JPH0530783B2 - - Google Patents
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- Publication number
- JPH0530783B2 JPH0530783B2 JP1281781A JP28178189A JPH0530783B2 JP H0530783 B2 JPH0530783 B2 JP H0530783B2 JP 1281781 A JP1281781 A JP 1281781A JP 28178189 A JP28178189 A JP 28178189A JP H0530783 B2 JPH0530783 B2 JP H0530783B2
- Authority
- JP
- Japan
- Prior art keywords
- glass fiber
- fiber bundle
- fiber bundles
- molding material
- sizing agent
- 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 - Lifetime
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- Reinforced Plastic Materials (AREA)
- Surface Treatment Of Glass Fibres Or Filaments (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
- Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、繊維補強熱可塑性樹脂体(FRTP)
の製造に有用な成型材料の製造方法に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a fiber reinforced thermoplastic resin body (FRTP).
The present invention relates to a method of manufacturing a molding material useful for manufacturing.
FRTPはガラス繊維のような補強繊維と熱可塑
性樹脂を含むペレツト(繊維含有ペレツト)を原
料とし、射出成型法によつて製造される。
FRTP is manufactured by injection molding using pellets (fiber-containing pellets) containing reinforcing fibers such as glass fibers and thermoplastic resin.
繊維含有ペレツトは通常補強繊維切断物(例え
ばチヨツプドストランド、CSと略称)と熱可塑
性樹脂を加熱下に混練することによつて製造され
るが、混練操作中に補強繊維が寸断され易く、こ
のため、このペレツトを使用して得られたFRTP
の強度が低下する難点がある。 Fiber-containing pellets are usually produced by kneading cut reinforcing fibers (for example, chopped strands, abbreviated as CS) and thermoplastic resin under heat, but the reinforcing fibers are likely to be shredded during the kneading operation. , therefore, the FRTP obtained using this pellet
The problem is that the strength of the material decreases.
上記難点を解消するため、ストランド、ロービ
ングのような連続したガラス繊維束に熱可塑性樹
脂を被着させた後、切断して繊維含有ペレツトを
製造する方法(長尺法と呼ぶ)が提案されて長尺
法においては連続したガラス繊維束が使用される
が、工業的にはガラス繊維束を円筒状に回巻した
回巻体(円筒状回巻体)が使用され、ガラス繊維
束は円筒状回巻体から引出され、熱可塑性樹脂被
着装置に連続して供給される。 In order to overcome the above-mentioned difficulties, a method has been proposed in which continuous glass fiber bundles such as strands or rovings are coated with thermoplastic resin and then cut to produce fiber-containing pellets (referred to as the long length method). Continuous glass fiber bundles are used in the long method, but industrially, a cylindrical wound body (cylindrical wound body) of glass fiber bundles is used; It is drawn out from the roll and continuously fed to a thermoplastic resin coating device.
ガラス繊維束が水分を含有していると、この水
分がFRTP成型の際気化しFRTPの性能が低下す
るので、円筒状回巻体としては予め乾燥したも
の、例えばタイプ30のような直捲ロービング回
巻体が使用される。 If the glass fiber bundle contains moisture, this moisture will evaporate during FRTP molding and the performance of FRTP will deteriorate. Therefore, the cylindrical wound body should be a pre-dried one, such as a direct-wound roving such as Type 30. A rolled body is used.
従来の長尺法は、次のような問題点を有する。 The conventional long length method has the following problems.
乾燥した円筒状回巻体からガラス繊維束を引出
し、熱可塑性樹脂被着装置へ送る間に、ガラス繊
維にも毛羽立ちを生じて、樹脂のガラス繊維束に
対する被着が不均一となり、FRTPの品質にバラ
ツキを生じ易く、又ガラス繊維束が切断してしま
うことがある。特にこの傾向は集束剤として、ア
クリル樹脂、ウレタン樹脂、AS樹脂を含むもの
を使用した場合著しい。又ガラス繊維束を引出す
際、ガラス繊維束が完全に直線状とならず、撚
れ、弯曲等の歪が残存し、このため熱可塑性樹脂
の被着が不均一となり、FRTPの品質にバラツキ
を生ずる原因となる。このような歪は円筒状回巻
体からガラス繊維束を引出す際、回巻体の長手方
向に引出すと引出されたガラス繊維束に発生す
る、円筒状回巻体の周長当り1回の撚れによるも
のと考えられ、円筒状回巻体を円筒の軸を中心と
して回転自在に支持して引出しを行なうことによ
り、上述した引出しによつて生ずる撚れの発生を
防止することも試みられるが、残存歪を完全に除
去し、均質なFRTPを得ることは困難である。 While the glass fiber bundle is pulled out from the dried cylindrical roll and sent to the thermoplastic resin coating device, the glass fibers also become fluffy, resulting in uneven adhesion of the resin to the glass fiber bundle, which may affect the quality of the FRTP. It is easy to cause variations in the glass fiber bundles, and the glass fiber bundles may be broken. This tendency is particularly noticeable when a sizing agent containing acrylic resin, urethane resin, or AS resin is used. Furthermore, when pulling out the glass fiber bundle, the glass fiber bundle is not perfectly straight, and distortions such as twisting and curving remain, resulting in uneven adhesion of the thermoplastic resin and variations in the quality of the FRTP. It causes the occurrence of Such strain occurs when a glass fiber bundle is pulled out from a cylindrical wound body in the longitudinal direction of the cylindrical body. This is thought to be due to this, and attempts have been made to prevent the twisting caused by the above-mentioned drawing process by supporting the cylindrical wound body rotatably around the axis of the cylinder and performing the drawing process. , it is difficult to completely remove the residual strain and obtain a homogeneous FRTP.
更に又従来技術は次のような問題点を有する。 Furthermore, the prior art has the following problems.
ガラス繊維束の集束本数を増加し、ガラス繊維
束を太く(1000m当りの重量を大と)する程、生
産性が向上するが、繊維束を太くすると、繊維束
に被着した熱可塑性樹脂が繊維束の内部に滲透し
難くなり、この繊維束を使用して得られたFRTP
の品質にバラツキを生ずる。 As the number of bundled glass fiber bundles increases and the thickness of the glass fiber bundles increases (the weight per 1000m increases), productivity improves, but when the fiber bundles are made thicker, the thermoplastic resin attached to the fiber bundles FRTP obtained using this fiber bundle becomes difficult to seep into the inside of the fiber bundle.
This causes variations in quality.
このため集束剤を附与したガラス繊維を複数の
群に分割して集束して複数の細い繊維束となし、
この複数の繊維束を同時に巻取つて回巻体とする
ことも提案されているが、この方法によるときは
繊維束の長さを完全に同一とすることはできず、
ループが生じ、繊維束の回巻体からの引出しが円
滑に行なわれ難くなり、又繊維束を次の工程へ送
る際使用されるガイドに繊維束が引懸つて切断し
たり、毛羽立ちを生じたりし易い。 For this purpose, glass fibers to which a sizing agent has been added are divided into multiple groups and bundled into multiple thin fiber bundles.
It has also been proposed to simultaneously wind a plurality of fiber bundles into a rolled body, but when using this method, the lengths of the fiber bundles cannot be made completely the same,
Loops may occur, making it difficult to smoothly pull out the fiber bundle from the wound body, and may cause the fiber bundle to get caught on the guide used to send the fiber bundle to the next process, causing it to break or fuzz. Easy to do.
太い繊維束を引出し、ついで複数の繊維束に分
割することも試みられたが、分割の際毛羽立ちが
生じて良好な結果をうることができなかつた。 Attempts have also been made to draw out a thick fiber bundle and then divide it into a plurality of fiber bundles, but fluffing occurs during division and good results could not be obtained.
本発明は、ガラス繊維束を引出すときの毛羽立
ち、切断を生ずることなく、且つ生産性を阻害す
ることもなく熱可塑性樹脂が内部迄均一に滲透し
ており、均質なFRTPがえられるような熱可塑性
樹脂を被着したFRTP用成型材の製造方法を提供
することを目的としている。 The present invention uses heat to uniformly permeate the thermoplastic resin to the inside without causing fuzzing or cutting when pulling out the glass fiber bundle, and without impairing productivity, resulting in a homogeneous FRTP. The purpose of this invention is to provide a method for manufacturing a molded material for FRTP coated with a plastic resin.
上記目的を達成するこめに、本発明において
は、ブツシングから引出された多数のガラス繊維
に集束剤を附与集束してガラス繊維束とする工
程、ガラス繊維束を回転する軸に沿つて往復動す
る案内部材に係合せしめて上記軸に巻取つて円筒
状回巻体とする工程、上記回巻体の水分含有量が
0.5〜13wt%の状態において回巻体からガラス繊
維束を引出す工程、引出されたガラス繊維束を複
数の繊維束に分割する工程、分割されたガラス繊
維束を走行状態において乾燥し、ついで熱可塑性
樹脂を被着させる工程とにより成型材料を製造す
る。
In order to achieve the above object, the present invention includes a step of applying a sizing agent to a large number of glass fibers drawn from a bushing and converging them into a glass fiber bundle, and a step of reciprocating the glass fiber bundle along a rotating axis. The step of engaging the guide member and winding it around the shaft to form a cylindrical rolled body, the moisture content of the rolled body being
A process of drawing out a glass fiber bundle from a rolled body in a state of 0.5 to 13 wt%, a process of dividing the drawn glass fiber bundle into a plurality of fiber bundles, drying the divided glass fiber bundle in a traveling state, and then converting it into thermoplastic A molding material is manufactured by a step of applying resin.
又分割されたガラス繊維束の太さを乾燥状態に
おける1000m当りの重量が10〜500gr望ましくは
50〜300grたらしめる。 The thickness of the divided glass fiber bundles should preferably be 10 to 500g per 1000m in dry condition.
It should be 50-300gr.
次に本発明を更に具体的に説明する。 Next, the present invention will be explained in more detail.
ブツシングから引出した多数のガラス繊維に集
束剤を附与し、集束部材で集束する。 A sizing agent is applied to a large number of glass fibers pulled out from the bushing, and the fibers are bundled by a sizing member.
ガラス繊維としては直径3〜23μ、望ましくは
9〜16μのものが好適に使用できる。 Glass fibers having a diameter of 3 to 23 microns, preferably 9 to 16 microns can be suitably used.
ガラス繊維束を製造する際、或は回巻体からガ
ラス繊維束を引出して使用する際の毛羽立ち、糸
切れを防止して作業性を良好ならしめ、又ガラス
繊維と熱可塑性樹脂の馴染みを良好ならしめて
FRTPの強度を向上させる為、集束剤としてカツ
プリング剤、潤滑剤、被膜形成剤を含むものを使
用する。 Prevents fuzzing and thread breakage when manufacturing glass fiber bundles or when pulling out glass fiber bundles from rolled bodies to improve workability, and improves compatibility between glass fibers and thermoplastic resin. Get used to it
In order to improve the strength of FRTP, a sizing agent containing a coupling agent, lubricant, and film forming agent is used.
カツプリング剤としてはアミノシラン、エポキ
シシラン、ビニルシランのようなシランカツプリ
ング剤或はチタン系カツプリング剤、特にシラン
カツプリング剤が好適に用いられる。 As the coupling agent, silane coupling agents such as aminosilane, epoxysilane, and vinylsilane, or titanium-based coupling agents, particularly silane coupling agents, are preferably used.
潤滑剤としては、脂肪酸アミド、非イオン系界
面活性剤等が、又被膜形成剤としてはウレタン樹
脂、アクリル樹脂、AS樹脂を用いるのが好まし
い。 As the lubricant, it is preferable to use fatty acid amide, nonionic surfactant, etc., and as the film forming agent, it is preferable to use urethane resin, acrylic resin, or AS resin.
集束剤中のカツプリング剤、潤滑剤、被膜形成
剤の濃度は、夫々0.05〜0.8wt%、0.05〜5wt%、
0.5〜10wt%としガラス繊維に集束剤を固型分と
して0.01〜2wt%、望ましくは0.1〜0.8wt%附与
するのが適当である。集束剤を附与したガラス繊
維は、常法に従つて、集束してガラス繊維束とな
し、案内部材に導く。 The concentrations of the coupling agent, lubricant, and film forming agent in the sizing agent are 0.05 to 0.8 wt%, 0.05 to 5 wt%, respectively.
It is appropriate to add 0.01 to 2 wt%, preferably 0.1 to 0.8 wt% of the sizing agent to the glass fiber as a solid content. The glass fibers to which a sizing agent has been added are bundled into a glass fiber bundle according to a conventional method and guided to a guide member.
案内部材を回転する軸に沿つて往復動させ、ガ
ラス繊維束を円筒状に巻取つて回巻体とし、つい
でこの回巻体からガラス繊維束を引出して次の工
程に送る。 The guide member is reciprocated along the rotating shaft, the glass fiber bundle is wound into a cylindrical shape to form a roll, and the glass fiber bundle is then pulled out from the roll and sent to the next step.
回巻体が多量の水分を含んでいる場合、引出し
に先立ち予備乾燥して水分含有量を0.5〜13wt%、
望ましくは3〜8wt%とする。 If the rolled body contains a large amount of moisture, it should be pre-dried before being pulled out to reduce the moisture content to 0.5-13wt%.
The content is desirably 3 to 8 wt%.
この水分含有量があまり多いと、後述する乾燥
工程での乾燥が不充分となつてFRTPの品質不良
を生じ易く、又この水分があまり少ないと毛羽立
ち防止等の効果が不充分となり、又マイグレーシ
ヨンが大となり易い。 If this moisture content is too high, drying in the drying process described below will be insufficient, which tends to cause quality defects in FRTP.If this moisture content is too low, effects such as preventing fluffing will be insufficient, and migration tends to become large.
ついで、引出されたガラス繊維束を分割する。 Then, the drawn glass fiber bundle is divided.
分割の手段に特に限定はないがガラス繊維束の
先端を手で複数個に分割し、複数の溝を有する櫛
歯状の分割部材を使用し、分割されたガラス繊維
束を上記溝中を通して引張ることにより毛羽立ち
を生ずることなく、分割をスムースに行ない、長
さが等しく、ループのない繊維束群をうることが
できる。 There is no particular limitation on the means of division, but the tip of the glass fiber bundle is manually divided into a plurality of pieces, a comb-like dividing member having a plurality of grooves is used, and the divided glass fiber bundle is pulled through the grooves. As a result, the division can be performed smoothly without causing fuzz, and fiber bundles with equal length and no loops can be obtained.
なお、分割数は、分割された個々の繊維束の乾
燥状態における1000m当りの重量が10〜500gr、
望ましくは50〜300grとなるよう定めるのが適当
である。分割されたガラス繊維束を走行状態にお
いて乾燥することにより乾燥を均一に行ない、歪
等のないガラス繊維束をうることができる。 The number of divisions is based on the weight of each divided fiber bundle in the dry state of 10 to 500g per 1000m,
Desirably, it is appropriate to set the amount to 50 to 300 gr. By drying the divided glass fiber bundles while running, drying can be performed uniformly and glass fiber bundles free from distortion can be obtained.
乾燥は、100〜300℃望ましくは120〜200℃に保
たれたオーブン中を5〜200m/min望ましくは
10〜100m/min程度の速さで繊維束を走行せし
めつつ行なうのが好ましいが、高周波加熱等によ
つて乾燥することもできる。 Drying is preferably carried out in an oven maintained at 100-300°C, preferably 120-200°C, at 5-200 m/min.
It is preferable to dry the fiber bundle while running it at a speed of about 10 to 100 m/min, but it is also possible to dry by high frequency heating or the like.
ついで、ガラス繊維束に熱可塑性樹脂を被着さ
せる。 The glass fiber bundle is then coated with a thermoplastic resin.
被着の方法に特に限定はないが、熱可塑性樹脂
溶融物中をガラス繊維束を走行させて該溶融物を
繊維束表面に被着し、過剰の樹脂をスクイズする
ことによつて好適に被着を行なうことができる。
樹脂被着量は、樹脂の種類、上記方法で製造され
た本成型材料の用途に応じて定められるが、ガラ
ス繊維含有量が20〜80wt%望ましくは30〜60wt
%となるよう定めるのが適当である。 Although there is no particular limitation on the method of application, it is preferable to run the glass fiber bundle through a thermoplastic resin melt, apply the melt to the surface of the fiber bundle, and squeeze out excess resin. can be dressed.
The amount of resin deposited is determined depending on the type of resin and the use of the molding material produced by the above method, but the glass fiber content is preferably 20 to 80 wt%, preferably 30 to 60 wt.
It is appropriate to set it as %.
本発明の作用に就いて充分明らかでないが、お
よそ次のように考えられる。ブツシングから引出
された多数のガラス繊維に集束剤を附与して集束
し、ガラス繊維束とすると、該繊維束内のガラス
繊維同志は互いに平行に一体的に強く密着せしめ
られる。
Although the function of the present invention is not fully clear, it is thought to be approximately as follows. When a large number of glass fibers drawn from a bushing are added with a sizing agent and converged to form a glass fiber bundle, the glass fibers in the fiber bundle are tightly and tightly attached to each other in parallel to each other.
このガラス繊維束を回転する軸に沿つて往復動
する案内部材に係合せしめて上記軸に巻取つて円
筒状回巻体とすると、ガラス繊維同志が互いに密
着した状態で巻取られる。 When this glass fiber bundle is engaged with a guide member that reciprocates along a rotating shaft and wound around the shaft to form a cylindrical wound body, the glass fibers are wound in a state in which they are in close contact with each other.
この状態で回巻体を従来技術のように乾燥する
と、水分の蒸発に伴なつて集束剤が表面に移行す
るマイグレーシヨン現象が発生する。 If the wound body is dried in this state as in the prior art, a migration phenomenon occurs in which the sizing agent migrates to the surface as the moisture evaporates.
マイグレーシヨンにより、マクロ的には回巻体
の表面に近い部分程集束剤の含有量が多くなる。 Due to migration, from a macroscopic perspective, the content of the sizing agent increases in a portion closer to the surface of the wound body.
又、水分は毛細管現象等により移動するが、回
巻体中の繊維の分布は均一でないため、水分の移
動し易い通路と、水分の移動し難い部分が、回巻
体中に不規則に混在するため、この水分と共に移
動する集束の分布がミクロ的に不均一となる。 In addition, although moisture moves through capillary action, the distribution of fibers in the rolled body is not uniform, so passages where moisture can easily move and areas where moisture cannot move are mixed irregularly in the rolled body. Therefore, the distribution of the focus that moves with this moisture becomes microscopically non-uniform.
このような状態でガラス繊維束は弯曲した形状
で円筒状に回巻され、互いに密着した状態で乾燥
され、集束剤で互に固着する。 In this state, the glass fiber bundles are wound into a cylindrical shape in a curved shape, dried in close contact with each other, and fixed together with a sizing agent.
このため、回巻体から引出されたガラス繊維束
は長さ方向に沿つて集束剤の含有量にバラツキを
有し、又弯曲した形状のまま集束剤が乾燥固化し
ているため、撚れ、弯曲が残存し、又引出した際
し局部的に大きい応力を受け、又集束剤の多い部
分は剥れ難いため、部分的な繊維の切断が発生
し、又弯曲した部分がガイド等で擦られるため、
毛羽立ちを生ずるものと考えられる。 For this reason, the glass fiber bundle pulled out from the wound body has variations in the content of the sizing agent along the length direction, and the sizing agent is dried and solidified while remaining in a curved shape, resulting in twisting, The curve remains, and when it is pulled out, it receives a large stress locally, and the part with a lot of sizing agent is difficult to peel off, so the fibers are partially cut, and the curved part is rubbed by the guide, etc. For,
It is thought that it causes fluff.
これに対し、本発明の方法によるときは、ガラ
ス繊維束は水分の含有率が0.5〜13wt%の状態で
引出され、集束剤は乾燥固化していないので、引
出されたガラス繊維束は容易に変形して直線状と
なり、繊維の切断も生ずることなく、乾燥工程に
伴なう集束剤分布のバラツキも小さく、均一な繊
維束が得られるものと考えられる。 On the other hand, when using the method of the present invention, the glass fiber bundle is drawn out with a moisture content of 0.5 to 13 wt%, and the sizing agent is not dried and solidified, so the drawn glass fiber bundle is easily drawn out. It is considered that the fibers are deformed into a straight shape, the fibers are not cut, and the variation in the distribution of the sizing agent during the drying process is small, resulting in a uniform fiber bundle.
又ガラス繊維束の分割を、上述したような湿つ
た、集束剤が乾燥固化していない状態で行なうこ
とにより、分割に際しての毛羽立ちを防止し、生
産性を阻害することなく、長さが等しく、ループ
を有しない、細いガラス繊維束を製造することが
できる。 Furthermore, by splitting the glass fiber bundles in a wet state where the sizing agent has not dried and solidified as described above, fluffing during splitting can be prevented, and the lengths can be made equal without impeding productivity. It is possible to produce thin glass fiber bundles without loops.
ブツシングから引出した太さ13μのガラス繊維
にPPエマルジヨンを4wt%、潤滑剤を0.5wt%、
アミノシランを0.6wt%含む集束剤を固型分とし
て0.4wt%附与して3200本集束しガラス繊維束と
した。
Add 4wt% of PP emulsion and 0.5wt% of lubricant to the 13μ thick glass fiber pulled out from the bushing.
A sizing agent containing 0.6 wt% of aminosilane was added as a solid content of 0.4 wt%, and 3200 fibers were bundled to form a glass fiber bundle.
このガラス繊維束を内径16cm、外径26cm、高さ
26cmの円筒状に回巻し、水分の含有量8wt%の状
態で30m/minの速さで引出し、櫛歯状ガイドに
導き1000当りの重量100grのガラス繊維束22個に
分割した。ついで200℃に保たれたオーブン中を
通過させて乾燥し、PPをガラス繊維に対し
150wt%被着させ、1cmに切断し、成型材料とし
た。 This glass fiber bundle has an inner diameter of 16 cm, an outer diameter of 26 cm, and a height of
It was wound into a 26 cm cylinder, pulled out at a speed of 30 m/min with a water content of 8 wt%, guided through a comb-shaped guide, and divided into 22 glass fiber bundles each weighing 100 gr. Then, it is passed through an oven kept at 200℃ to dry it, and the PP is bonded to the glass fiber.
It was coated at 150wt% and cut into 1cm pieces to be used as a molding material.
成型材料製造中に毛羽立ち、糸切れを生ずるこ
とがなかつた。又この成型材料を使用しASTM.
D−256号の試験片を製造し、測定した衝撃強度
は50Kg−cm/cmであつた。 No fluffing or thread breakage occurred during the production of the molding material. Also, using this molding material, ASTM.
A test piece of No. D-256 was manufactured and the measured impact strength was 50 kg-cm/cm.
実施例と同一の回巻体を水分0.1wt%以下とな
る迄乾燥し、引出したガラス繊維束にそのまま樹
脂を附与し、実施例と同一の実験を行なつた。
The same experiment as in the example was carried out by drying the same rolled body as in the example until the water content was 0.1 wt% or less, applying resin to the drawn glass fiber bundle as it was.
毛羽立ちが屡々発生し、又得られた試験片の衝
撃強度は40Kg−cm/cmであつた。 Fuzzing frequently occurred, and the impact strength of the test piece obtained was 40 kg-cm/cm.
成型材料製造時の毛羽立ち、糸切れの発生がな
く、均質な成型材料が得られ、この成型材料を使
用し、高強度のFRTPが得られる。
A homogeneous molding material can be obtained without fluffing or thread breakage during the production of the molding material, and high-strength FRTP can be obtained using this molding material.
又生産性を阻害することなく長さが等しく、ル
ープのない細いガラス繊維束をうることができ
る。 Further, it is possible to obtain thin glass fiber bundles having equal lengths and no loops without hindering productivity.
Claims (1)
に集束剤を附与集束してガラス繊維束とする工
程、ガラス繊維束を回転する軸に沿つて往復動す
る案内部材に係合せしめて上記軸に巻取つて円筒
状回巻体とする工程、上記回巻体の水分含有量が
0.5〜13wt%の状態において回巻体からガラス繊
維束を引出す工程、引出されたガラス繊維束を複
数の繊維束に分割する工程、分割された繊維束を
走行状態において乾燥し、ついで熱可塑性樹脂被
着させる工程とを含む成型材料の製造方法。 2 分割されたガラス繊維束の乾燥状態における
重量は10〜500gr/1000mである請求項1記載の
成型材料の製造方法。[Scope of Claims] 1. A step of applying a sizing agent to a large number of glass fibers pulled out from a bushing and converging them into a glass fiber bundle, and engaging the glass fiber bundle with a guide member that reciprocates along a rotating axis. In the process of tightening and winding it around the shaft to form a cylindrical roll, the water content of the roll is
A process of drawing out a glass fiber bundle from a rolled body in a state of 0.5 to 13 wt%, a process of dividing the drawn glass fiber bundle into a plurality of fiber bundles, drying the divided fiber bundles in a running state, and then adding a thermoplastic resin A method for producing a molding material, including a step of adhering the molding material. 2. The method for producing a molding material according to claim 1, wherein the weight of the divided glass fiber bundle in a dry state is 10 to 500 gr/1000 m.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1281781A JPH03146442A (en) | 1989-10-31 | 1989-10-31 | Production of molding material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1281781A JPH03146442A (en) | 1989-10-31 | 1989-10-31 | Production of molding material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03146442A JPH03146442A (en) | 1991-06-21 |
| JPH0530783B2 true JPH0530783B2 (en) | 1993-05-10 |
Family
ID=17643887
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1281781A Granted JPH03146442A (en) | 1989-10-31 | 1989-10-31 | Production of molding material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03146442A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20060057319A1 (en) * | 2004-09-11 | 2006-03-16 | Gleich Klaus F | Methods and systems for making fiber reinforced products and resultant products |
-
1989
- 1989-10-31 JP JP1281781A patent/JPH03146442A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03146442A (en) | 1991-06-21 |
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