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JPS5848333B2 - How do you know what to do? - Google Patents
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JPS5848333B2 - How do you know what to do? - Google Patents

How do you know what to do?

Info

Publication number
JPS5848333B2
JPS5848333B2 JP49013093A JP1309374A JPS5848333B2 JP S5848333 B2 JPS5848333 B2 JP S5848333B2 JP 49013093 A JP49013093 A JP 49013093A JP 1309374 A JP1309374 A JP 1309374A JP S5848333 B2 JPS5848333 B2 JP S5848333B2
Authority
JP
Japan
Prior art keywords
plate
fibers
resin
thermoplastic resin
extruder
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
JP49013093A
Other languages
Japanese (ja)
Other versions
JPS50107073A (en
Inventor
啓 岩田
六郎 村井
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.)
Sekisui Chemical Co Ltd
Original Assignee
Sekisui Chemical Co 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 Sekisui Chemical Co Ltd filed Critical Sekisui Chemical Co Ltd
Priority to JP49013093A priority Critical patent/JPS5848333B2/en
Publication of JPS50107073A publication Critical patent/JPS50107073A/ja
Publication of JPS5848333B2 publication Critical patent/JPS5848333B2/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/465Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using rollers
    • B29C48/467Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using rollers using single rollers, e.g. provided with protrusions, closely surrounded by a housing with movement of the material in the axial direction
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/07Flat, e.g. panels
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/375Plasticisers, homogenisers or feeders comprising two or more stages
    • B29C48/39Plasticisers, homogenisers or feeders comprising two or more stages a first extruder feeding the melt into an intermediate location of a second extruder

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Moulding By Coating Moulds (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Molding Of Porous Articles (AREA)

Description

【発明の詳細な説明】 本発明は繊維で補強された熱可塑性樹脂の板状体の製遣
方法に関するものであり特に押出成型法によって上記板
状体を製造する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for manufacturing a fiber-reinforced thermoplastic resin plate, and particularly to a method for producing the plate by extrusion molding.

従来熱可塑性樹脂に繊維補強材を混合し、該混合物を押
出機に供給して溶融混練を経て押出機の先端に取着され
た金型から板状に押出して繊維補強熱可塑性樹脂板状体
を製造する方法が知られている。
Conventionally, a fiber reinforced thermoplastic resin plate is produced by mixing a thermoplastic resin with a fiber reinforcing material, supplying the mixture to an extruder, melting and kneading it, and extruding it into a plate from a mold attached to the tip of the extruder. A method of manufacturing is known.

しかしながら上述のような従来の方法においては下記の
如き欠点がある。
However, the conventional method as described above has the following drawbacks.

即ち、先ず熱可塑性樹脂中に含有されている補強繊維の
樹脂中への分散が不良であることである。
That is, first, the reinforcing fibers contained in the thermoplastic resin are poorly dispersed in the resin.

補強繊維は通常単繊維が集束されたものであるが、か\
る集束された補強繊維は樹脂の溶融混線下にも容易には
樹脂中に均一に分散せず束のまへで存在する傾向にあり
、従って補強繊維による樹脂の補強効果が充分現われず
延では強度の犬なる板状体を製造することが困難である
Reinforcing fibers are usually bundles of single fibers, but...
The bundled reinforcing fibers do not easily disperse uniformly in the resin even when the resin is melted and mixed, and tend to exist between the bundles. It is difficult to manufacture a strong plate-shaped body.

次に補強繊維が押出工程中に押出方向に配列することに
よって、得られた板状体は押出方向には大きい強度を有
し得ても押出方向と直角方向の強度は向上しないか又は
却って低下する。
Next, because the reinforcing fibers are arranged in the extrusion direction during the extrusion process, even though the obtained plate-shaped body may have high strength in the extrusion direction, the strength in the direction perpendicular to the extrusion direction does not improve or on the contrary decreases. do.

このため得られる板状体は均一な強度を有さず強度に方
向性のある板状体しか得られない。
For this reason, the resulting plate-like body does not have uniform strength, and only a plate-like body with directional strength can be obtained.

本発明は叙上の如き従来の方法に存する欠点を改善する
ためになされたものであり、補強繊維の樹脂中での分布
が均一であり且補強繊維の分散状態に方向性が存しない
ようにし以って繊維による補強効果が犬なる熱可塑性樹
脂板状体を製造することを目白勺とする。
The present invention has been made in order to improve the drawbacks of the conventional methods as described above, and it is possible to ensure that the distribution of reinforcing fibers in the resin is uniform and that there is no directionality in the dispersion state of the reinforcing fibers. Therefore, the aim is to manufacture a thermoplastic resin plate-like body in which the reinforcing effect of fibers is effective.

しかして本発明は相対的に回転又は反転している軸と外
型との間に形成される環状細隙に、補強繊維を含有する
加熱溶融された熱可塑性樹脂を通過せしめた後、これを
板状体戒型金型に送給し押出すことを特徴とする繊維補
強熱可塑性樹脂板状体の製造方法を要旨とするものであ
る。
Therefore, in the present invention, a heated and melted thermoplastic resin containing reinforcing fibers is passed through an annular gap formed between a relatively rotating or inverted shaft and an outer mold, and then The gist of the present invention is a method for manufacturing a fiber-reinforced thermoplastic resin plate, which is characterized by feeding the plate into a mold and extruding it.

本発明において用いられる補強繊維としては樹脂が加熱
溶融される温度下でも劣化しない性質を有し且強度の犬
なるものが用いられ、更に熱可塑性樹脂との接着性が良
いものが用いられて好適である。
The reinforcing fiber used in the present invention is preferably one that has a property of not degrading even at the temperature at which the resin is heated and melted and is strong, and also has good adhesion to the thermoplastic resin. It is.

上記補強繊維の具体的な例としては例えばガラス繊維、
炭素繊維、ボロン繊維等の無機繊維の他麻や木綿或いは
ボリアミドやポリエステルからなる繊維の如き有機繊維
が挙げられる。
Specific examples of the reinforcing fibers include glass fiber,
Examples include inorganic fibers such as carbon fibers and boron fibers, and organic fibers such as fibers made of hemp, cotton, polyamide, and polyester.

補強繊維の長さについては極端に短い短繊維を用いた場
合には補強効果が現われないので通常1關以−Lの長さ
のものが用いられ、特に長繊維のものが好ましい。
Regarding the length of reinforcing fibers, if extremely short short fibers are used, no reinforcing effect will be obtained, so those having a length of 1 L or more are usually used, and long fibers are particularly preferred.

又上述の補強繊維は単繊維であってもよく、又単繊維が
複数本集束されたものであっても良い。
Further, the above-mentioned reinforcing fiber may be a single fiber, or may be a bundle of a plurality of single fibers.

次に本発明において用いられる熱可塑性樹脂としては押
出成型に用いられる通常の樹脂が好適に用いられるので
あって例えばポリエチレン、ポリプロピレン、ポリスチ
レン、ポリ塩化ビニル、ポリアミド、ポリエステル、ポ
リカーポネート等の他エチレンー塩化ビニル共重合体、
エヂレンープロピレン共重合体、エチレンー酢酸ビニル
」、事合体、スチレンーアクリロニ1〜リル共重合体等
が挙げられる。
Next, as the thermoplastic resin used in the present invention, ordinary resins used in extrusion molding are suitably used, such as polyethylene, polypropylene, polystyrene, polyvinyl chloride, polyamide, polyester, polycarbonate, etc. vinyl chloride copolymer,
Examples include ethylene-propylene copolymer, ethylene-vinyl acetate copolymer, styrene-acryloni-1-lyl copolymer, and the like.

又本発明においては上記各樹脂は2種以上のものが混合
されて用いられてもよく、更に樹脂と発泡剤との混合物
を用いて発泡体とせしめることも可能である。
Further, in the present invention, two or more of the above-mentioned resins may be used as a mixture, and it is also possible to form a foam by using a mixture of the resin and a foaming agent.

上記発泡剤としては例えば、アゾジカルボンアミド、ア
ゾビスイソブチロニトリル、重炭酸ナトリウム、窒素ガ
ス、炭酸ガス、プロパン、ブタン、ペンタン、塩化弗化
炭化水素類等が挙げられる。
Examples of the blowing agent include azodicarbonamide, azobisisobutyronitrile, sodium bicarbonate, nitrogen gas, carbon dioxide, propane, butane, pentane, chlorofluorohydrocarbons, and the like.

以上に説明した補強繊維と熱可塑性樹脂とは予め混合さ
れたものであっても良く又後述するところの本発明にお
いて好適に用いられ得る装置に各別に供給し−L記装置
内で混合されても良い。
The reinforcing fibers and thermoplastic resin described above may be mixed in advance, or they may be supplied separately to a device that can be suitably used in the present invention, which will be described later, and then mixed in the device described in L. Also good.

次に本発明において好適に用いられる装置の一実施例を
示す図面を参照しながら本発明方法を更に詳細に説明す
る。
Next, the method of the present invention will be explained in more detail with reference to the drawings showing an embodiment of the apparatus preferably used in the present invention.

図において1は通常の押出機であって押出筒4とスクリ
ュー3とクロスヘッド5と原料供給口2とからなり、該
押出機1に原料供給口2から熱可塑性樹脂を供給し加熱
溶融下に混練してクロスヘッド5を経て連通管6を通じ
て後段の押出機に供給する。
In the figure, 1 is an ordinary extruder, which is composed of an extrusion tube 4, a screw 3, a crosshead 5, and a raw material supply port 2. Thermoplastic resin is supplied to the extruder 1 from the raw material supply port 2, and is heated and melted. The mixture is kneaded and fed through a crosshead 5 and a communicating pipe 6 to a subsequent extruder.

上記後段の押出機は外型7と軸8とからなり該外型7と
軸8とは環状細隙81を形成するべく配置され且図示す
る装置においては軸8は、駆動装置13に連結され回転
されている。
The latter stage extruder comprises an outer mold 7 and a shaft 8, and the outer mold 7 and shaft 8 are arranged to form an annular gap 81, and in the illustrated apparatus, the shaft 8 is connected to a drive device 13. It's being rotated.

環状細隙81には該環状細隙81の断面形状に沿って設
けられた多数の細孔10が連通されており、連続したガ
ラス繊維束12が各細孔10を通じて環状細隙81に供
給される。
A large number of pores 10 provided along the cross-sectional shape of the annular slit 81 are communicated with the annular slit 81, and a continuous glass fiber bundle 12 is supplied to the annular slit 81 through each pore 10. Ru.

11はガラス繊維束12を導ひくガイドローラーである
11 is a guide roller that guides the glass fiber bundle 12.

押出機1中で加熱溶融された熱可塑性樹脂は前述の如く
連通管6を経て環状細隙81に供給され同時に環状細隙
81に供給されるガラス繊維束12と共に、押出機1に
よる背圧によって順次押出される。
The thermoplastic resin heated and melted in the extruder 1 is supplied to the annular slit 81 through the communication pipe 6 as described above, and together with the glass fiber bundle 12 supplied to the annular slit 81 at the same time, the thermoplastic resin is heated and melted in the extruder 1 by back pressure from the extruder 1. Extruded sequentially.

しかして軸8は回転しているため環状細隙81中に存す
る溶融状態にある樹脂及びガラス繊維束12は押出方向
と直交する剪断力を受けることとなりその結果ガラス繊
維束12はバラバラにほぐされると共に押出方向に対し
て斜めの方向に配列される。
Since the shaft 8 is rotating, the molten resin and glass fiber bundle 12 present in the annular gap 81 are subjected to a shearing force perpendicular to the extrusion direction, and as a result, the glass fiber bundle 12 is loosened into pieces. and are arranged in a direction diagonal to the extrusion direction.

バラバラにほぐされたガラス繊維が均一に樹脂中に分散
され且押出方向に対して斜め方向に配列されたガラス繊
維を含有する溶融樹脂は次いで溶融状態を保ったま5板
状体或型金型15に供給される。
The loosened glass fibers are uniformly dispersed in the resin, and the molten resin containing the glass fibers arranged diagonally with respect to the extrusion direction is then molded into a plate-shaped body or a mold 15, which remains in a molten state. supplied to

環状細隙81と上記板状体成型金型15は連続的にその
断面形状が変化する通路14によって連通されてなり、
ガラス繊維を含有する−L記溶融樹脂は筒状体から連続
的に板状体に賦型される。
The annular slit 81 and the plate molding die 15 are communicated with each other by a passage 14 whose cross-sectional shape continuously changes,
The molten resin containing glass fibers is continuously shaped into a plate-like body from a cylindrical body.

板状体或型金型15から押出された板状体16は次いで
冷却サイジング水槽17を経て引取ロール18によって
引取られ製品化される。
The plate-shaped body 16 extruded from the plate-shaped body or die 15 is then passed through a cooling sizing water tank 17 and taken up by a take-up roll 18 to be manufactured into a product.

向、図においては図示していないが押出機1、外型7及
び板状体成型金型15はいずれも樹脂を溶融状態に保つ
べく加熱手段が施されている。
Although not shown in the drawings, the extruder 1, the outer mold 7, and the plate molding die 15 are all equipped with heating means to keep the resin in a molten state.

又上述の実施例においては軸8は回転されているが反転
せしめてもよく、この場合グラス繊維の配列方向を交互
に変化せしめることができる。
Further, although the shaft 8 is rotated in the above-described embodiment, it may be reversed, in which case the direction in which the glass fibers are arranged can be alternately changed.

更に又−h述の実施例では外型7は固定され軸8を回転
せしめたが逆に外型7を回転せしめて軸8を固定すると
か或いは外型T及び軸8の双方を互いに反対方向に回転
せしめるか反転せしめることも可能である。
Furthermore, in the embodiment described in -h, the outer mold 7 is fixed and the shaft 8 is rotated, but instead, the outer mold 7 is rotated and the shaft 8 is fixed, or both the outer mold T and the shaft 8 are rotated in opposite directions. It is also possible to rotate or invert.

又上述の実施例においては樹脂を加熱溶融下に混練する
ために別に押出機1を設けて該押出機1から環状細隙8
1に樹脂を供給せしめたが環状細隙81を有する押出機
と前記押出機1とを一体にすることも可能である。
Further, in the above-mentioned embodiment, an extruder 1 is separately provided in order to knead the resin while heating and melting it.
Although the resin is supplied to the extruder 1, it is also possible to integrate the extruder 1 with an extruder having an annular gap 81.

本発明においては板状体成型金型15は必ずしも平板状
に賦形するものに限られず、断面形状がコ字型とか波型
とかの異形断面を有する板状体に賦形ずるための板状体
或型金型を用いることも可能である。
In the present invention, the plate-shaped object molding die 15 is not necessarily limited to a mold for shaping into a flat plate shape, but a plate-like object for forming a plate-like object having an irregular cross section such as a U-shape or a wave shape. It is also possible to use a body or mold.

以上に詳説した通り本発明においては相対的に回転又は
反転している軸と外型との間に形或ざれる環状細隙に、
補強繊維を含有する加熱溶融された熱可塑性樹脂を通過
せしめるという工程が採用されるのであるから、上記樹
脂中の補強繊維は環状細隙を通過する間に回転又は反転
作用に基づく押出方向と直角方向の剪断力によって配列
方向が押出方向に対して斜めになる。
As explained in detail above, in the present invention, in the annular gap formed between the relatively rotated or reversed shaft and the outer mold,
Since the process of passing the heated and melted thermoplastic resin containing reinforcing fibers is adopted, the reinforcing fibers in the resin pass through the annular gap at right angles to the extrusion direction due to rotation or reversal action. Due to the shearing force in the direction, the arrangement direction becomes oblique to the extrusion direction.

又補強繊維が集束されたものであると上記剪断力によっ
てバラバラにほぐされ樹脂中に均一に分散する。
If the reinforcing fibers are bundled, they will be loosened by the shearing force and uniformly dispersed in the resin.

このように樹脂中での補強繊維の分布状態或いは配列方
向が改善されることによって板状体成型金型から押出さ
れて製される板状体は強度が犬で且強度に方向性がなく
商品価値の高いものである。
By improving the distribution and arrangement direction of the reinforcing fibers in the resin, the plate-shaped body extruded from the plate-shaped body mold has a high strength and is not directional, making it a good product. It is of high value.

従って従来方法の如く補強繊維と樹脂とを押出機に供給
して単に押出成型することによって板状体を製造する方
法に比してより犬なる強度を有する板状体を製すること
ができる。
Therefore, it is possible to produce a plate-like body with greater strength compared to the conventional method of producing a plate-like body by simply supplying reinforcing fibers and resin to an extruder and extrusion molding.

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

第1図は本発明に用いられて好適なる装置の一実施例を
示す一部切欠上面図である。 図において要部の名称は下記の通りである。 7・・・・・・外型、8・・・・・・軸、12・・・・
・・補強繊維(ガラス繊維束)、81・・・・・・環状
細隙、15・・・・・・板状体成型金型。
FIG. 1 is a partially cutaway top view showing an embodiment of a device suitable for use in the present invention. In the figure, the names of the main parts are as follows. 7... Outer mold, 8... Shaft, 12...
... Reinforcement fiber (glass fiber bundle), 81 ... Annular slit, 15 ... Plate-shaped body mold.

Claims (1)

【特許請求の範囲】[Claims] 1 相対的に回転又は反転している軸と外型との間に形
威される環状細隙に、補強繊維を含有する加熱溶融され
た熱可塑性樹脂を通過せしめた後、これを板状体戒型金
型に送給し押出すことを特徴とする繊維補強熱可塑性樹
脂板状体の製造方法。
1. After passing a heated and melted thermoplastic resin containing reinforcing fibers through an annular gap formed between a shaft and an outer mold that are relatively rotating or inverted, this is formed into a plate-shaped body. A method for manufacturing a fiber-reinforced thermoplastic resin plate, characterized by feeding the fiber into a mold and extruding it.
JP49013093A 1974-01-30 1974-01-30 How do you know what to do? Expired JPS5848333B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP49013093A JPS5848333B2 (en) 1974-01-30 1974-01-30 How do you know what to do?

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP49013093A JPS5848333B2 (en) 1974-01-30 1974-01-30 How do you know what to do?

Publications (2)

Publication Number Publication Date
JPS50107073A JPS50107073A (en) 1975-08-23
JPS5848333B2 true JPS5848333B2 (en) 1983-10-27

Family

ID=11823534

Family Applications (1)

Application Number Title Priority Date Filing Date
JP49013093A Expired JPS5848333B2 (en) 1974-01-30 1974-01-30 How do you know what to do?

Country Status (1)

Country Link
JP (1) JPS5848333B2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3404203A (en) * 1963-05-03 1968-10-01 Dow Chemical Co Method of extruding bi-helically oriented thermoplastic tube

Also Published As

Publication number Publication date
JPS50107073A (en) 1975-08-23

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