JPH0880576A - Method and apparatus for producing resin molding material - Google Patents

Method and apparatus for producing resin molding material

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Publication number
JPH0880576A
JPH0880576A JP6243241A JP24324194A JPH0880576A JP H0880576 A JPH0880576 A JP H0880576A JP 6243241 A JP6243241 A JP 6243241A JP 24324194 A JP24324194 A JP 24324194A JP H0880576 A JPH0880576 A JP H0880576A
Authority
JP
Japan
Prior art keywords
thermoplastic resin
fiber bundle
fiber
molding material
reinforced thermoplastic
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.)
Granted
Application number
JP6243241A
Other languages
Japanese (ja)
Other versions
JP2662853B2 (en
Inventor
Masamichi Taguchi
昌道 田口
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.)
Asahi Fiber Glass Co Ltd
Original Assignee
Asahi Fiber Glass 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 Asahi Fiber Glass Co Ltd filed Critical Asahi Fiber Glass Co Ltd
Priority to JP6243241A priority Critical patent/JP2662853B2/en
Publication of JPH0880576A publication Critical patent/JPH0880576A/en
Application granted granted Critical
Publication of JP2662853B2 publication Critical patent/JP2662853B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE: To stably produce a fiber reinforced thermoplastic resin material containing an inorg. long fiber as a reinforcing material and high in mechanical strength at high speed. CONSTITUTION: A continuous inorg. fiber bundle 12 is impregnated with a molten thermoplastic resin 14 and the excessive resin is pressed from the impregnated fiber bundle 12 by the squeezing bar 18 composed of at least one rod 28 arranged so as to cross the running direction of the fiber bundle 12, pref. at a right angle thereto and, thereafter, the impregnated fiber bundle 12 is shaped by a shaping device consisting of at least a pair of rollers 25 arranged so as to come into contact with the fiber bundle 12 on the opposite sides thereof to prepare a long fiber reinforced thermoplastic resin material. The process impregnating the fiber bundle 12 with the molten thermoplastic resin 14 and the process pressing the excessive resin from the fiber bundle by the squeezing bar 18 are pref. performed in an inert gas atmosphere. As the inorg. fiber, a glass fiber is pref. used.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、連続した無機繊維束を
強化材とした長繊維強化熱可塑性樹脂成形材料(L−F
RTP)の製造法及び製造装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a long fiber reinforced thermoplastic resin molding material (LF) using a continuous inorganic fiber bundle as a reinforcing material.
RTP) manufacturing method and manufacturing apparatus.

【0002】[0002]

【従来の技術】従来より、熱可塑性樹脂の剛性、耐熱性
等を改良するための手段として、ガラス繊維等の無機繊
維を補強材として配合することが行われている。
2. Description of the Related Art Conventionally, as a means for improving the rigidity, heat resistance and the like of a thermoplastic resin, blending of an inorganic fiber such as a glass fiber as a reinforcing material has been performed.

【0003】通常、このような補強材としては、樹脂の
含浸性の点から、チョップドストランドが多く用いられ
ている。このような、チョップドストランドを補強材と
する繊維強化熱可塑性樹脂成形材料は、長さ3〜6mm程
度のチョップドストランドと熱可塑性樹脂とを押出スク
リューで加熱混練して押出すことによりペレット化し、
このペレットを配合して樹脂の成形を行う方法により製
造されている。
Usually, chopped strands are often used as such reinforcing materials from the viewpoint of resin impregnation. Such a fiber-reinforced thermoplastic resin molding material using a chopped strand as a reinforcing material is pelletized by extruding a chopped strand having a length of about 3 to 6 mm and a thermoplastic resin by heating and kneading with an extrusion screw,
It is manufactured by a method of blending these pellets and molding a resin.

【0004】しかしながら、チョップドストランドを補
強材とする場合、次のような問題点があった。すなわ
ち、押出成形機でチョップドストランドと熱可塑性樹脂
とを加熱混練するときに、押出スクリューとチョップド
ストランドとの摩擦等により、チョップドストランドの
切断が起こる。また、繊維強化熱可塑性樹脂成形材料の
成形の際にも、射出成形機のスクリューとの摩擦によっ
て切断が起こるため、ガラス繊維が更に短く切断され、
当初3〜6mmであった繊維長が、最終的には0.05〜0.8
mm程度になってしまう。このため、成形品の機械的物
性、特に耐衝撃性を充分に向上させることができなかっ
た。
However, when chopped strands are used as a reinforcing material, there are the following problems. That is, when the chopped strands and the thermoplastic resin are heated and kneaded by the extruder, the chopped strands are cut due to friction between the extrusion screw and the chopped strands. Also, when molding the fiber-reinforced thermoplastic resin molding material, because the cutting occurs by friction with the screw of the injection molding machine, the glass fiber is cut further shorter,
Initially, the fiber length was 3-6 mm, but finally 0.05-0.8
mm. For this reason, the mechanical properties, especially the impact resistance, of the molded product could not be sufficiently improved.

【0005】上記問題点を解決するために、近年、例え
ば、特公昭52-10140号、特開昭63-264326 号、USP4,
439,387 号等に開示されているように、連続した無機繊
維に、溶融した熱可塑性樹脂を電線被覆法により含浸さ
せる方法が行われるようになっている。この方法の場
合、溶融樹脂が繊維束の内部にまで含浸しにくいという
問題があるので、上記公報においては、含浸のさせ方が
いろいろ研究されているが、その製造工程は一般的に、
含浸ダイにおいて、連続した繊維束に、溶融樹脂を含浸
させた後、含浸ダイの先端に設けられた所定の孔径をも
つノズル、スリット又はダイスを通すか、あるいは賦形
ダイを通して、余分な樹脂を取り除いて所定の繊維含有
率にするとともに所定形状にして、長繊維強化熱可塑性
樹脂成形材料としている。
In order to solve the above problems, recently, for example, Japanese Patent Publication No. 52-10140, Japanese Patent Application Laid-Open No. 63-264326, US Pat.
As disclosed in Japanese Patent No. 439,387, etc., a method has been employed in which continuous inorganic fibers are impregnated with a molten thermoplastic resin by an electric wire coating method. In the case of this method, there is a problem that the molten resin is difficult to impregnate even into the inside of the fiber bundle, so in the above publication, various methods of impregnation have been studied, but the manufacturing process is generally
In the impregnation die, after impregnating the continuous fiber bundle with the molten resin, pass through a nozzle having a predetermined hole diameter provided at the tip of the impregnation die, a slit or a die, or pass an excess resin through a shaping die. It is removed to obtain a predetermined fiber content and a predetermined shape to obtain a long fiber reinforced thermoplastic resin molding material.

【0006】図5には、従来の長繊維強化熱可塑性樹脂
成形材料の製造工程の一例が示され、図6には、従来の
製造工程に用いられるチョークバーを用いた引き抜き成
形用ダイの一例が示されている。図5、図6を併せて説
明すると、引き抜き成形用のダイ61に、図示しないロ
ービング、ケーキ等の回巻体から引き出されたガラス長
繊維の繊維束12を連続して供給するとともに、押出機
63から、溶融した熱可塑性樹脂14をダイ61に供給
し、ダイ61の内部で、チョークバー65により繊維束
12に張力を与え、繊維束12を解繊させた状態で熱可
塑性樹脂14を含浸させて、ノズル66から引き抜い
て、長繊維強化熱可塑性樹脂15とした後、冷却槽16
で冷却して熱可塑性樹脂14を硬化させ、次いで、引取
り機17により引取られる。
FIG. 5 shows an example of a manufacturing process of a conventional long fiber reinforced thermoplastic resin molding material, and FIG. 6 shows an example of a drawing die using a choke bar used in the conventional manufacturing process. It is shown. 5 and 6 together, a fiber bundle 12 of glass long fibers drawn out from a wound body such as a roving or cake (not shown) is continuously supplied to a drawing die 61 and an extruder. From 63, the molten thermoplastic resin 14 is supplied to the die 61, the tension is applied to the fiber bundle 12 by the choke bar 65 inside the die 61, and the thermoplastic resin 14 is impregnated with the fiber bundle 12 being opened. Then, after being pulled out from the nozzle 66 to obtain the long fiber reinforced thermoplastic resin 15, the cooling bath 16
Then, the thermoplastic resin 14 is hardened by cooling, and is then taken off by a take-off machine 17.

【0007】[0007]

【発明が解決しようとする課題】しかしながら、上記の
方法ではいずれも、高速で引き抜き成形を行うと、繊維
束にかなり大きな応力がかかるため、ダイ内において繊
維束中のモノフィラメントが切断され、いわゆる単糸切
れを起こしやすい。このため、切れたフィラメントがダ
イ内に蓄積して毛羽となり、この毛羽がダイの吐出口に
移動してノズル、スリット又はダイスを塞ぎ、繊維束の
引張抵抗が増してその破断を誘発しやすいという問題が
あった。したがって、高速成形時には、ダイを時々分解
して、ダイ内に蓄積した毛羽を除去する必要があり、高
速かつスムーズな連続生産を行うことは事実上困難であ
った。
However, in any of the above methods, when the drawing is performed at a high speed, a considerably large stress is applied to the fiber bundle, so that the monofilament in the fiber bundle is cut in the die, and the so-called monofilament is cut. Easy to break thread. Therefore, the broken filaments are accumulated in the die and become fluff, and the fluff moves to the discharge port of the die to close the nozzle, the slit, or the die, and the tensile resistance of the fiber bundle increases to easily induce the breakage. There was a problem. Therefore, at the time of high-speed molding, it is necessary to disassemble the die from time to time to remove fluff accumulated in the die, and it has been practically difficult to perform high-speed and smooth continuous production.

【0008】本発明は上記問題点に鑑みてなされたもの
で、その目的は、無機長繊維を補強材とする機械的強度
の高い繊維強化熱可塑性樹脂材料を、高速で安定して製
造するための製造法及び製造装置を提供することにあ
る。
The present invention has been made in view of the above problems, and an object thereof is to stably produce a fiber-reinforced thermoplastic resin material having high mechanical strength using inorganic long fibers as a reinforcing material at a high speed. To provide a manufacturing method and a manufacturing apparatus.

【0009】[0009]

【課題を解決するための手段】本発明者らは、上記目的
を達成するため鋭意研究した結果、連続した無機繊維の
繊維束に、溶融樹脂を含浸させた後、スクイズバーによ
り余分な樹脂を絞り取り、繊維束の走行方向に対して、
それぞれ反対側から接するように配置された少なくとも
一対のローラからなる賦形装置により賦形することによ
り、単糸切れを起こしにくくし、高速で安定して製造す
ることができることを見出し、本発明を完成させるに至
った。
Means for Solving the Problems The inventors of the present invention have conducted intensive studies to achieve the above object, and as a result, after impregnating a continuous inorganic fiber bundle with a molten resin, excess resin was squeezed with a squeeze bar. For the squeezing and the running direction of the fiber bundle,
The present invention was found to be one in which single yarn breakage is less likely to occur and stable production can be performed at high speed by performing shaping by a shaping device including at least a pair of rollers arranged so as to contact each other from opposite sides. It came to completion.

【0010】上記目的を達成するため、本発明による長
繊維強化熱可塑性樹脂成形材料の製造法は、連続した無
機繊維の繊維束に、溶融した熱可塑性樹脂を含浸させた
後、賦形する長繊維強化熱可塑性樹脂成形材料の製造法
において、前記繊維束に前記熱可塑性樹脂を含浸させる
工程と、前記溶融した熱可塑性樹脂の樹脂面より上方に
あって、前記繊維束の走行方向に対して交差するように
配設された少なくとも1本の棒からなるスクイズバーに
より余分な樹脂を絞り取る工程と、前記繊維束の走行方
向に対して、それぞれ反対側から接するように配置され
た少なくとも一対のローラからなる賦形装置により賦形
する工程とを含むことを特徴とする。
In order to achieve the above-mentioned object, the method for producing a long fiber reinforced thermoplastic resin molding material according to the present invention is such that a continuous fiber bundle of inorganic fibers is impregnated with a molten thermoplastic resin and then shaped. In the method for producing a fiber-reinforced thermoplastic resin molding material, a step of impregnating the fiber bundle with the thermoplastic resin, and above the resin surface of the molten thermoplastic resin, with respect to the running direction of the fiber bundle A step of squeezing out excess resin by a squeeze bar composed of at least one rod arranged so as to intersect, and at least a pair of at least one pair arranged so as to come into contact with each other from the opposite side with respect to the running direction of the fiber bundle. And a step of performing shaping by a shaping device including a roller.

【0011】また、本発明の長繊維強化熱可塑性樹脂成
形材料の製造装置は、連続した無機繊維の繊維束に、溶
融した熱可塑性樹脂を含浸させた後、賦形して長繊維強
化熱可塑性樹脂成形材料を製造する装置において、前記
熱可塑性樹脂が流入する樹脂流入口と、前記熱可塑性樹
脂が貯留される含浸槽と、前記繊維束を導入して前記含
浸槽に導く導入口と、前記含浸槽から前記繊維束を取り
出す導出口と、この導出口において前記繊維束の走行方
向に対して交差するように配設された少なくとも1本の
棒からなるスクイズバーとを有する塗布装置と、前記ス
クイズバーを経て前記塗布装置から取り出される前記繊
維束の走行方向に対して、それぞれ反対側から接するよ
うに配置された少なくとも一対のローラからなる賦形装
置とを備えていることを特徴とする。
In addition, the apparatus for producing a long-fiber-reinforced thermoplastic resin molding material of the present invention impregnates a continuous fiber bundle of inorganic fibers with a molten thermoplastic resin and then shapes the fiber bundle to form a long-fiber-reinforced thermoplastic resin. In an apparatus for producing a resin molding material, a resin inflow port into which the thermoplastic resin flows, an impregnation tank in which the thermoplastic resin is stored, and an introduction port for introducing the fiber bundle and leading to the impregnation tank, An outlet for taking out the fiber bundle from the impregnation tank, and a coating device having a squeeze bar including at least one rod disposed so as to intersect the running direction of the fiber bundle at the outlet. A shaping device including at least a pair of rollers disposed so as to be in contact with each other from the opposite side with respect to the traveling direction of the fiber bundle taken out of the coating device through a squeeze bar. And wherein the door.

【0012】以下、本発明について好ましい態様を挙げ
て詳細に説明する。
Hereinafter, the present invention will be described in detail with reference to preferred embodiments.

【0013】本発明に使用する熱可塑性樹脂としては、
特に限定されないが、例えば、ポリエチレン、ポリプロ
ピレン、ナイロン、PET(ポリエチレンテレフタレー
ト)、PBT(ポリブチレンテレフタレート)、ポリス
チレン、AS(アクリルニトリルスチレン樹脂)、AB
S(アクリルニトリルブタジエンスチレン樹脂)、PE
I(ポリエーテルイミド)、PEEK(ポリエーテルエ
ーテルケトン)等が好ましく用いられる。本発明では、
上記のような樹脂を単独で用いてもよく、2種以上混合
して用いてもよい。また、熱可塑性樹脂には、用途や成
形条件に応じて、着色剤、改良剤、無機繊維以外の充填
材等、公知の添加剤を適宜含有させることができ、これ
らは常法に従い混練使用される。
[0013] The thermoplastic resin used in the present invention includes:
Although not particularly limited, for example, polyethylene, polypropylene, nylon, PET (polyethylene terephthalate), PBT (polybutylene terephthalate), polystyrene, AS (acrylonitrile styrene resin), AB
S (acrylonitrile butadiene styrene resin), PE
I (polyether imide), PEEK (polyether ether ketone) and the like are preferably used. In the present invention,
The above resins may be used alone or in combination of two or more. Further, the thermoplastic resin may appropriately contain known additives such as a colorant, an improving agent, and a filler other than the inorganic fiber depending on the use and molding conditions, and these are kneaded and used according to a conventional method. It

【0014】本発明において、連続した無機繊維の繊維
束としては、ケーキ、ロービング等の回捲体から引き出
されたガラス繊維、カーボン繊維等が好ましく使用され
る。これらのうち、Eガラス、Sガラス等の市販のガラ
ス繊維を用いると、コスト的にも有利であり、より好ま
しい。繊維束の集束本数は、取り扱い性や、溶融樹脂が
含浸される際の開繊性等を考慮して、100 〜4000本程度
とするのが好ましい。なお、一般的に、ガラス繊維に
は、ハンドリングの改善、複合化の際のマトリックスと
の接着性の改善等のために、種々の表面処理が施されて
いるが、これらの種類は、使用する熱可塑性の樹脂に応
じて選択すればよい。
In the present invention, as the continuous fiber bundle of inorganic fibers, glass fibers, carbon fibers and the like drawn from a wound body such as cake and roving are preferably used. Among these, the use of commercially available glass fibers such as E glass and S glass is more advantageous in terms of cost and is more preferable. The number of bundles of the fiber bundles is preferably about 100 to 4,000 in consideration of handleability, spreadability when the molten resin is impregnated, and the like. In general, glass fibers are subjected to various surface treatments for improving handling, improving adhesiveness with a matrix during compounding, etc., but these types are used. It may be selected according to the thermoplastic resin.

【0015】本発明の長繊維強化熱可塑性樹脂成形材料
の製造装置は、例えば図1、図2によって示される装置
によって基本的に構成される。図1は一部断面側面図、
図2は平面図である。
An apparatus for producing a long-fiber-reinforced thermoplastic resin molding material of the present invention is basically constituted by an apparatus shown in FIGS. 1 and 2, for example. FIG. 1 is a partial cross-sectional side view,
FIG. 2 is a plan view.

【0016】図1、図2において、図示しない回巻体等
から引き出された連続した無機繊維の繊維束12を、塗
布装置11に導入して、溶融した熱可塑性樹脂14を含
浸させ、スクイズバー18により余分な樹脂14を絞り
取った後、賦形装置19により賦形する。こうして得ら
れた長繊維強化熱可塑性樹脂15は、通常の工程通り、
冷却槽16で冷却し、引取り機17で引き取って長繊維
強化熱可塑性樹脂成形材料とされる。
In FIGS. 1 and 2, a continuous fiber bundle 12 of inorganic fibers drawn from a winding body or the like (not shown) is introduced into a coating device 11 to be impregnated with a molten thermoplastic resin 14, and a squeeze bar. After the excess resin 14 is squeezed out by 18, the shaping is performed by the shaping device 19. The long fiber reinforced thermoplastic resin 15 thus obtained is subjected to a usual process,
It is cooled in a cooling tank 16 and taken off by a take-off machine 17 to obtain a long fiber reinforced thermoplastic resin molding material.

【0017】塗布装置11は、熱可塑性樹脂14が流入
する樹脂流入口21と、熱可塑性樹脂14が貯留される
含浸槽22と、繊維束12を導入して含浸槽22に導く
導入口23と、含浸槽22から熱可塑性樹脂14が含浸
された繊維束12を取り出す導出口24と、この導出口
24において繊維束12の走行方向に対して交差するよ
うに、好ましくは直角に配設された少なくとも1本の棒
28からなるスクイズバー18とから構成される。な
お、導入口23は、例えば3mm×12mm程度のスリット
状の孔が好ましく採用される。また、導出口24は、熱
可塑性樹脂14が含浸された繊維束12を取り出すだけ
で、余分な樹脂14を絞り取ったり、賦形したりする機
能は必要なく、したがって、従来のようなノズル、スリ
ット又はダイス状ではない。
The coating device 11 includes a resin inlet 21 into which the thermoplastic resin 14 flows, an impregnation tank 22 in which the thermoplastic resin 14 is stored, and an inlet 23 that introduces the fiber bundle 12 and guides it to the impregnation tank 22. The outlet 24 for taking out the fiber bundle 12 impregnated with the thermoplastic resin 14 from the impregnation tank 22 and the outlet 24 are arranged at right angles so as to intersect the traveling direction of the fiber bundle 12. And a squeeze bar 18 including at least one rod 28. In addition, as the inlet 23, a slit-like hole of, for example, about 3 mm × 12 mm is preferably adopted. In addition, the outlet 24 only needs to take out the fiber bundle 12 impregnated with the thermoplastic resin 14 and does not need to have a function of squeezing out the excess resin 14 or shaping it. Not slit or die-shaped.

【0018】そして、含浸槽14及びスクイズバー18
が、不活性ガス雰囲気槽20で覆われ、ガス導入口26
から不活性ガス27が導入されている。したがって、繊
維束12に熱可塑性樹脂14を含浸させる工程と、スク
イズバー18により余分な樹脂14を絞り取る工程と
は、不活性ガス27の雰囲気下に行なわれる。不活性ガ
ス雰囲気槽20は、必ず必要というものではないが、設
けておくと、溶融した熱可塑性樹脂14は酸化劣化を防
止することができるのでより好ましい。不活性ガス27
としては、窒素、アルゴン、ヘリウム等が好ましく用い
られる。
Then, the impregnation tank 14 and the squeeze bar 18
Is covered with the inert gas atmosphere tank 20, and the gas inlet 26
, An inert gas 27 is introduced. Therefore, the step of impregnating the fiber bundle 12 with the thermoplastic resin 14 and the step of squeezing out the excess resin 14 with the squeeze bar 18 are performed in an atmosphere of the inert gas 27. The inert gas atmosphere tank 20 is not always necessary, but is preferably provided because the molten thermoplastic resin 14 can be prevented from being oxidized and degraded. Inert gas 27
As such, nitrogen, argon, helium and the like are preferably used.

【0019】図1、図2に示される塗布装置11におい
ては、繊維束12を、熱可塑性樹脂14が貯留される含
浸槽22に浸漬することにより熱可塑性樹脂14が含浸
されるプルトルージョン法を採用したが、この方法に限
定されず、そのほか、ホットメルトロールコータ等を用
いて含浸させてもよい。また、溶融した熱可塑性樹脂1
4の粘度が高い場合には、含浸槽22内に、チョークバ
ーを設けておくとより好ましい。
In the coating apparatus 11 shown in FIGS. 1 and 2, the fiber bundle 12 is immersed in an impregnation tank 22 in which the thermoplastic resin 14 is stored, so that the thermoplastic resin 14 is impregnated. Although adopted, it is not limited to this method, and it may be impregnated using a hot melt roll coater or the like. The molten thermoplastic resin 1
When the viscosity of No. 4 is high, it is more preferable to provide a choke bar in the impregnation tank 22.

【0020】スクイズバー18は、繊維束12の走行方
向に対して好ましくは直角に配設された少なくとも1本
の棒28からなり、導出口24の上部に配設される。棒
28の形状は、繊維束12との接触面が平滑な曲面を有
しているものが好ましく、例えば、その断面が円、楕
円、半円等であるものが好ましい。また、その材質、
径、本数等は特に限定されず使用する熱可塑性樹脂14
の種類、得ようとする繊維含有率等に応じて選択され
る。なお、棒28を複数本使用する場合には、繊維束1
2をその間を縫うように交互に通すと、余分な熱可塑性
樹脂14を効率的に絞り取ることができる。
The squeeze bar 18 is composed of at least one rod 28 arranged at right angles to the traveling direction of the fiber bundle 12, and is arranged above the outlet 24. The shape of the rod 28 is preferably such that the contact surface with the fiber bundle 12 has a smooth curved surface, and for example, the cross section thereof is preferably a circle, an ellipse, a semicircle, or the like. Also, its material,
The diameter, the number, etc. are not particularly limited, and the thermoplastic resin 14 to be used
Is selected according to the type of the fiber, the fiber content to be obtained, and the like. When using a plurality of rods 28, the fiber bundle 1
By alternately passing the two so as to sew between them, the excess thermoplastic resin 14 can be efficiently squeezed out.

【0021】本発明に用いる賦形装置19は、スクイズ
バー18を経て塗布装置11から取り出される繊維束1
2、すなわち、硬化されていない長繊維強化熱可塑性樹
脂15の走行方向に対して、それぞれ反対側から接する
ように配置された少なくとも一対のローラ25、25か
らなる。このローラ25、25の間を通過させることに
より、円形ロッド状、テープ状等、所望の形状に賦形す
ることができる。この実施例では、このローラ25、2
5は、中央部が円弧状の凹部とされ、長繊維強化熱可塑
性樹脂15を水平方向から円形ロッド状に賦形するよう
にされている。しかし、ローラ25の形状、配置位置
は、これに限定されず、例えば、図3に側面図、図4に
平面図が示されるように、円筒形状のローラ29、29
により、長繊維強化熱可塑性樹脂15を上下方向から賦
形する形状等であってもよい。この場合、長繊維強化熱
可塑性樹脂15はテープ状に賦形される。
The shaping device 19 used in the present invention is a fiber bundle 1 taken out from the coating device 11 via the squeeze bar 18.
2, that is, at least one pair of rollers 25, 25 arranged to be in contact with the running direction of the uncured long fiber reinforced thermoplastic resin 15 from opposite sides. By passing between the rollers 25, 25, a desired shape such as a circular rod shape or a tape shape can be formed. In this embodiment, the rollers 25, 2
5 has an arcuate recess at the center, and is configured to shape the long fiber reinforced thermoplastic resin 15 from the horizontal direction into a circular rod shape. However, the shape and arrangement position of the roller 25 are not limited to this, and for example, as shown in the side view of FIG. 3 and the plan view of FIG.
Accordingly, the long-fiber-reinforced thermoplastic resin 15 may be shaped in a vertical direction. In this case, the long fiber reinforced thermoplastic resin 15 is shaped like a tape.

【0022】本発明の特徴は、上記したスクイズバー1
8を配設した塗布装置11及び賦形装置19にあり、そ
のほかの冷却槽16、引取り機17等は通常のものをそ
のまま使用することができる。
A feature of the present invention is that the squeeze bar 1 described above is used.
8 are provided in the coating device 11 and the shaping device 19, and other cooling tanks 16, take-up devices 17, etc. can be used as they are.

【0023】[0023]

【作用】本発明によれば、連続した無機繊維の繊維束
に、溶融した熱可塑性樹脂を含浸させた後、スクイズバ
ーにより余分な樹脂を絞り取り、繊維束の走行方向に対
して、それぞれ反対側から接するように配置された少な
くとも一対のローラからなる賦形装置により賦形するの
で、高速で引き取っても単糸切れを起こしにくく、した
がって、長繊維強化熱可塑性樹脂成形材料を、高速で安
定して製造することができる。
According to the present invention, a continuous inorganic fiber bundle is impregnated with a molten thermoplastic resin, and then excess resin is squeezed out with a squeeze bar. Since shaping is performed by a shaping device consisting of at least a pair of rollers arranged so as to be in contact from the side, single yarn breakage is unlikely to occur even when pulled at high speed, and therefore, the long fiber reinforced thermoplastic resin molding material can be stabilized at high speed. Can be manufactured.

【0024】また、好ましい態様において、含浸槽及び
スクイズバーが、不活性ガス雰囲気下に配設されている
場合、繊維束に熱可塑性樹脂を含浸させる工程と、スク
イズバーにより余分な樹脂を絞り取る工程とが、不活性
ガス雰囲気下に行われるので、溶融した熱可塑性樹脂の
酸化劣化を防止することができ、高品質の長繊維強化熱
可塑性樹脂成形材料を製造することができる。
Further, in a preferred embodiment, when the impregnation tank and the squeeze bar are arranged in an inert gas atmosphere, a step of impregnating the fiber bundle with the thermoplastic resin and a squeeze bar to squeeze out excess resin Since the step and the step are performed in an inert gas atmosphere, it is possible to prevent oxidative deterioration of the molten thermoplastic resin, and it is possible to produce a high-quality long fiber reinforced thermoplastic resin molding material.

【0025】[0025]

【実施例】【Example】

実施例1 前記した図1、図2に示す装置を用いて、長繊維強化熱
可塑性樹脂成形材料を製造した。
Example 1 A long fiber reinforced thermoplastic resin molding material was produced using the apparatus shown in FIGS. 1 and 2 described above.

【0026】連続した無機繊維の繊維束12として、繊
維径13μmのEガラス繊維を800 本集束させた繊維束13
本を引き揃えたものを用い、熱可塑性樹脂14としてポ
リプロピレン樹脂を用いた。
As a continuous fiber bundle 12 of inorganic fibers, a fiber bundle 13 in which 800 E glass fibers having a fiber diameter of 13 μm are bundled
A book obtained by arranging books was used, and a polypropylene resin was used as the thermoplastic resin 14.

【0027】また、スクイズバー18としては、8mmφ
のガラス棒を15mmピッチで、繊維束12の走行方向に対
して直角に5本配列させたものを用いた。
As the squeeze bar 18, 8 mmφ
The five glass rods were arranged at a pitch of 15 mm at right angles to the running direction of the fiber bundle 12.

【0028】不活性ガス雰囲気槽20は、アクリル製の
箱体とし、ガス導入口26から、1m3/minで、窒素ガス
を流入させた。
The inert gas atmosphere tank 20 was an acrylic box, and nitrogen gas was introduced from the gas inlet 26 at 1 m 3 / min.

【0029】賦形装置19としては、塗布装置11から
取り出される繊維束12、すなわち、硬化されていない
長繊維強化熱可塑性樹脂15の走行方向に対して、それ
ぞれ反対側から接するように左右に配置された、中央部
が円弧状の凹部を有する一対のローラ25、25からな
るものを用いた。
As the shaping device 19, the fiber bundles 12 taken out from the coating device 11, that is, the left and right sides are arranged so as to come in contact with the running direction of the uncured long fiber reinforced thermoplastic resin 15 from opposite sides. A pair of rollers 25 having a circular arc-shaped concave portion was used.

【0030】冷却槽16、引取り機17は従来から用い
られている通常のものを用い、引取り速度は60m/min と
した。
The cooling tank 16 and the take-up machine 17 used were conventional ones, and the take-up speed was 60 m / min.

【0031】上記の条件により、繊維束12を、含浸槽
22に導入し、樹脂14を含浸させ、スクイズバー18
で余分な樹脂を絞り取った後、賦形装置19で賦形し、
冷却槽16、引取り機17を通して、ガラス含有率が72
wt%で、円形ロッド状の長繊維強化熱可塑性樹脂成形
材料を得た。
Under the above conditions, the fiber bundle 12 is introduced into the impregnation tank 22, the resin 14 is impregnated, and the squeeze bar 18 is added.
After squeezing out the excess resin with, it is shaped with the shaping device 19,
The glass content was reduced to 72 through the cooling tank 16 and the take-off machine 17.
A long rod reinforced thermoplastic resin molding material in the form of a circular rod was obtained in wt%.

【0032】次いで、得られた長繊維強化熱可塑性樹脂
成形材料を6mmの長さに切断した。この切断物をマスタ
ーバッチ用のペレットとして、ポリプロピレンを所定量
添加し、射出成形機にて、ガラス含有率20wt%の試験
片を得た。
Then, the obtained long fiber reinforced thermoplastic resin molding material was cut into a length of 6 mm. A predetermined amount of polypropylene was added to the cut product as pellets for a masterbatch, and a test piece having a glass content of 20 wt% was obtained by an injection molding machine.

【0033】実施例2 実施例1において、賦形装置19を、図3、図4に示さ
れる、硬化されていない長繊維強化熱可塑性樹脂15の
走行方向に対して、それぞれ反対側から接するように上
下に配置された、円筒状の一対のローラ29、29から
なるものに替えて、長繊維強化熱可塑性樹脂15を幅約
6mm、厚さ約0.3 mmのテープ状に賦形し、あとは実施例
1と同様の材料、装置、条件により、ガラス含有率が73
wt%で、テープ状の長繊維強化熱可塑性樹脂成形材料
を得た。
Embodiment 2 In Embodiment 1, the shaping apparatus 19 is brought into contact with the running direction of the uncured long fiber reinforced thermoplastic resin 15 shown in FIGS. In place of a pair of cylindrical rollers 29, 29 arranged vertically, a long fiber reinforced thermoplastic resin 15 is shaped into a tape having a width of about 6 mm and a thickness of about 0.3 mm. With the same materials, equipment and conditions as in Example 1, the glass content was 73
A tape-shaped long-fiber-reinforced thermoplastic resin molding material was obtained with a wt%.

【0034】得られた長繊維強化熱可塑性樹脂成形材料
を、実施例1と同様に処理して試験片を得た。
The obtained long-fiber-reinforced thermoplastic resin molding material was treated in the same manner as in Example 1 to obtain a test piece.

【0035】比較例1 図5、図6に示す装置を用い、実施例1と同様の繊維束
12、熱可塑性樹脂14を用いて、長繊維強化熱可塑性
樹脂成形材料を製造した。
Comparative Example 1 A long fiber reinforced thermoplastic resin molding material was produced by using the apparatus shown in FIGS. 5 and 6 and using the same fiber bundle 12 and thermoplastic resin 14 as in Example 1.

【0036】ダイ61に設けられたノズル66の径は2.
0 mmφとした。
The diameter of the nozzle 66 provided on the die 61 is 2.
0 mmφ.

【0037】上記の条件により、繊維束12を、含浸槽
22に導入し、樹脂14を含浸させ、ノズル66を通し
て余分な樹脂14を絞り取るとともに、賦形し、冷却槽
16、引取り機17を通して、ガラス含有率72wt%、
円形ロッド状の長繊維強化熱可塑性樹脂成形材料を得
た。なお、引取り速度は20m/min とした。
Under the above conditions, the fiber bundle 12 is introduced into the impregnation tank 22, impregnated with the resin 14, and the excess resin 14 is squeezed through the nozzle 66 and shaped, and the cooling tank 16 and the take-up machine 17 are provided. Through, glass content rate 72 wt%,
A circular rod shaped long fiber reinforced thermoplastic resin molding material was obtained. The take-up speed was 20 m / min.

【0038】得られた長繊維強化熱可塑性樹脂成形材料
を、実施例1と同様に処理して試験片を得た。
The obtained long-fiber-reinforced thermoplastic resin molding material was treated in the same manner as in Example 1 to obtain a test piece.

【0039】比較例2 比較例1において、引取り速度を40m/min に替え、あと
は比較例1と同様にして、長繊維強化熱可塑性樹脂成形
材料を得、比較例と同様に処理して試験片を得た。
Comparative Example 2 In Comparative Example 1, the take-up speed was changed to 40 m / min, and the long fiber-reinforced thermoplastic resin molding material was obtained in the same manner as in Comparative Example 1 and treated in the same manner as in Comparative Example. A test piece was obtained.

【0040】試験例 実施例1、2、及び比較例1、2で得られた試験片につ
いて、繊維の分散状態を観察した。その結果を表1に示
す。
Test Examples The test pieces obtained in Examples 1 and 2 and Comparative Examples 1 and 2 were observed for fiber dispersion. The results are shown in Table 1.

【0041】[0041]

【表1】 表中、PPはポリプロピレンを表す。[Table 1] In the table, PP represents polypropylene.

【0042】表1の結果から、本発明の装置を用いて本
発明の製造法により製造した実施例1、2の試験片は、
繊維の分散性が良好な状態で、引取り速度60m/min で引
取っても引取り時の繊維の破断はないが、従来の装置を
用いた比較例1、2においては、いずれも繊維の分散性
は良好であるが、比較例2のように、引取り速度40m/mi
n で引取ると、引取り時に繊維の破断が生じることがわ
かる。
From the results of Table 1, the test pieces of Examples 1 and 2 produced by the production method of the present invention using the apparatus of the present invention,
In the state where the fiber dispersibility is good, there is no breakage of the fiber at the time of drawing at a drawing speed of 60 m / min. However, in Comparative Examples 1 and 2 using the conventional apparatus, all of the fibers were broken. The dispersibility is good, but as in Comparative Example 2, the take-off speed is 40 m / mi.
It can be seen that when the fiber is taken at n, the fiber breaks at the time of taking.

【0043】[0043]

【発明の効果】以上説明したように、本発明によれば、
連続した無機繊維の繊維束に、溶融した熱可塑性樹脂を
含浸させ、スクイズバーにより余分な樹脂を絞り取った
後、繊維束の走行方向に対して、それぞれ反対側から接
するように配置された少なくとも一対のローラからなる
賦形装置により賦形することにより、無機長繊維を補強
材とする機械的強度の高い繊維強化熱可塑性樹脂材料
を、高速で安定して製造することができる。
As described above, according to the present invention,
A fiber bundle of continuous inorganic fibers is impregnated with a molten thermoplastic resin, and after squeezing excess resin with a squeeze bar, at least so arranged that they are in contact with each other from the opposite side with respect to the running direction of the fiber bundle. By performing shaping with a shaping device including a pair of rollers, a fiber-reinforced thermoplastic resin material having high mechanical strength and using inorganic long fibers as a reinforcing material can be stably manufactured at high speed.

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

【図1】本発明の長繊維強化熱可塑性樹脂成形材料の製
造装置の一実施例を示す一部断面側面図である。
FIG. 1 is a partial cross-sectional side view showing one embodiment of a manufacturing apparatus of a long fiber reinforced thermoplastic resin molding material of the present invention.

【図2】同実施例を示す平面図である。FIG. 2 is a plan view showing the same embodiment.

【図3】本発明の長繊維強化熱可塑性樹脂成形材料の製
造装置に用いる賦形装置の他の実施例を示す側面図であ
る。
FIG. 3 is a side view showing another embodiment of the shaping apparatus used in the apparatus for producing a long fiber reinforced thermoplastic resin molding material of the present invention.

【図4】同実施例を示す平面図である。FIG. 4 is a plan view showing the same embodiment.

【図5】従来の長繊維強化熱可塑性樹脂成形材料の製造
工程の一例を示す概略図である。
FIG. 5 is a schematic view showing an example of a production process of a conventional long fiber reinforced thermoplastic resin molding material.

【図6】従来の長繊維強化熱可塑性樹脂成形材料の製造
装置に用いる含浸ダイの一例を示す断面図である。
FIG. 6 is a cross-sectional view showing an example of an impregnation die used in a conventional apparatus for manufacturing a long fiber reinforced thermoplastic resin molding material.

【符号の説明】[Explanation of symbols]

11 塗布装置 12 繊維束 14 熱可塑性樹脂 15 長繊維強化熱可塑性樹脂 16 冷却槽 17 引取り機 18 スクイズバー 19 賦形装置 20 不活性ガス雰囲気槽 21 樹脂流入口 22 含浸槽 23 導入口 24 導出口 25、29 ローラ 27 不活性ガス 28 棒 REFERENCE SIGNS LIST 11 coating device 12 fiber bundle 14 thermoplastic resin 15 long fiber reinforced thermoplastic resin 16 cooling tank 17 take-off machine 18 squeeze bar 19 shaping device 20 inert gas atmosphere tank 21 resin inlet 22 impregnation tank 23 inlet 24 outlet 25, 29 Roller 27 Inert gas 28 bar

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 連続した無機繊維の繊維束に、溶融した
熱可塑性樹脂を含浸させた後、賦形する長繊維強化熱可
塑性樹脂成形材料の製造法において、前記繊維束に前記
熱可塑性樹脂を含浸させる工程と、前記溶融した熱可塑
性樹脂の樹脂面より上方にあって、前記繊維束の走行方
向に対して交差するように配設された少なくとも1本の
棒からなるスクイズバーにより余分な樹脂を絞り取る工
程と、前記繊維束の走行方向に対して、それぞれ反対側
から接するように配置された少なくとも一対のローラか
らなる賦形装置により賦形する工程とを含むことを特徴
とする長繊維強化熱可塑性樹脂成形材料の製造法。
1. A method for producing a long fiber reinforced thermoplastic resin molding material, in which a continuous inorganic fiber fiber bundle is impregnated with a molten thermoplastic resin, and then the thermoplastic resin is added to the fiber bundle. An impregnating step, and an excess resin by a squeeze bar consisting of at least one rod disposed above the resin surface of the molten thermoplastic resin and arranged to intersect the running direction of the fiber bundle. Squeezing, and shaping with a shaping device comprising at least a pair of rollers arranged so as to be in contact with each other from the opposite side with respect to the running direction of the fiber bundle. Manufacturing method of reinforced thermoplastic resin molding material.
【請求項2】 前記繊維束に前記熱可塑性樹脂を含浸さ
せる工程と、前記スクイズバーにより余分な樹脂を絞り
取る工程とを、不活性ガス雰囲気下に行う請求項1記載
の長繊維強化熱可塑性樹脂成形材料の製造法。
2. The long fiber reinforced thermoplastic according to claim 1, wherein the step of impregnating the fiber bundle with the thermoplastic resin and the step of squeezing off the excess resin with the squeeze bar are performed under an inert gas atmosphere. Manufacturing method of resin molding material.
【請求項3】 前記無機繊維がガラス繊維である請求項
1又は2記載の長繊維強化熱可塑性樹脂成形材料の製造
法。
3. The method for producing a long fiber reinforced thermoplastic resin molding material according to claim 1, wherein the inorganic fibers are glass fibers.
【請求項4】 連続した無機繊維の繊維束に、溶融した
熱可塑性樹脂を含浸させた後、賦形して長繊維強化熱可
塑性樹脂成形材料を製造する装置において、前記熱可塑
性樹脂が流入する樹脂流入口と、前記熱可塑性樹脂が貯
留される含浸槽と、前記繊維束を導入して前記含浸槽に
導く導入口と、前記含浸槽から前記繊維束を取り出す導
出口と、この導出口において前記繊維束の走行方向に対
して交差するように配設された少なくとも1本の棒から
なるスクイズバーとを有する塗布装置と、 前記スクイズバーを経て前記塗布装置から取り出される
前記繊維束の走行方向に対して、それぞれ反対側から接
するように配置された少なくとも一対のローラからなる
賦形装置とを備えていることを特徴とする長繊維強化熱
可塑性樹脂成形材料の製造装置。
4. A device for producing a continuous fiber-reinforced thermoplastic resin molding material by impregnating a continuous fiber bundle of a molten inorganic resin with a molten thermoplastic resin, and then injecting the thermoplastic resin. A resin inlet, an impregnation tank in which the thermoplastic resin is stored, an inlet for introducing the fiber bundle to the impregnation tank, an outlet for taking out the fiber bundle from the impregnation tank, and an outlet for this. A coating device having a squeeze bar composed of at least one rod arranged so as to intersect the traveling direction of the fiber bundle, and a traveling direction of the fiber bundle taken out of the coating device via the squeeze bar. And a shaping device including at least a pair of rollers arranged so as to contact with each other from opposite sides, respectively, for manufacturing a long fiber reinforced thermoplastic resin molding material.
【請求項5】 前記含浸槽及び前記スクイズバーが、内
部に不活性ガスを導入される槽で覆われている請求項4
記載の長繊維強化熱可塑性樹脂成形材料の製造装置。
5. The impregnation tank and the squeeze bar are covered with a tank into which an inert gas is introduced.
An apparatus for producing the long-fiber-reinforced thermoplastic resin molding material as described above.
JP6243241A 1994-09-12 1994-09-12 Manufacturing method and manufacturing apparatus for long fiber reinforced thermoplastic resin molding material Expired - Fee Related JP2662853B2 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103072292A (en) * 2013-01-09 2013-05-01 金发科技股份有限公司 Molding device and preparation method for long fiber-reinforced nylon
KR20160054661A (en) * 2014-11-06 2016-05-17 한화첨단소재 주식회사 Complex materials with unidirectional continuous fiber reinforced thermoplasticity resins, apparatus and method for manufacturing the same
WO2020071923A1 (en) * 2018-10-05 2020-04-09 Comrod As Apparatus and method for controlling a quantity of binder resine that follows a thread

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103072292A (en) * 2013-01-09 2013-05-01 金发科技股份有限公司 Molding device and preparation method for long fiber-reinforced nylon
KR20160054661A (en) * 2014-11-06 2016-05-17 한화첨단소재 주식회사 Complex materials with unidirectional continuous fiber reinforced thermoplasticity resins, apparatus and method for manufacturing the same
WO2020071923A1 (en) * 2018-10-05 2020-04-09 Comrod As Apparatus and method for controlling a quantity of binder resine that follows a thread
US11820705B2 (en) 2018-10-05 2023-11-21 Comrod As Apparatus and method for controlling a quantity of binder resin that follows a thread

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