JPH0530782B2 - - Google Patents
Info
- Publication number
- JPH0530782B2 JPH0530782B2 JP1281780A JP28178089A JPH0530782B2 JP H0530782 B2 JPH0530782 B2 JP H0530782B2 JP 1281780 A JP1281780 A JP 1281780A JP 28178089 A JP28178089 A JP 28178089A JP H0530782 B2 JPH0530782 B2 JP H0530782B2
- Authority
- JP
- Japan
- Prior art keywords
- glass fiber
- fiber bundle
- molding material
- sizing agent
- fibers
- 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 - Fee Related
Links
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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)
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).
This invention relates to a method for producing a molding material useful for the production of.
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)が提案されてい
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). There is.
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。 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
維束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 fiber bundle also becomes fluffy, resulting in uneven adhesion of the resin to the glass fiber bundle, which leads to problems with FRTP. Quality tends to vary, and the glass fiber bundles may break. In particular, this tendency is seen as a sizing agent.
This is noticeable when using materials containing acrylic resin, urethane resin, or AS resin. Furthermore, when the glass fiber bundle is pulled out, the glass fiber bundle is not completely straight, and distortions due to twisting and curvature remain, resulting in uneven adhesion of the thermoplastic resin and variations in the quality of FRTP. Cause. When a glass fiber bundle is pulled out from a cylindrical wound body, such distortion occurs in the drawn glass fiber bundle when the glass fiber bundle is pulled out in the longitudinal direction of the wound body.
This is thought to be due to one twist per circumference of the cylindrical spiral body, and by supporting the cylindrical spiral body rotatably around the axis of the cylinder and pulling it out,
Attempts have been made to prevent the twisting caused by the above-mentioned drawing, but it is difficult to completely eliminate residual strain and obtain a homogeneous FRTP.
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、均質なFRTPが得ら
れるような、熱可塑性樹脂を被着したFRTP用成
型材の製造法を提供することを目的としている。 An object of the present invention is to provide a method for producing a molding material for FRTP coated with a thermoplastic resin, which allows a homogeneous FRTP to be obtained without fuzzing or cutting when pulling out a glass fiber bundle. .
上記目的を達成するために、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 pulled out 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 molding material is produced by the steps of drawing out the glass fiber bundle from the rolled body in a state of 0.5 to 13 wt%, drying the drawn out glass fiber bundle in a running state, and then coating it with a thermoplastic resin.
又ガラス繊維束として乾燥状態における1000m
当りの重量が300〜10000gr望ましくは500〜
5000grのものを使用する。 1000m in dry condition as glass fiber bundle
The weight per unit is 300~10000gr, preferably 500~
Use 5000gr.
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
面活性剤等が好適に使用できる。又被膜形成剤と
してウレタン樹脂、アクリル樹脂、AS樹脂を用
いた場合特に著しい効果をうることができる。 As the lubricant, fatty acid amides, nonionic surfactants, etc. can be suitably used. In addition, particularly remarkable effects can be obtained when urethane resin, acrylic resin, or AS resin is used as the film forming agent.
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%、0.05〜0.5wt%、
0.5〜10wt%とし、又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 0.5 wt%, respectively.
0.5 to 10 wt%, and 0.01 to 2 wt%, preferably 0.1 to 0.8 wt% of the sizing agent in the glass fiber as a solid content.
It is appropriate to grant it. 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。引出し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。 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. By drying the pulled out glass fiber bundle while it is running, it is possible to dry it uniformly and obtain a glass fiber bundle free from distortion.
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程度の速させ繊維束を走行せし
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 5-200m/min.
It is preferable to carry out the drying while running the spun fiber bundle 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のが、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, and the glass fiber content is preferably 20 to 80 wt%.
It is appropriate to set it at 60wt%.
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、集束剤で互いに固着する。 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 to each other 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、又引出しに際
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, Curves remain, and when the fibers are pulled out, they are subjected to large local stresses, and areas with a large amount of sizing agent are difficult to peel off, resulting in local fiber breakage, and curved areas are rubbed by guides, etc.
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.
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の速さで引出した。 This glass fiber bundle has an inner diameter of 16 cm, an outer diameter of 26 cm, and a height of
It was rolled into a 26 cm cylinder and pulled out at a speed of 30 m/min with a moisture content of 8 wt%.
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。 Then, it was dried by passing through an oven kept at 200°C, and 150wt% PP was applied to the glass fibers, and the fibers were 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45Kg−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 45 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.
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法。 2 ガラス繊維束の乾燥状態における重量は300
〜10000gr/1000mである請求項1記載の成型材
料の製造法。[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 method for producing a molding material, comprising the steps of drawing out a glass fiber bundle from a rolled body in a state of 0.5 to 13 wt%, drying the drawn glass fiber bundle in a running state, and then coating it with a thermoplastic resin. 2 The dry weight of the glass fiber bundle is 300
2. The method for producing a molding material according to claim 1, wherein the molding material has a particle size of 10000gr/1000m.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1281780A JPH03146441A (en) | 1989-10-31 | 1989-10-31 | Production of molding material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1281780A JPH03146441A (en) | 1989-10-31 | 1989-10-31 | Production of molding material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03146441A JPH03146441A (en) | 1991-06-21 |
| JPH0530782B2 true JPH0530782B2 (en) | 1993-05-10 |
Family
ID=17643874
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1281780A Granted JPH03146441A (en) | 1989-10-31 | 1989-10-31 | Production of molding material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03146441A (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 JP1281780A patent/JPH03146441A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03146441A (en) | 1991-06-21 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |