JPH0788841A - Resin composite material and preparation thereof - Google Patents
Resin composite material and preparation thereofInfo
- Publication number
- JPH0788841A JPH0788841A JP5241299A JP24129993A JPH0788841A JP H0788841 A JPH0788841 A JP H0788841A JP 5241299 A JP5241299 A JP 5241299A JP 24129993 A JP24129993 A JP 24129993A JP H0788841 A JPH0788841 A JP H0788841A
- Authority
- JP
- Japan
- Prior art keywords
- resin
- glass fibers
- composite material
- reinforced
- glass
- 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.)
- Pending
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- Reinforced Plastic Materials (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、ガラス繊維が熱可塑性
樹脂中に混入された樹脂複合材料及びこの製造方法に関
する。この樹脂複合材料を使用した樹脂成形品は、自動
車、建築土木等の分野において利用できる。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a resin composite material in which glass fibers are mixed in a thermoplastic resin and a method for producing the same. A resin molded product using this resin composite material can be used in fields such as automobiles and construction civil engineering.
【0002】[0002]
【背景技術及び発明が解決しようとする課題】熱可塑性
樹脂をマトリックス(基材)とする樹脂成形品は、非強
化型と強化型に大別される。非強化型樹脂成形品は、押
出機より溶融樹脂を金型内に押し出し、プレス成形して
得られるものである。これは、繊維等で強化できない
か、できても極めて短かい繊維を使用した場合に限られ
る。Background Art and Problems to be Solved by the Invention Resin molded articles having a thermoplastic resin as a matrix (base material) are roughly classified into a non-reinforced type and a reinforced type. The non-reinforced type resin molded product is obtained by extruding a molten resin into a mold by an extruder and press molding. This is limited to the case where a fiber or the like cannot be used for reinforcement or, if possible, an extremely short fiber is used.
【0003】一方、強化型樹脂成形品の場合は、ガラス
繊維等の長繊維が混入した樹脂よりなるウェブを加熱、
積層して製造したり、連続繊維をニードルパンチしたマ
ットに樹脂を加熱、含浸させて製造している。しかし、
これらの樹脂成形品の製造方法は、2,3工程を要する
ため、製造が煩雑になるという問題があった。また、得
られた樹脂成形品自体は、形状が複雑なものの場合、必
ずしも強度的に満足すべきものではなかった。即ち、成
形品末端部も含めて成形品全体としてガラス繊維による
補強が図られたものではなかった。On the other hand, in the case of a reinforced resin molded product, a web made of a resin mixed with long fibers such as glass fibers is heated,
It is manufactured by laminating or by matting needle-punched continuous fibers with a resin heated and impregnated. But,
The method for producing these resin molded products requires a few steps, and thus there is a problem that the production becomes complicated. Further, when the obtained resin molded product itself has a complicated shape, the strength was not necessarily satisfactory. That is, the entire molded product including the end of the molded product was not reinforced with glass fiber.
【0004】なお、ガラス繊維強化熱可塑性樹脂の製造
方法で、二軸スクリュー式押出機の押出方向に2個所の
供給口を設け、第1の供給口に熱可塑性樹脂、第2の供
給口にガラスロービングをそれぞれ供給するようにした
構成、又は3個所の供給口を設け、第1の供給口に熱可
塑性樹脂、第2の供給口にガラスロービング、第3の供
給口にガラスビーズをそれぞれ供給するようにした構成
も提案されている(特開昭58-56818号公報)が、前記問
題点の解決には到っていない。そこで、本発明は、樹脂
成形品とした場合に末端部も含めて全体として充分なガ
ラス繊維による補強効果が得られる樹脂複合材料及びこ
の樹脂複合材料の製造方法を提供することを目的とす
る。In the glass fiber reinforced thermoplastic resin manufacturing method, two supply ports are provided in the extrusion direction of the twin-screw extruder, and the first supply port is made of the thermoplastic resin and the second supply port is made of the thermoplastic resin. Glass roving is configured to be supplied respectively, or three supply ports are provided, a thermoplastic resin is supplied to the first supply port, glass roving is supplied to the second supply port, and glass beads are supplied to the third supply port. Although a structure configured to do so has been proposed (Japanese Patent Laid-Open No. 58-56818), the problem has not been solved yet. Therefore, an object of the present invention is to provide a resin composite material that can obtain a sufficient reinforcing effect by glass fibers as a whole including a terminal portion when a resin molded product is provided, and a method for producing the resin composite material.
【0005】[0005]
【課題を解決するための手段及び作用】本発明は、熱可
塑性樹脂中にガラス繊維が混入された樹脂複合材料であ
って、前記ガラス繊維は、前記熱可塑性樹脂中に繊維長
について2つの山形分布を有する含有割合で混在してい
ることを特徴とする。前記熱可塑性樹脂とは、ポリエチ
レン(PE)、ポリプロピレン(PP)、ナイロン(N
y)、ポリエステル、ポリカーボネート、ポリスチレン
等である。前記山形分布は、必ずしも正規分布のような
左右対象でなくてもよい。また、一方と他方の山形分布
の形状は、必ずしも同じでなくてもよい。即ち、比較的
短いガラス繊維と比較的長いガラス繊維の含有割合は、
異なっていてもよい。The present invention is a resin composite material in which glass fibers are mixed in a thermoplastic resin, wherein the glass fibers have two chevron shapes in the thermoplastic resin. It is characterized in that they are mixed in a content ratio having a distribution. The thermoplastic resin is polyethylene (PE), polypropylene (PP), nylon (N
y), polyester, polycarbonate, polystyrene and the like. The mountain-shaped distribution does not necessarily have to be symmetrical, such as a normal distribution. Further, the shapes of the mountain-shaped distributions on one side and the other side do not necessarily have to be the same. That is, the content ratio of relatively short glass fiber and relatively long glass fiber,
It may be different.
【0006】このような樹脂複合材料を使用して得られ
た樹脂成形品は、その中にガラス繊維が繊維長について
2つの山形分布を有する含有割合で混在しているため、
補強効果が高まる。即ち、形状の複雑な樹脂成形品であ
っても、比較的短いガラス繊維が末端部にまで行き届い
てこの末端部においてもガラス繊維による補強効果を発
揮し、その他の部分においては比較的長いガラス繊維が
強度(特に、衝撃強度)の発現に寄与する。これによ
り、成形品末端部に加えて成形品全体としての強度向上
が実現することになる。In the resin molded product obtained by using such a resin composite material, glass fibers are mixed therein in a content ratio having two chevron distributions with respect to the fiber length.
The reinforcing effect is enhanced. That is, even in the case of a resin molded product having a complicated shape, a relatively short glass fiber reaches the terminal part and the reinforcing effect by the glass fiber is exerted also at this terminal part, and in the other part, the relatively long glass fiber is used. Contributes to the development of strength (particularly impact strength). As a result, the strength of the molded product as a whole can be improved in addition to the end portion of the molded product.
【0007】一方の山形分布の平均繊維長としては5〜
40mmの範囲が適当であり、これより長いと成形品末端部
やリブ部分への樹脂の流動性が劣るようになる。また、
他方の山形分布の平均繊維長としては90〜110mm の範囲
が適当であり、これより長くても不都合は生じないが、
通常 150mmを超えることはない。樹脂複合材料(樹脂+
ガラス繊維)中のガラス繊維の含有量は、20〜60wt%が
適当である。20wt%未満の場合、ガラス繊維による補強
効果が得られなくなり、逆に60wt%を超えると樹脂とガ
ラス繊維との密着性(ぬれ性)及び賦形性が不良にな
る。On the other hand, the average fiber length of the mountain distribution is 5 to
A range of 40 mm is suitable, and if it is longer than this, the fluidity of the resin to the end parts and ribs of the molded product becomes poor. Also,
On the other hand, it is appropriate that the average fiber length of the chevron distribution is in the range of 90 to 110 mm, and longer lengths will not cause any inconvenience.
It usually does not exceed 150 mm. Resin composite material (resin +
The content of glass fiber in (glass fiber) is suitably 20 to 60 wt%. If it is less than 20 wt%, the reinforcing effect by the glass fiber cannot be obtained, and conversely, if it exceeds 60 wt%, the adhesion (wettability) between the resin and the glass fiber and the formability become poor.
【0008】本発明に係る樹脂複合材料を使用し、スタ
ンピング成形やプレス成形等により所望の樹脂成形品に
製造できる。また、この樹脂複合材料の製造工程と連続
させた押出し成形によって板材やパイプのような樹脂成
形品に製造できる。本発明に係る樹脂複合材料の製造方
法は、熱可塑性樹脂のホッパー及び樹脂押出方向に沿っ
てガラス繊維の2つのフィード部を備えた二軸混練押出
機を使用し、熱可塑性樹脂を前記ホッパーに投入すると
共に、前記各フィード部からガラス繊維を投入すること
を特徴とする。Using the resin composite material according to the present invention, a desired resin molded product can be manufactured by stamping molding, press molding or the like. Further, a resin molded product such as a plate or a pipe can be manufactured by extrusion molding which is continuous with the manufacturing process of the resin composite material. The method for producing a resin composite material according to the present invention uses a hopper of a thermoplastic resin and a twin-screw kneading extruder having two feed portions of glass fibers along the resin extrusion direction, and the thermoplastic resin is applied to the hopper. Along with the feeding, glass fibers are fed from each of the feed sections.
【0009】前記山形分布の形状(幅及び高さ)の制御
は、各フィード部へのガラス繊維の投入量及びその比率
を調整することにより可能である。投入するガラス繊維
の長さは、任意である。二軸混練押出機に熱可塑性樹脂
と共にガラス繊維を投入すると、スクリューによる混練
によってガラス繊維が切断されるため、元のガラス繊維
の長さは短くなる。同じ二軸混練押出機であれば、押出
機出口が遠い所から投入したガラス繊維ほど長い時間混
練されているため、ガラス繊維の長さは短くなる。The shape (width and height) of the chevron distribution can be controlled by adjusting the amount and ratio of the glass fibers fed into each feed section. The length of the glass fiber to be added is arbitrary. When the glass fiber is introduced into the twin-screw kneading extruder together with the thermoplastic resin, the glass fiber is cut by the kneading by the screw, so that the length of the original glass fiber is shortened. In the case of the same twin-screw kneading extruder, the length of glass fiber becomes shorter because the glass fiber charged from a position farther from the extruder outlet is kneaded for a longer time.
【0010】従って、二軸混練押出機にガラス繊維のフ
ィード部を樹脂押出方向に沿って、例えば出口から遠い
所(第1フィード部とする)と近い所(第2フィード部
とする)の2個所に設けた場合、第1フィード部から入
れたガラス繊維は、ガラス繊維の長さが短くなって開繊
度が良好となり、ガラス繊維とのぬれ性も良好になる。
一方、第2フィード部から入れたガラス繊維は、元のガ
ラス繊維の長さが比較的良く保たれ、しかもぬれ性も或
る程度良好である。Therefore, in the twin-screw kneading extruder, the glass fiber feed portion is arranged along the resin extruding direction, for example, at a location far from the outlet (first feed portion) and a location near the second feed portion (second feed portion). When it is provided at a portion, the glass fiber put in from the first feed portion has a shorter length of the glass fiber and has a good degree of opening, and also has a good wettability with the glass fiber.
On the other hand, the glass fiber put in from the second feed portion has a relatively long length of the original glass fiber and has a good wettability to some extent.
【0011】本製造方法において、ホッパーから投入さ
れた樹脂は、第1フィード部付近に到った時点において
完全に溶融している必要がある。樹脂が完全に溶融して
いない場合、ガラス繊維と樹脂との密着性が不良にな
る。また、固体状態のガラス繊維と樹脂が混合されるこ
とになるため、スクリューやシリンダーの摩耗が大きく
なる虞れがある。このような樹脂の溶融状態は、スクリ
ュー形状やバレル温度を変えることにより制御すること
ができる。In the present manufacturing method, the resin charged from the hopper needs to be completely melted when it reaches the vicinity of the first feed section. If the resin is not completely melted, the adhesion between the glass fiber and the resin will be poor. Further, since the glass fiber in the solid state and the resin are mixed, the abrasion of the screw or the cylinder may be increased. The molten state of such a resin can be controlled by changing the screw shape and barrel temperature.
【0012】また、第2フィード部直前においては、第
1フィード部から投入されたガラス繊維が開繊している
必要がある。開繊していないと、第2フィード部から投
入されたガラス繊維の開繊が妨げられたり、第2フィー
ド部から投入されたガラス繊維と樹脂との密着性(ぬれ
性)が不良となる。このようなガラス繊維の開繊状態
は、スクリュー形状や第1〜第2フィード部間の距離を
変えることにより制御することができる。ガラス繊維の
開繊度を大きくすることにより、ガラス繊維の流動性や
充填性が良くなり、細部の強度も向上する。加えて、ガ
ラス繊維の偏在がなくなり、均一に充填されるため、全
体としての強度も向上する。Immediately before the second feed section, the glass fibers introduced from the first feed section must be opened. If the fibers are not opened, the opening of the glass fibers fed from the second feed portion is hindered, or the adhesion (wettability) between the glass fibers fed from the second feed portion and the resin becomes poor. The opened state of such glass fibers can be controlled by changing the screw shape and the distance between the first and second feed portions. By increasing the degree of openness of the glass fiber, the flowability and filling property of the glass fiber are improved, and the strength of details is also improved. In addition, since the uneven distribution of glass fibers is eliminated and the glass fibers are uniformly filled, the strength as a whole is improved.
【0013】前記ぬれ性を良くすることにより、引張り
強度、曲げ強度等の物理的特性が向上する。第1及び第
2フィード部の各投入口からのガラス繊維の投入量は、
樹脂に対して重量で2/3以内とすることが適当であ
り、これを超えるとガラス繊維が互いに摩擦して繊維が
短くなり、本来の強度が発現しない場合がある。投入さ
れるガラス繊維は、通常、個々のガラス繊維が収束され
たもの(ロービング)となっているが、収束本数は 200
〜20000 程度、1本のガラス繊維の太さは9〜23μm 程
度である。なお、混練時の運転温度は、熱可塑性樹脂の
融点の+30〜80℃程度とする。By improving the wettability, physical properties such as tensile strength and bending strength are improved. The amount of glass fiber charged from each charging port of the first and second feed parts is
It is appropriate that the weight of the resin is within 2/3, and if it exceeds this, the glass fibers rub against each other to shorten the fibers, and the original strength may not be exhibited. The glass fibers to be put in are usually bundles of individual glass fibers (roving), but the number of bundles is 200
Approximately 20,000, the thickness of one glass fiber is approximately 9 to 23 μm. The operating temperature during kneading is about +30 to 80 ° C, which is the melting point of the thermoplastic resin.
【0014】[0014]
【実施例】本実施例で使用する二軸混練押出機は、混練
用の2本のスクリューと熱可塑性樹脂投入用のホッパー
を通常通り備え、加えてガラス繊維投入用のフィード部
を樹脂押出方向に沿って2つ備えたものである。具体的
寸法は、例えばシリンダーの内径が40mm、L/Dが28で
ある。一方のフィード部(第1フィード部とする)は、
ホッパーと押出機出口との略中間に設けられ、他方のフ
ィード部(第2フィード部とする)は、この第1フィー
ド部と押出機出口との略中間に設けられている。従っ
て、第1フィード部は、押出機出口から遠い位置に設け
られて出口までの距離が長くなっており、第2フィード
部は、押出機出口から近い位置に設けられて出口までの
距離が短くなっている。EXAMPLE The twin-screw kneading extruder used in this example is equipped with two screws for kneading and a hopper for charging a thermoplastic resin as usual, and in addition, a feed section for charging a glass fiber is provided in the resin extrusion direction. It is equipped with two along. Specific dimensions are, for example, a cylinder inner diameter of 40 mm and an L / D of 28. One of the feed parts (referred to as the first feed part) is
The feed section (second feed section) is provided substantially in the middle of the hopper and the extruder outlet, and is provided substantially in the middle of the first feed section and the extruder outlet. Therefore, the first feed portion is provided at a position far from the extruder outlet and the distance to the outlet is long, and the second feed portion is provided at a position close to the extruder outlet and the distance to the outlet is short. Has become.
【0015】実施例1 前記二軸混練押出機を使用し、次のように実施例に係る
樹脂複合材料であるGF強化PPを製造し、更にこのG
F強化PPより成るシート及びリブ付き成形品を製造し
た。先ず、熱可塑性樹脂としてホモグレードのポリプロ
ピレン(MI=20)を用意し、ガラス繊維としてガラス
繊維(GF)ロービング〔番手400(0.4g/m) 、単繊維 4
00本収束〕を用意した。押出機のシリンダー温度を 210
℃、スクリューの回転数を200rpmに保った状態で前記ホ
ッパーからポリプロピレンを押出機のシリンダー内に投
入すると共に、GFロービングを前記第1フィード部か
ら5本、また第2フィード部から5本シリンダー内に投
入して混練した。 Example 1 Using the above-mentioned twin-screw kneading extruder, GF reinforced PP, which is a resin composite material according to an example, was manufactured as follows, and further this G
Sheets and ribbed moldings made of F-reinforced PP were produced. First, prepare homo-grade polypropylene (MI = 20) as a thermoplastic resin, and use glass fiber (GF) roving as glass fiber [count 400 (0.4 g / m), single fiber 4
00 Convergence] was prepared. Adjust the extruder cylinder temperature to 210
℃, while maintaining the number of revolutions of the screw at 200 rpm, polypropylene was introduced from the hopper into the cylinder of the extruder, and 5 GF rovings were fed from the first feed section and 5 from the second feed section. And kneaded.
【0016】この混練の際、ホッパーから投入されたP
Pは、第1フィード部付近に到った時点において完全に
溶融していた。また、第2フィード部直前においては、
第1フィード部から投入されたGFが開繊していた。そ
して、このGF強化PPより次のようにしてシートを製
造した。即ち、ダイス(幅100mm 、厚さ3mm)から吐出
したGF強化PPを固化しないうちに切り取り、金型内
に投入してプレス圧10〜15トンで厚さ3 .8mmのGF強化
PPシートを成形した。引き続き、このPPシートの周
辺部をカットして幅210mm 、奥行き125mm 、厚さ3.8mm
の長方形のGF強化PPシートを得た。At the time of this kneading, P charged from the hopper
P was completely melted when it reached the vicinity of the first feed section. Also, immediately before the second feed section,
The GF introduced from the first feed section was opened. Then, a sheet was produced from this GF-reinforced PP as follows. That is, the GF-reinforced PP sheet discharged from the die (width 100 mm, thickness 3 mm) is cut out before it is solidified and put into a mold to form a GF-reinforced PP sheet with a thickness of 3.8 mm at a press pressure of 10 to 15 tons. did. Then, cut the periphery of this PP sheet to a width of 210 mm, a depth of 125 mm, and a thickness of 3.8 mm.
To obtain a rectangular GF-reinforced PP sheet.
【0017】このシート中のGFの含量は、38.9wt%で
あった。この「GF含量」の測定は、GF強化PPシー
トを灰化して測定したものである。このシート中、GF
は、繊維長について2つの山形の正規分布状態で混在し
ていた。一方の山形分布の繊維長の幅は、30〜40mm(平
均繊維長35mm)であり、この含有割合が50wt%、他方の
山形分布の繊維長の幅は、90〜100mm (平均繊維長95m
m)であり、この含有割合が50wt%であった。この「G
F繊維長」の測定は、製造したGF強化PPシートを灰
化し、その中心部付近のGF50本を分離し、直線定規で
長さを測定することにより行ったものである。この測定
の際、長さ2mm以下のGFは、その量が非常に少ないた
め無視した。The GF content in this sheet was 38.9 wt%. This "GF content" is measured by ashing a GF-reinforced PP sheet. GF in this sheet
Were mixed in two chevron-shaped normal distributions with respect to the fiber length. The width of the fiber length of one chevron distribution is 30-40 mm (average fiber length 35 mm), the content ratio is 50 wt%, the width of the fiber length of the other chevron distribution is 90-100 mm (average fiber length 95 m
m), and the content ratio was 50 wt%. This "G
The "F fiber length" is measured by ashing the produced GF-reinforced PP sheet, separating 50 GF fibers near the center thereof, and measuring the length with a straight line ruler. In this measurement, GF having a length of 2 mm or less was ignored because its amount was very small.
【0018】このGF強化PPシート中のGFとPPと
のぬれ性は良好であった。この「ぬれ性」は、GF強化
PPシートの表面を電子顕微鏡で観察して、GFとPP
との接合性を調べて評価したものである。そして、GF
とPPとの或る程度の接合性が認められる場合を「良
好」、GFとPPとが完全に分離している場合を「不
良」とした。このGF強化PPシートの外観は、良好で
あった。この「外観」は、表面を目視で観察して評価し
たものである。表面が平滑でGFが見えない場合を「良
好」、GFが凸部となって見える場合を「不良」とし
た。The wettability between GF and PP in this GF-reinforced PP sheet was good. This "wettability" is due to the fact that the surface of the GF-reinforced PP sheet is observed by an electron microscope and
It was evaluated by examining the bondability with. And GF
When a certain degree of conjugation between GF and PP was recognized, it was defined as “good”, and when GF and PP were completely separated, it was defined as “poor”. The GF-reinforced PP sheet had a good appearance. This "appearance" is evaluated by visually observing the surface. The case where the surface was smooth and GF was not visible was defined as “good”, and the case where GF was visible as a convex portion was defined as “poor”.
【0019】このGF強化PPシートの開繊状態は、良
好であった。この「開繊状態」の評価は、GF強化PP
シートの表面を電子顕微鏡で観察して評価したものであ
る。収束したGF単繊維が開繊し、ばらばらになってい
る状態を「良好」とした。次に、前記GF強化PPより
次のようにしてリブ付き成形品を製造した。即ち、前記
シートの場合と同様に、ダイスから吐出した樹脂複合材
料を金型内に投入してプレス圧10〜15トンで成形して図
1に示すような箱形成形品11を得た。この成形品11は、
長方形の底面部12の周縁に4つの側壁部13〜16が形成さ
れ、長い側壁部13,15 の略中央にそれぞれ第1のリブ17
及び第2のリブ18が形成されたものである。The opened state of this GF-reinforced PP sheet was good. This "opened state" is evaluated by GF-reinforced PP
The surface of the sheet was observed by an electron microscope and evaluated. The state in which the converged GF single fibers were opened and separated was defined as “good”. Next, a ribbed molded article was produced from the GF-reinforced PP as follows. That is, as in the case of the above-mentioned sheet, the resin composite material discharged from the die was put into a mold and molded at a press pressure of 10 to 15 tons to obtain a box-formed product 11 as shown in FIG. This molded product 11 is
Four side wall portions 13 to 16 are formed on the periphery of the rectangular bottom portion 12, and the first ribs 17 are respectively formed at the approximate centers of the long side wall portions 13 and 15.
And the second rib 18 is formed.
【0020】具体的寸法は、例えば、底面部12の一辺が
250mm、他辺が 150mm、側壁部13〜16の高さが65mm、第
1のリブ17の長さが50mm、高さが25mm、厚さが3mm、第
2のリブ18の長さが50mm、高さが5mm、厚さが3mmであ
る。この成形品11について、前記シートの場合と同様に
外観とリブ外観を評価したところ、良好であった。前記
第1のリブ17のGF充填率を測定したところ、80%以上
であり、評価は良好であった。この「GF充填率」と
は、第1のリブ17を切り取り、この試験片に対してソフ
トX線撮影を行い、影の部分として表れたGF充填部の
断面積の全断面積に対する割合を測定したものである。
そして、80%以上を「良好」、50%以下を「不良」とし
た。Specific dimensions are, for example, that one side of the bottom portion 12 is
250 mm, the other side is 150 mm, the height of the side walls 13 to 16 is 65 mm, the length of the first rib 17 is 50 mm, the height is 25 mm, the thickness is 3 mm, the length of the second rib 18 is 50 mm, The height is 5 mm and the thickness is 3 mm. The appearance and rib appearance of this molded product 11 were evaluated in the same manner as in the case of the above-mentioned sheet, and were good. When the GF filling rate of the first rib 17 was measured, it was 80% or more, and the evaluation was good. The "GF filling rate" is obtained by cutting the first rib 17 and performing soft X-ray photography on this test piece, and measuring the ratio of the cross-sectional area of the GF-filled portion shown as a shaded portion to the total cross-sectional area. It was done.
And 80% or more was made "good" and 50% or less was made "bad".
【0021】前記側壁部と前記底面部とのGF充填率
は、0.90以上であり、良好であった。この「GF充填
率」の測定も前記第1のリブ17のGF充填率測定と同様
に行い、0.90以上を「良好」、0.90未満を「不良」とし
た。そして、成形品11の底面部12から試験片を切り取
り、この試験片について各種物理的特性の測定を行った
ところ、引張り強度は1010kg/mm2 、曲げ強度は1840kg
/mm2 、曲げ弾性率は69100 、衝撃強度は60kg・cm/cm
2 であった。各物理的特性の測定は、引張り強度…ASTM
D638 、曲げ強度…ASTM D790 、曲げ弾性率…ASTM D79
0 、衝撃強度…ASTM D256 に基づいて行った。The GF filling rate of the side wall portion and the bottom surface portion was 0.90 or more, which was good. The "GF filling rate" was also measured in the same manner as the GF filling rate measurement of the first rib 17, and 0.90 or more was "good" and less than 0.90 was "bad". Then, a test piece was cut from the bottom surface portion 12 of the molded product 11, and various physical properties were measured on the test piece. Tensile strength was 1010 kg / mm 2 , bending strength was 1840 kg.
/ Mm 2 , flexural modulus of 69100, impact strength of 60 kg · cm / cm
Was 2 . Each physical property is measured by tensile strength ... ASTM
D638, flexural strength ... ASTM D790, flexural modulus ... ASTM D79
0, impact strength ... Performed based on ASTM D256.
【0022】次に、前記GF強化PPについて下記のよ
うにして賦形性を調べた。即ち、幅 290mm、奥行き 170
mm、厚さ65mmの金型を用い、上記長方形のGF強化PP
シートを3枚重ねて、加熱ブランク温度 230〜 250℃、
上部金型温度50〜60℃、下部金型温度30〜45℃、プレス
圧力140kg/cm2 、プレス加圧時間20秒の条件でスタンピ
ング成形して四角形の容器状成形品を作製した。この成
形試験の結果、5つのサンプル全部について完全に賦形
でき、評価は良好であった。なお、完全に賦形できた割
合が3/5以上を「良好」、2/5以下を「不良」と評
価した。Next, the shapeability of the GF-reinforced PP was examined as follows. That is, width 290 mm, depth 170
mm, 65 mm thick mold, using the rectangular GF reinforced PP
Stack 3 sheets, heating blank temperature 230-250 ℃,
The upper mold temperature was 50 to 60 ° C., the lower mold temperature was 30 to 45 ° C., the pressing pressure was 140 kg / cm 2 , and the pressing time was 20 seconds. As a result of this molding test, all five samples could be completely shaped, and the evaluation was good. It should be noted that a ratio of 3/5 or more that could be completely shaped was evaluated as “good” and a ratio of 2/5 or less as “poor”.
【0023】実施例2〜5 実施例1と同様にして各実施例に係るGF強化PPを製
造し、更にこのGF強化PPより成るシート及びリブ付
き成形品を製造した。但し、各実施例において、押出機
で混練する際、第1フィード部及び第2フィード部から
それぞれ投入するGFロービング本数を表1と2の「G
Fロービングの投入方法」の欄で示すように変えた。そ
して、各実施例に係る長方形のGF強化PPシートにつ
いて、実施例1と同様にして、GF含量、GF繊維長、
ぬれ性、外観及び開繊状態の測定及び評価を行った。 Examples 2 to 5 GF-reinforced PP according to each example was manufactured in the same manner as in Example 1, and a sheet and a ribbed molded product made of this GF-reinforced PP were manufactured. However, in each example, when kneading with an extruder, the number of GF rovings to be fed from the first feed section and the second feed section, respectively, was determined as “G” in Tables 1 and 2.
The method was changed as shown in the column of “F roving charging method”. Then, regarding the rectangular GF-reinforced PP sheet according to each example, in the same manner as in Example 1, the GF content, the GF fiber length,
The wettability, the appearance and the opened state were measured and evaluated.
【0024】これらの測定及び評価の結果を表1,2に
示す。表中、GFロービングの投入方法の欄で、F1は
第1フィード部、F2は第2フィード部を表す。次に、
GF強化PPから、実施例1と同様に各実施例に係るリ
ブ付き成形品11を製造した。そして、このリブ付き成形
品11について、実施例1と同様にして、外観、リブ外
観、リブGF充填率、側壁部と底面部のGF充填率及び
各種物理的特性の測定及び評価を行った。次に、各実施
例に係るGF強化PPの賦形性についても実施例1と同
様に調べた。The results of these measurements and evaluations are shown in Tables 1 and 2. In the column of GF roving charging method in the table, F1 represents the first feed section and F2 represents the second feed section. next,
A ribbed molded product 11 according to each example was manufactured in the same manner as in Example 1 from GF-reinforced PP. Then, this ribbed molded product 11 was measured and evaluated in the same manner as in Example 1 for the appearance, rib appearance, rib GF filling rate, GF filling rate of the side wall portion and the bottom surface portion, and various physical characteristics. Next, the shapeability of the GF-reinforced PP according to each example was also examined in the same manner as in Example 1.
【0025】比較例1〜5 実施例1と同様にして各比較例に係るGF強化PPを製
造し、更にこのGF強化PPより成るシート及びリブ付
き成形品を製造した。但し、各実施例において、押出機
で混練する際、第1フィード部及び/又は第2フィード
部から投入するGFロービング本数を表3と4の「GF
ロービングの投入方法」の欄で示すように変えた。そし
て、各比較例に係る長方形のGF強化PPシートについ
て、実施例1と同様にして、GF含量、GF繊維長、ぬ
れ性、外観及び開繊状態の測定及び評価を行った。 Comparative Examples 1 to 5 GF-reinforced PP according to each comparative example was manufactured in the same manner as in Example 1, and a sheet and a ribbed molded product made of this GF-reinforced PP were manufactured. However, in each example, when kneading with an extruder, the number of GF rovings fed from the first feed section and / or the second feed section was set to "GF" in Tables 3 and 4.
The method was changed as shown in the column of "Roving input method". Then, with respect to the rectangular GF-reinforced PP sheet according to each comparative example, the GF content, the GF fiber length, the wettability, the appearance and the opened state were measured and evaluated in the same manner as in Example 1.
【0026】これらの測定及び評価の結果を表3,4に
示す。次に、GF強化PPから、実施例1と同様に各比
較例に係るリブ付き成形品を製造した。そして、このリ
ブ付き成形品について、実施例1と同様にして、外観、
リブ外観、リブGF充填率、側壁部と底面部のGF充填
率及び各種物理的特性の測定及び評価を行った。次に、
各比較例に係るGF強化PPの賦形性についても実施例
1と同様に調べた。The results of these measurements and evaluations are shown in Tables 3 and 4. Next, a ribbed molded product according to each comparative example was manufactured from GF-reinforced PP in the same manner as in Example 1. Then, with respect to this ribbed molded article, in the same manner as in Example 1, the appearance,
The rib appearance, the rib GF filling rate, the GF filling rate of the side wall portion and the bottom surface portion, and various physical properties were measured and evaluated. next,
The shapeability of the GF-reinforced PP according to each comparative example was also examined in the same manner as in Example 1.
【0027】[0027]
【表1】 [Table 1]
【0028】[0028]
【表2】 [Table 2]
【0029】[0029]
【表3】 [Table 3]
【0030】[0030]
【表4】 [Table 4]
【0031】表1,2より、実施例1〜5に係るGF強
化PPシートによれば、GFが繊維長について2つの山
形分布を有する含有割合で混在し、一方の山形分布の平
均繊維長が5〜40mm、他方の山形分布の平均繊維長が90
〜110mm の範囲にあり、かつガラス繊維の含有量が20〜
60wt%の範囲内にあるため、ぬれ性、外観及び開繊状態
に関して良好であることがわかる。従って、ぬれ性と開
繊状態が良好であることにより、GFによる補強効果を
充分に発揮させることができる。From Tables 1 and 2, according to the GF-reinforced PP sheets according to Examples 1 to 5, GF was mixed in a content ratio having two chevron distributions with respect to the fiber length, and one of the chevron distributions had an average fiber length. 5-40 mm, mean fiber length of the other chevron distribution is 90
~ 110 mm and glass fiber content of 20 ~
Since it is in the range of 60 wt%, it is understood that the wettability, the appearance and the opened state are good. Therefore, since the wettability and the spread state are good, the reinforcing effect of GF can be sufficiently exerted.
【0032】また、各実施例に係るリブ付き成形品11に
よれば、外観、リブ外観、リブGF充填率、側壁部と底
面部のGF充填率及び各種物理的特性に関しても良好で
あることがわかる。従って、短い繊維長のGFが、成形
品11のリブ17,18 にも充分行き渡っているため、これら
のリブ17,18 においても、また成形品11全体としてもG
Fによる充分な補強効果が得られる。更に、各実施例に
係るGF強化PPは、賦形性についても良好であること
がわかる。従って、GFの含有割合を本発明に係る2山
分布としたことによる成形上の問題点は何等生じない。Further, according to the ribbed molded product 11 according to each example, the appearance, the rib appearance, the rib GF filling rate, the GF filling rate of the side wall portion and the bottom surface portion, and various physical characteristics are good. Recognize. Therefore, since the GF having a short fiber length is sufficiently distributed to the ribs 17 and 18 of the molded product 11, the ribs 17 and 18 and the molded product 11 as a whole are G
A sufficient reinforcing effect by F can be obtained. Furthermore, it can be seen that the GF-reinforced PP according to each example also has good shapeability. Therefore, there is no problem in molding due to the two peak distribution of the present invention.
【0033】一方、比較例1,2,4に係るGF強化P
Pシートによれば、GFが繊維長について、2つの山形
分布ではなく、1つの山形分布で混在しているため、ぬ
れ性、外観及び開繊状態に関して表3,4に示す通り不
良となる場合がある。また、比較例1,2,4に係るリ
ブ付き成形品によれば、外観、リブ外観、リブGF充填
率、側壁部と底面部のGF充填率及び各種物理的特性に
関しても表3,4に示す通り不良となる場合がある。従
って、比較例1,4に係るリブ付き成形品のように、リ
ブGF充填率が不良の場合、成形品のリブにGFが充分
に行き渡っていないため、このリブにおいて充分な補強
効果が得られない虞れがある。On the other hand, the GF-reinforced P according to Comparative Examples 1, 2, and 4
According to the P sheet, since GF is mixed in the fiber length not in two chevron distributions but in one chevron distribution, the wettability, the appearance, and the opened state are poor as shown in Tables 3 and 4. There is. Further, according to the ribbed molded products of Comparative Examples 1, 2, and 4, the appearance, the rib appearance, the rib GF filling rate, the GF filling rate of the side wall portion and the bottom surface portion, and various physical characteristics are also shown in Tables 3 and 4. It may be defective as shown. Therefore, when the rib GF filling rate is poor as in the ribbed molded products according to Comparative Examples 1 and 4, the ribs of the molded product are not sufficiently filled with GF, and a sufficient reinforcing effect can be obtained with this rib. There is a fear that it will not.
【0034】なお、賦形性については、比較例1,2,
4に係るGF強化PPはいずれも良好であった。比較例
3に係るGF強化PPシートによれば、GFが繊維長に
ついて2つの山形分布を有する含有割合で混在している
が、他方の山形分布の平均繊維長が70mmと短いうえ、G
Fの含有量が60wt%を超えているため、ぬれ性、外観及
び開繊状態に関して不良であった。また、比較例3の場
合、リブ付き成形品を作製しようとしたが、GFの含有
量が多すぎて流動性が不良となり、成形できなかった。Regarding the shapeability, Comparative Examples 1, 2,
All of the GF-reinforced PPs of No. 4 were good. According to the GF-reinforced PP sheet according to Comparative Example 3, GF is mixed at a content ratio having two chevron distributions with respect to the fiber length, but the other chevron distribution has a short average fiber length of 70 mm and G
Since the content of F exceeds 60 wt%, the wettability, the appearance and the opened state were poor. Further, in the case of Comparative Example 3, an attempt was made to produce a ribbed molded product, but the content of GF was too large and the flowability was poor, and molding was not possible.
【0035】更に、比較例3に係るGF強化PPは、賦
形性についても不良であった。比較例5に係るGF強化
PPシートによれば、GFが繊維長について2つの山形
分布を有する含有割合で混在しているが、他方の山形分
布の平均繊維長が50mmと短いため、ぬれ性、外観及び開
繊状態に関して不良であった。また、比較例5に係るリ
ブ付き成形品によれば、外観、リブ外観、リブGF充填
率及び側壁部と底面部のGF充填率に関しても不良であ
った。更に、比較例5に係るGF強化PPは、賦形性に
ついても不良であった。Further, the GF-reinforced PP according to Comparative Example 3 was also poor in shapeability. According to the GF-reinforced PP sheet according to Comparative Example 5, GF is mixed in a content ratio having two chevron distributions with respect to the fiber length, but since the mean fiber length of the other chevron distribution is as short as 50 mm, the wettability, The appearance and the opened state were poor. In addition, according to the ribbed molded product of Comparative Example 5, the appearance, the rib appearance, the rib GF filling rate, and the GF filling rate of the side wall portion and the bottom portion were also poor. Furthermore, the GF-reinforced PP according to Comparative Example 5 was also poor in shapeability.
【0036】[0036]
【発明の効果】本発明に係る樹脂複合材料及びこの樹脂
複合材料の製造方法によれば、樹脂成形品とした場合に
末端部も含めて全体として充分なガラス繊維による補強
効果が得られる。EFFECTS OF THE INVENTION According to the resin composite material and the method for producing the resin composite material according to the present invention, when a resin molded product is obtained, a sufficient reinforcing effect by the glass fiber including the end portion can be obtained as a whole.
【図1】本発明の実施例に係るF強化PPより成るリブ
付き成形品の斜視図である。FIG. 1 is a perspective view of a ribbed molded product made of F-reinforced PP according to an embodiment of the present invention.
11 箱形成形品 17 第1のリブ 18 第2のリブ 11 Box-formed product 17 First rib 18 Second rib
───────────────────────────────────────────────────── フロントページの続き (72)発明者 和田 成俊 三重県四日市市千歳町2番地 出光エヌエ スジー株式会社内 (72)発明者 須藤 健司 三重県四日市市千歳町2番地 出光エヌエ スジー株式会社内 (72)発明者 野村 学 千葉県市原市姉崎海岸1番地1 出光石油 化学株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Narutoshi Wada 2 Chitose-cho, Yokkaichi-shi, Mie Idemitsu NSG Co., Ltd. (72) Kenji Sudo 2 Chitose-cho, Yokkaichi-shi, Mie Idemitsu NGS Co., Ltd. ( 72) Inventor Manabu Nomura 1 Inezaki Kaigan Co., Ltd. 1 Anezaki Kaigan, Ichihara City, Chiba Prefecture
Claims (3)
た樹脂複合材料であって、前記ガラス繊維は、前記熱可
塑性樹脂中に繊維長について2つの山形分布を有する含
有割合で混在していることを特徴とする樹脂複合材料。1. A resin composite material in which glass fibers are mixed in a thermoplastic resin, wherein the glass fibers are mixed in the thermoplastic resin in a content ratio having two chevron distribution with respect to the fiber length. A resin composite material characterized by the above.
繊維長が5〜40mm、他方の山形分布の平均繊維長が90〜
110mm の範囲にあり、かつ前記ガラス繊維の含有量が20
〜60wt%であることを特徴とする請求項1記載の樹脂複
合材料。2. An average fiber length of one chevron distribution of the glass fibers is 5 to 40 mm, and an average fiber length of the other chevron distribution is 90 to
It is in the range of 110 mm and the glass fiber content is 20
The resin composite material according to claim 1, wherein the content is -60 wt%.
向に沿ってガラス繊維の2つのフィード部を備えた二軸
混練押出機を使用し、 熱可塑性樹脂を前記ホッパーに投入すると共に、前記各
フィード部からガラス繊維を投入することを特徴とする
請求項1又は2記載の樹脂複合材料の製造方法。3. A twin-screw kneading extruder equipped with a thermoplastic resin hopper and two glass fiber feed portions along the resin extrusion direction is used, and the thermoplastic resin is introduced into the hopper and each of the feeds is fed. The method for producing a resin composite material according to claim 1 or 2, wherein glass fibers are charged from a portion.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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JP5241299A JPH0788841A (en) | 1993-09-28 | 1993-09-28 | Resin composite material and preparation thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5241299A JPH0788841A (en) | 1993-09-28 | 1993-09-28 | Resin composite material and preparation thereof |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0788841A true JPH0788841A (en) | 1995-04-04 |
Family
ID=17072219
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Application Number | Title | Priority Date | Filing Date |
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JP5241299A Pending JPH0788841A (en) | 1993-09-28 | 1993-09-28 | Resin composite material and preparation thereof |
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Country | Link |
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JP (1) | JPH0788841A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2015140353A (en) * | 2014-01-27 | 2015-08-03 | 東レ株式会社 | Fiber-reinforced thermoplastic resin composition, method for producing the same, and method for producing fiber-reinforced thermoplastic resin molding |
-
1993
- 1993-09-28 JP JP5241299A patent/JPH0788841A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2015140353A (en) * | 2014-01-27 | 2015-08-03 | 東レ株式会社 | Fiber-reinforced thermoplastic resin composition, method for producing the same, and method for producing fiber-reinforced thermoplastic resin molding |
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