JPS6344706B2 - - Google Patents
Info
- Publication number
- JPS6344706B2 JPS6344706B2 JP56087516A JP8751681A JPS6344706B2 JP S6344706 B2 JPS6344706 B2 JP S6344706B2 JP 56087516 A JP56087516 A JP 56087516A JP 8751681 A JP8751681 A JP 8751681A JP S6344706 B2 JPS6344706 B2 JP S6344706B2
- Authority
- JP
- Japan
- Prior art keywords
- gypsum
- slurry
- gypsum board
- less
- manufacturing
- 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
Landscapes
- Curing Cements, Concrete, And Artificial Stone (AREA)
Description
本発明は石こう板の製造方法、さらに詳しくは
製品の表面にしわがより、あたかも象の皮のよう
な様相を呈し、外観並びに製品の性状を著しく悪
くする現象(以下象皮現象という)を伴なわない
石こう板を丸網抄造法によつて製造する方法に関
するものである。
丸網抄造法により石こう板を製造するには、石
こう、繊維及び水を含むスラリーを丸網抄造装置
により抄造するが、従来丸網抄造法に用いられる
石こうは石膏石灰誌No.144(1976)19ページに示さ
れているようにその粉末度がブレーン値で7000〜
8000cm2/g程度であつた。
しかし、従来の丸網抄造法は得られる製品の表
面に象皮現象が発生し易すく、かつ機械的強度が
大幅に低下するという欠点があつた。この対策と
して抄造のスピードを下げることによつてある程
度その発生を抑制できるが、完全ではなくまた生
産性が大幅に低下する欠点がある。
本発明者らは従来の丸網抄造法の欠点を排除
し、象皮現象の発生を伴なわず、かつ従来よりも
生産性を低下させない丸網抄造法で、石こう板を
製造する方法を求めて研究した結果、使用するβ
−半水石こうの粉末度をブレーン値で1000cm2/g
以上6000cm2/g未満にすれば、これらの問題が解
決し得るとの知見を得て本発明を完成するにいた
つた。
すなわち、本発明の要旨は、β−半水石こう、
繊維、凝結遅延剤及び水を含むスラリーを丸網抄
造装置により抄造して石こう板を製造するにさい
し、粉末度がブレーン値で1000cm2/g以上5000
cm2/g未満であるβ−半水石こうまたは該石こう
に対しブレーン値で2000〜5000cm2/gである濾過
補助材を50重量%以下添加した原料を用いて濃度
7〜15%のスラリーとし、これを真空脱水装置付
ベルトコンベアーのスピードを40〜65m/minと
して抄き上げることを特徴とする石こう板の製造
方法である。β−半水石こうの発生源別では天然
産石こう、排ガスの脱硫及びりん酸製造のさい等
の副産石こうが用いられる。
繊維としてはアスベスト、ガラス繊維、ロツク
ウール等の無機繊維、及びパルプ、ナイロン、ポ
リプロピレン、アクリル等の有機繊維が用いられ
る。
β−半水石こうの粉末度がブレーン値で1000
cm2/g未満であると、スラリーの固形分が沈降し
易く抄き上げにくくなり、得られた製品の可撓性
が少く強度が弱くなる。
また、5000cm2/g以上であると、丸網抄造法に
より得られる石こう板に象皮現象の発生が見ら
れ、これにより強度が大巾に低下する。また、ス
ラリー中のβ−半水石こう分が過水中に移行し
易くなり、これに伴ない石こうの歩留が低下す
る。さらに抄造した生板の含水率も高くなる。
スラリー調製時から抄造するまでの最適時間
は、使用する原料及び最終製品の仕様によつて異
なり、これに対応して慣用の凝結遅延剤、例えば
クエン酸、その塩、アミノ酸、その塩及び蛋白
質、その変成物等を用いることができる。
本発明の石こう板の製造方法では慣用の丸網抄
造装置を用いる。すなわち、β−半水石こう、繊
維及び水並びに石こう凝結遅延剤とを混練して得
られるスラリーより、複数個の丸網回転ドラムに
よつてその固形物を抄きあげ、得られた複数個の
スラリーの固形物のフイルムを真空脱水装置付ベ
ルトコンベヤー面上で積層させ、ついでこの積層
フイルムをさらに所定の厚みとなるようにメーキ
ングロールによりロール加圧しながらまき合わせ
て第一次石こう板を得、さらにこの第一次石こう
板を加圧又は加圧しないで成型し乾燥して石こう
板の製品を得る。製品の板厚は4〜10mm程度であ
る。
この場合石こう板の象皮現象は、前記メーキン
グロールにより積層フイルムをロール加圧する段
階で生ずる。
また、石灰石、硅石、タルク、パーライト、バ
ーミユキライト、雲母、スラグ、フライアツシユ
等の粉末が過補助材として併用されることがで
きる。このさいの粉末度は2000〜5000cm2/gであ
ることが好ましい。添加量は石こうに対して50重
量%以下である。
なお、抄造のさいのスラリーのpHが5.5〜110
であれば本発明の方法による石こう板はさらに強
度を増大する。
真空装置付ベルトコンベアーのスピードは、40
〜65m/minが好ましい。
40m/min未満だと、フイルムの脱水性、加圧
特性をある程度改善して象皮を低減できるが、脱
水し過ぎて含水率を下げ過ぎると、積層した場合
の層間の接着性が低下し、品質が低下するととも
に繊維の配向性、生産性が著しく低下する。
また、65m/minを超えると、原料配合、運転
条件等を変えても象皮現象が生じるとともに均質
な平板が得られず、品質も低下するので好ましく
ない。
なお、本願発明においてスラリー濃度は通常の
繊維の分散性、フイルムの均質性並びに生産性
(丸網への抄き上げ厚)から10%程度とし、7〜
15%の範囲が好ましい。
スラリー濃度が15%よりも濃いと繊維の分散
性、フイルムの均質性、抄造性が悪化するとと共
に、フイルムの脱水性、加圧特性が悪くなり象皮
現象が多発する。
また、スラリー濃度が7%よりも薄くなると、
抄き厚が減少し、フイルムの含水率が低下し過
ぎ、積層間の接着不良、生産性の低下を来すので
好ましくない。
また、真空脱水圧はこれを上げると、脱水性を
良好にし、含水率を低下させ、象皮現象を低減す
ることになる。
真空脱水はベルトコンベアー(フエルト布)を
介して、フイルムから水を引くため、若干のリー
クがあり、また真空圧力を下げすぎるとベルトコ
ンベアーに負荷が掛り過ぎてベルトコンベアーの
スリツプ、停止等のトラブルが生ずる。
さらにフイルムの含水率を低下し過ぎると、前
記同様な層間の接着不良の問題が生ずることとな
る。
そこで、真空脱水圧はブルドン管のゲージ圧
(目盛0〜76cmHg、minO、max76cmHg)で10〜
50cmHgとすることが好ましい。
本発明によれば製品の表面に象皮現象がみられ
ず美麗な面を有する石こう板を丸網抄造法により
生産性を低下させずに、かつ製品強度を大にして
製造することができる。
また本発明によれば水への石こうの流出が少
ない。そのため、リサイクルされる水中での二
水石こうの生成が少なくなり、この二水石こうに
よる石こうの凝結促進作用が大幅に減少し長期安
定運転が可能となつた。
つぎに本発明の実施態様を実施例によつて説明
するが、本発明はこれらによつて限定されるもの
ではない。
なお、本文中の%および部は特記しない限りそ
れぞれ重量%および重量部を示すものである。
実施例1〜4、比較例1〜5
表1に示される粉末度を有するβ−半水石こう
67.5%にパルプ10%、アスベスト10%、ガラス繊
維2.5%および石灰石粉末10%をそれぞれ配合し
た。なおそれぞれの配合組成物には石こう凝結遅
延剤としてたん白質を加水分解して変性した、変
性アミノ酸塩を石こうに対して0.3%添加した。
それぞれの配合組成物1部に対して10部の水を加
えパルパーで撹拌してスラリーとし、このスラリ
ーを金網の付いた4基のシリンダーを有する丸網
抄造機によつて抄造し得られた抄造体を100Kg/
cm2の面圧プレスによつて加圧し、それぞれの石こ
う板を得た。それぞれの石こう板について凝結時
間、曲げ強度および含水率を測定し、得た結果を
表1に示した。
The present invention relates to a method for manufacturing a gypsum board, and more specifically to a method for manufacturing a gypsum board, which is accompanied by a phenomenon in which wrinkles form on the surface of the product, making it look like an elephant skin, which significantly deteriorates the appearance and properties of the product (hereinafter referred to as elephant skin phenomenon). The present invention relates to a method for manufacturing a gypsum board without any gypsum using a round netting method. In order to manufacture gypsum board using the round netting method, a slurry containing gypsum, fibers and water is made into paper using a round netting machine, but the gypsum conventionally used in the round netting method is manufactured by Gypsum Lime Journal No. 144 (1976). As shown on page 19, its fineness is Blaine value 7000 ~
It was about 8000cm 2 /g. However, the conventional round-mesh papermaking method has the disadvantage that elephant skin phenomenon tends to occur on the surface of the obtained product, and the mechanical strength is significantly reduced. As a countermeasure to this problem, it is possible to suppress the occurrence to some extent by reducing the speed of papermaking, but it is not perfect and has the drawback that productivity is significantly reduced. The present inventors sought a method for manufacturing gypsum board using a circular mesh paper manufacturing method that eliminates the drawbacks of the conventional round mesh paper manufacturing method, does not involve the occurrence of the elephant skin phenomenon, and does not reduce productivity compared to the conventional method. As a result of research, the β
-The fineness of hemihydrate gypsum is 1000 cm 2 /g in Blaine value.
The present invention was completed based on the knowledge that these problems can be solved by reducing the density to less than 6000 cm 2 /g. That is, the gist of the present invention is that β-hemihydrate gypsum,
When manufacturing a gypsum board by making a slurry containing fibers, a setting retarder, and water using a circular mesh papermaking machine, the fineness must be 1000 cm 2 /g or more in Blaine value 5000.
A slurry with a concentration of 7 to 15% is made using β-hemihydrate gypsum with a density of less than cm 2 /g or a raw material in which 50% by weight or less of a filter aid with a Blaine value of 2000 to 5000 cm 2 /g is added to the gypsum. This is a method for producing a gypsum board, which is characterized in that it is processed using a belt conveyor equipped with a vacuum dewatering device at a speed of 40 to 65 m/min. By the source of β-hemihydrate gypsum, naturally produced gypsum and by-product gypsum from exhaust gas desulfurization and phosphoric acid production are used. The fibers used include inorganic fibers such as asbestos, glass fiber, and rock wool, and organic fibers such as pulp, nylon, polypropylene, and acrylic. The fineness of β-hemihydrate gypsum is 1000 in Blaine value.
If it is less than cm 2 /g, the solid content of the slurry will tend to settle, making it difficult to scoop out, and the resulting product will have less flexibility and strength. Moreover, if it is 5000 cm 2 /g or more, the occurrence of elephant skin phenomenon will be observed in the gypsum board obtained by the round net papermaking method, which will significantly reduce the strength. In addition, the β-hemihydrate gypsum component in the slurry tends to migrate into the superhydrate, and the yield of gypsum decreases accordingly. Furthermore, the moisture content of the paper-formed raw board also increases. The optimal time from the time of slurry preparation to the time of papermaking varies depending on the raw materials used and the specifications of the final product, and correspondingly, conventional setting retarders such as citric acid, its salts, amino acids, its salts and proteins, A modified product thereof can be used. In the method for manufacturing a gypsum board of the present invention, a conventional circular mesh machine is used. That is, from a slurry obtained by kneading β-hemihydrate gypsum, fibers, water, and a gypsum setting retarder, a plurality of solids are extracted using a plurality of circular mesh rotating drums. A film of the solid slurry is laminated on the surface of a belt conveyor equipped with a vacuum dewatering device, and then this laminated film is further rolled together while applying roll pressure with a making roll to obtain a primary gypsum board, so as to have a predetermined thickness. Further, this primary gypsum board is molded with or without pressure and dried to obtain a gypsum board product. The thickness of the product is approximately 4 to 10 mm. In this case, the elephant skin phenomenon of the gypsum board occurs at the stage where the laminated film is roll-pressed by the making roll. Further, powders such as limestone, silica, talc, pearlite, vermiyukilite, mica, slag, fly ash, etc. can be used in combination as a supplementary material. The powder degree at this time is preferably 2000 to 5000 cm 2 /g. The amount added is 50% by weight or less based on the gypsum. In addition, the pH of the slurry during papermaking is 5.5 to 110.
If so, the strength of the gypsum board produced by the method of the invention is further increased. The speed of the belt conveyor with vacuum device is 40
~65 m/min is preferred. If it is less than 40 m/min, the dehydration and pressure properties of the film can be improved to some extent and elephant skin can be reduced, but if it is dehydrated too much and the water content is lowered too much, the adhesion between the layers will decrease when laminated. Along with the quality deterioration, fiber orientation and productivity are significantly reduced. Further, if the speed exceeds 65 m/min, elephant skin phenomenon occurs even if the raw material composition, operating conditions, etc. are changed, and a homogeneous flat plate cannot be obtained, resulting in a decrease in quality, which is not preferable. In addition, in the present invention, the slurry concentration is approximately 10% from the viewpoint of normal fiber dispersibility, film homogeneity, and productivity (thickness of sheeting into a circular screen), and 7 to 7%.
A range of 15% is preferred. If the slurry concentration is higher than 15%, fiber dispersibility, film homogeneity, and papermaking properties will deteriorate, as well as film dehydration and pressure properties will deteriorate, resulting in frequent occurrence of elephant skin phenomenon. Also, when the slurry concentration becomes thinner than 7%,
This is not preferable because the paper thickness decreases, the water content of the film decreases too much, and this causes poor adhesion between laminated layers and a decrease in productivity. In addition, increasing the vacuum dehydration pressure improves the dehydration properties, lowers the water content, and reduces the elephant skin phenomenon. Vacuum dehydration draws water from the film through a belt conveyor (felt cloth), so there may be some leakage, and if the vacuum pressure is lowered too much, it will put too much load on the belt conveyor, causing problems such as belt conveyor slipping and stopping. occurs. Furthermore, if the water content of the film is reduced too much, the same problem of poor adhesion between layers as described above will occur. Therefore, the vacuum dehydration pressure is 10 to 76cmHg using the Bourdon tube gauge pressure (scale 0 to 76cmHg, minO, max76cmHg).
It is preferable to set it to 50cmHg. According to the present invention, a gypsum board having a beautiful surface without the elephantine phenomenon on the surface of the product can be manufactured by the round-mesh papermaking method without reducing productivity and increasing the strength of the product. Furthermore, according to the present invention, there is less gypsum flowing out into water. As a result, less gypsum dihydrate is produced in the recycled water, and the promoting effect of gypsum dihydrate on setting of gypsum is significantly reduced, making stable operation possible over a long period of time. Next, the embodiments of the present invention will be described with reference to Examples, but the present invention is not limited thereto. Note that % and parts in the text indicate weight % and parts by weight, respectively, unless otherwise specified. Examples 1 to 4, Comparative Examples 1 to 5 β-hemihydrate gypsum having the fineness shown in Table 1
67.5% with 10% pulp, 10% asbestos, 2.5% glass fiber and 10% limestone powder. In addition, 0.3% of modified amino acid salts, which are denatured by hydrolyzing proteins, were added to each blended composition as a gypsum setting retardant, based on the amount of gypsum.
10 parts of water is added to 1 part of each blended composition and stirred with a pulper to form a slurry, and this slurry is made into paper using a circular mesh paper machine having four cylinders equipped with wire mesh. Body 100Kg/
Pressure was applied using a cm 2 surface pressure press to obtain each gypsum board. The setting time, bending strength, and moisture content of each gypsum board were measured, and the results are shown in Table 1.
【表】
表1から明かなようにブレーン値で1000cm2/g
以上5000cm2/g未満の粉末度を有する石こうを用
いた実施例品には、その表面に象皮現象が全く認
められず、またカサ比重及び曲げ強度も大とな
り、製造過程において得られる生板はその含水率
が小さく、かつ凝結時間も長くなり作業性が良好
になることが認められた。
また、生産性も従来法に比べると30%向上する
のが認められた。[Table] As is clear from Table 1, the Blaine value is 1000cm 2 /g
In the example products using gypsum having a fineness of less than 5000 cm 2 /g, no elephantine phenomenon was observed on the surface, and the bulk specific gravity and bending strength were also high, and the green plate obtained in the manufacturing process was It was found that the water content was low and the setting time was long, resulting in good workability. It was also observed that productivity was improved by 30% compared to the conventional method.
Claims (1)
含むスラリーを丸網抄造装置により抄造して石こ
う板を製造するにさいし、粉末度がブレーン値で
1000cm2/g以上5000cm2/g未満であるβ−半水石
こうまたは該石こうに対しブレーン値で2000〜
5000cm2/gである濾過補助剤を50重量%以下添加
した原料を用いて濃度7〜15%のスラリーとし、
これを真空脱水装置付ベルトコンベアーのスピー
ドを40〜65m/minとして抄き上げることを特徴
とする石こう板の製造方法。1 When manufacturing gypsum board by making a slurry containing β-hemihydrate gypsum, fibers, setting retardant, and water using a circular mesh machine, the fineness is the Blaine value.
β-hemihydrate gypsum that is 1000 cm 2 /g or more and less than 5000 cm 2 /g or 2000 to 2000 in Blaine value for the gypsum
A slurry with a concentration of 7 to 15% is made using raw materials to which 50% by weight or less of a filter aid of 5000 cm 2 /g is added,
A method for producing a gypsum board, which is characterized in that it is processed by a belt conveyor equipped with a vacuum dewatering device at a speed of 40 to 65 m/min.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8751681A JPS57205351A (en) | 1981-06-09 | 1981-06-09 | Manufacture of gypsum board |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8751681A JPS57205351A (en) | 1981-06-09 | 1981-06-09 | Manufacture of gypsum board |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57205351A JPS57205351A (en) | 1982-12-16 |
| JPS6344706B2 true JPS6344706B2 (en) | 1988-09-06 |
Family
ID=13917148
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8751681A Granted JPS57205351A (en) | 1981-06-09 | 1981-06-09 | Manufacture of gypsum board |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57205351A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60171261A (en) * | 1984-02-14 | 1985-09-04 | 太平洋セメント株式会社 | Manufacture of incombustible gypsum board |
| JPS6241748A (en) * | 1985-08-13 | 1987-02-23 | 太平洋セメント株式会社 | Manufacture of incombustible inorganic construction material |
| JPS6241747A (en) * | 1985-08-13 | 1987-02-23 | 太平洋セメント株式会社 | Manufacture of incombustible gypsum board |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5258729A (en) * | 1975-11-10 | 1977-05-14 | Nihon Cement | Gypsum paper |
| JPS53134029A (en) * | 1977-04-28 | 1978-11-22 | Nihon Cement | Gypsum composite |
| JPS5436332A (en) * | 1977-08-26 | 1979-03-17 | Nihon Cement | Water resisting fibrous plaster board |
-
1981
- 1981-06-09 JP JP8751681A patent/JPS57205351A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57205351A (en) | 1982-12-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP2647610B1 (en) | Inorganic material board | |
| US3951735A (en) | Process for preparing gypsum board | |
| US4085001A (en) | Fiber reinforced cementitious substrate | |
| CA1192709A (en) | Mineral fiber-containing paper for the production of gypsum wallboard and wallboard product prepared therewith | |
| EP0068741A1 (en) | Boards and sheets | |
| US6268042B1 (en) | High strength low density board for furniture industry | |
| JPH0476943B2 (en) | ||
| EP0047158B2 (en) | A process for the manufacture of fibre reinforced shaped articles | |
| JPS6344706B2 (en) | ||
| JP2000302522A (en) | Production of fiber reinforced cement board | |
| JPS59165615A (en) | Manufacture of press molding machining fibrous making board | |
| CA1059736A (en) | Method of producing fibre-containing building members | |
| EP0655966A1 (en) | Continuous processing equipment for making fiberboard | |
| JP2836941B2 (en) | Method for manufacturing gypsum sheet board | |
| JPH1192207A (en) | Method for manufacturing gypsum sheet board | |
| JP3308854B2 (en) | Manufacturing method of inorganic plate | |
| JPH085704B2 (en) | Method for producing anhydrous gypsum papermaking board | |
| SU706360A1 (en) | Raw mixture for producing building articles | |
| JPS62191455A (en) | Anhydrous gypsum papered board and manufacture | |
| JP2601781B2 (en) | Cement fiberboard | |
| AU2011201384B2 (en) | Inorganic board and inorganic board production method | |
| CA2090285A1 (en) | Process for producing fibrous composites, particularly double floor plates, as well as plates produced by this process | |
| JPH0520377B2 (en) | ||
| JP2514462B2 (en) | Cement board manufacturing method | |
| JPH02116515A (en) | Manufacture of inorganic building material |