP5018477A patent/JPS6029602B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS53134816A (en) | 1978-11-24 |
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