JPH03261519A - Manufacture of fiber reinforced thermoplastic resin molded product - Google Patents
Manufacture of fiber reinforced thermoplastic resin molded productInfo
- Publication number
- JPH03261519A JPH03261519A JP2059428A JP5942890A JPH03261519A JP H03261519 A JPH03261519 A JP H03261519A JP 2059428 A JP2059428 A JP 2059428A JP 5942890 A JP5942890 A JP 5942890A JP H03261519 A JPH03261519 A JP H03261519A
- Authority
- JP
- Japan
- Prior art keywords
- thermoplastic resin
- fiber
- sheet
- mold
- resin
- 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
Links
Landscapes
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
- Moulding By Coating Moulds (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〈産業上の利用分野〉
本発明は自動車外板パネル、内装パネル等の自動車部品
、土木建築用資材等の工業材料に供する繊維強化熱可塑
性樹脂成形品の製造方法に関する。[Detailed Description of the Invention] <Industrial Application Field> The present invention relates to a method for manufacturing fiber-reinforced thermoplastic resin molded products for use in automobile parts such as automobile exterior panels and interior panels, and industrial materials such as civil engineering and construction materials. .
詳しくは繊維配向等による変形が少なく、外観光沢、寸
法安定性及び機械的物性の優れた繊維強化熱可塑性樹脂
成形品の製造方法に関する。More specifically, the present invention relates to a method for producing fiber-reinforced thermoplastic resin molded articles that are less deformed due to fiber orientation and have excellent appearance gloss, dimensional stability, and mechanical properties.
〈従来の技術〉
従来、繊維強化熱可塑性樹脂成形品を得るのにいくつか
の方法が知られている0代表的な方法は、短繊維強化ペ
レットを用いて射出成形等の一般的成形法で繊維強化成
形品を製造する方法である。<Prior art> Several methods have been known to obtain fiber-reinforced thermoplastic resin molded products. The most representative method is to use short fiber-reinforced pellets to obtain a molded product using a general molding method such as injection molding. This is a method for manufacturing fiber-reinforced molded products.
またペレット製造時のベレット切断長さとほぼ同じ長さ
の中繊維長の繊維で強化された熱可塑性樹脂ペレットを
用い、射出成形等で繊維強化成形品を製造する方法もあ
る。一方、近年、繊維強化熱可塑性樹脂シートを再加熱
し、ブレス成形により製品を得る、いわゆるスタンパプ
ル・シートの技術が注目されている。スタンパプル・シ
ートの技術は強化に用いられる繊維により、2つに大別
される。1つは、数sat〜100鴫長さの単繊維と熱
可塑性樹脂粉末を湿式、又は乾式で混合し、加熱、ロー
ルプレスを経てスタンパプル・シートを製造し、このシ
ートを予備加熱後、プレスして繊維強化成形品を得る方
法である。(例えば特開昭57−28135号公報)、
もう一方のスタンパプル・シート技術は、長繊維強化ス
タンパプル・シートである。この方法では、編んだ長繊
維マットに溶融した熱可塑性樹脂を押出ラミネーシヲン
し、ロールプレスを経てスタンパブルシートを製造、こ
のシートを予備加熱し、プレス成形で繊維強化成形品を
製造する。There is also a method of producing a fiber-reinforced molded product by injection molding or the like using thermoplastic resin pellets reinforced with medium fiber length fibers that are approximately the same length as the pellet cutting length during pellet production. On the other hand, in recent years, a so-called stamped sheet technology has been attracting attention, in which a fiber-reinforced thermoplastic resin sheet is reheated and a product is obtained by press molding. Stamped sheet technology can be broadly divided into two types depending on the fibers used for reinforcement. One is to mix single fibers of several sat to 100 lengths with thermoplastic resin powder in a wet or dry process, heat and roll press to produce a stamped sample sheet, and then preheat this sheet and press it. This is a method to obtain fiber-reinforced molded products. (For example, Japanese Patent Application Laid-open No. 57-28135),
Another stamped sample sheet technology is long fiber reinforced stamped sample sheets. In this method, a woven long fiber mat is extrusion laminated with a molten thermoplastic resin, a stampable sheet is produced through roll pressing, this sheet is preheated, and a fiber-reinforced molded product is produced by press molding.
〈発明が解決しようとする課題〉
従来の技術はそれぞれ固有の技術、経済性の問題点を有
している。繊維強化成形品の製造法として最も一般的に
普及している短繊維強化ペレット法は、成形性、デザイ
ン対応性、コスト等は他の技術に比較し優位であるが繊
維強化の最大の目的である機械的強度の向上、特に耐衝
撃強度の点で効果が低いという欠点を有している。この
理由は、繊維と樹脂の混合、分散過程、すなわち造粒時
、及び成形時の2回の可塑化、混練工程で繊維は著しく
切断されるためである。さらに成形過程で、繊維は溶融
樹脂とともに金型内を流動するために、成形品中に繊維
配向が残り成形品が大きく変形する欠点も有している。<Problem to be solved by the invention> Each of the conventional techniques has its own technical and economic problems. The short fiber-reinforced pellet method, which is the most popular method for manufacturing fiber-reinforced molded products, has advantages over other technologies in terms of moldability, design compatibility, cost, etc. It has the disadvantage that it is less effective in improving certain mechanical strengths, especially impact strength. The reason for this is that the fibers are significantly cut during the mixing and dispersion process of the fibers and resin, that is, during the plasticization and kneading process twice, once during granulation and during molding. Furthermore, since the fibers flow in the mold together with the molten resin during the molding process, fiber orientation remains in the molded product, resulting in large deformation of the molded product.
又、繊維、特に無m繊維の場合、造粒、成形等で使用さ
れる押出機、射出成形機のスクリュー、シリンダ一部を
著しく摩耗させることもコストの点から大きな問題とな
る。In addition, in the case of fibers, especially non-molecular fibers, it is a big problem from the point of view of cost that parts of the screws and cylinders of extruders and injection molding machines used in granulation, molding, etc. are significantly worn out.
方、中繊維長の強化ペレットの製造工程は特殊な押出機
ヘッドを必要とし、又生産性も単繊維強化ペレットに会
較し低下するため、コストの高い製品となる。さらに成
形品中の繊維配向による変形、スクリュー、シリンダー
等の摩耗は単繊維ペレ。On the other hand, the manufacturing process of reinforced pellets with medium fiber length requires a special extruder head, and the productivity is lower than that of single fiber reinforced pellets, resulting in a high-cost product. Furthermore, deformation due to fiber orientation in the molded product and wear of screws, cylinders, etc. are caused by single fiber pellets.
トの場合と同様である。This is the same as in the case of
中及び長繊維長の繊維強化スタンパブルシートでは、成
形品中に残留する繊維が、原料として用いられた繊維の
長さをそのまま保つためきわめて高い機械的強度が得ら
れる。しかしながら中繊維長の単繊維強化スタンパブル
シートの技術においては、熱可塑性樹脂原料は粉末でな
ければならず、製品は粉砕コストのため割高となる。さ
らに抄紙機、ロール・プレス、予熱機など高価で特殊な
設備を要する。成形品内の繊維配向は、成形時に溶融樹
脂と共に一部の繊維が流れるため、繊維強化ペレットの
場合より少ないが、発生し、成形品を変形させることが
ある。Fiber-reinforced stampable sheets with medium and long fiber lengths have extremely high mechanical strength because the fibers remaining in the molded product maintain the same length of fibers used as raw materials. However, in the technology of single fiber reinforced stampable sheets with medium fiber length, the thermoplastic resin raw material must be powder, and the product is expensive due to the grinding cost. Furthermore, it requires expensive and special equipment such as a paper machine, roll press, and preheating machine. Fiber orientation within the molded product may occur and deform the molded product, although this is less than in the case of fiber-reinforced pellets, since some fibers flow together with the molten resin during molding.
長繊維スタンパブルシートの場合、成形時に溶融した樹
脂のみ流動し、繊維が流れないために成形品外周部が樹
脂のみの部分が発生し、強度的に安定しない。又、収束
した繊維を用いるため表面外観の粗いものしか得られな
い、さらに中繊維長のスタンパブルシートと同様に繊維
織機、押出機、ロール・プレス、予熱機などの高価で特
殊な設備を要する。In the case of a long-fiber stampable sheet, only the molten resin flows during molding, and the fibers do not flow, so that the outer periphery of the molded product is made up of only resin, making it unstable in terms of strength. In addition, since converged fibers are used, only a rough surface appearance can be obtained, and like stampable sheets with medium fiber length, expensive and special equipment such as a fiber loom, extruder, roll press, and preheating machine are required. .
以上述べた他に、繊維強化熱可塑性樹脂成形品の表面外
観、光沢は、非強化成形品に比較し、表面に繊維が部分
的に露出するため著しく劣る。又熱可塑性樹脂は、線膨
張係数が大きく、金属と接合した場合、気温差で寸法が
変わる問題がある。In addition to the above, the surface appearance and gloss of fiber-reinforced thermoplastic resin molded products are significantly inferior to those of non-reinforced molded products because fibers are partially exposed on the surface. Furthermore, thermoplastic resins have a large coefficient of linear expansion, and when bonded to metal, there is a problem that the dimensions change due to temperature differences.
く課題を解決するための手段〉
このように、従来の技術はm械的物性、変形、外観、コ
ストなどにそれぞれ問題点を有し、工業的技術としては
十分なものとは言えない0本願発明者らはこれらの問題
点を克服する技術を開発すべく鋭意研究を進めてきたが
、ついに以下に述べる工業的に優れた、かつ低コストの
、表面外観が優れた繊維強化熱可塑性樹脂成形品の新し
い製造方法を開発するに至った。As described above, the conventional techniques have problems in mechanical properties, deformation, appearance, cost, etc., and cannot be said to be sufficient as industrial techniques. The inventors have been conducting intensive research to develop a technology to overcome these problems, and have finally developed the following industrially superior, low-cost, fiber-reinforced thermoplastic resin molding with an excellent surface appearance. This led to the development of a new manufacturing method for the product.
すなわち本発明は、(i)溶融した熱可塑性樹脂(A)
を複数の多孔性繊維質シートの層間に供給し、樹脂供給
圧力及び/又はプレス圧力により多孔性繊維質シートの
空隙を通し該熱可塑性樹脂(A)を浸透させて、多孔性
繊維質シートの最外層面に位置した、熱可塑性樹脂(A
)と接着性を有する熱可塑性樹脂CB)よりなるシート
又はフィルムと接着させることを特徴とする繊維強化熱
可塑性樹脂成形品の製造方法、(11)未閉鎖の金型内
に溶融した熱可塑性樹脂(A)を供給し、多孔性繊維質
シート及び熱可塑性樹脂(A)と接着性を有する熱可塑
性樹脂CB)よりなるシート又はフィルムを重ねて、多
孔性繊維質シートが溶融した熱可塑性樹脂(A)に面す
る向きに載置し、金型を閉し多孔性繊維質シ→トの空隙
を通し溶融した熱可塑性樹脂(A)を浸透させ、熱可塑
性樹脂(B)よりなるシート又はフィルムと接着させる
ことを特徴とする繊維強化熱可塑性樹脂成形品の製造方
法、並びに(ii)未閉鎖の金型内に、熱可塑性樹脂(
A)と接着性を有する熱可塑性樹脂(8)よりなるフィ
ルム又はシートを載置し、次いで熱可塑性樹脂(A)を
マトリックス材料とする溶融した繊維強化熱可塑性樹脂
を金型内に供給しながら又は供給した後、金型を閉し加
圧冷却して成形することを特徴とする繊維強化熱可塑性
樹脂成形品の製造方法である。That is, the present invention provides (i) a molten thermoplastic resin (A)
is supplied between the layers of a plurality of porous fibrous sheets, and the thermoplastic resin (A) is infiltrated through the voids of the porous fibrous sheets by resin supply pressure and/or press pressure to form the porous fibrous sheets. The thermoplastic resin (A
) and a sheet or film made of a thermoplastic resin CB) having adhesive properties. (A) is supplied, and a sheet or film made of a porous fibrous sheet and a thermoplastic resin (CB) having adhesive properties with the thermoplastic resin (A) is stacked on top of the thermoplastic resin (CB) in which the porous fibrous sheet is melted. The sheet or film made of the thermoplastic resin (B) is prepared by placing the sheet facing A), closing the mold, and allowing the molten thermoplastic resin (A) to penetrate through the voids in the porous fibrous sheet. A method for manufacturing a fiber-reinforced thermoplastic resin molded article, characterized in that (ii) a thermoplastic resin (
A film or sheet made of a thermoplastic resin (8) having adhesive properties with A) is placed, and then a molten fiber-reinforced thermoplastic resin containing the thermoplastic resin (A) as a matrix material is fed into the mold. Alternatively, a method for producing a fiber-reinforced thermoplastic resin molded article is characterized in that after supplying, the mold is closed and the molded article is cooled under pressure.
以下、本発明における成形方法の例を図面を用いて説明
する。その−例は第1.2図に示すように、複数の多孔
性繊維質シー)(3)、及び熱可塑性樹脂(A)と加圧
下で接着性を有する熱可塑性樹脂(B)よりなるフィル
ム又はシート(4)を閉鎖または未閉鎖の金型内に載置
した後、溶融した熱可塑性樹脂(A)を該多孔性繊維質
シート(3)の層間に供給し、樹脂供給圧力及び/又は
プレス圧力により多孔性繊維質シートの空隙を通し溶融
樹脂を浸透させて、熱可塑性樹脂(B)よりなるシート
又はフィルム(4)と接着させて成形を行う方法である
。Hereinafter, an example of the molding method according to the present invention will be explained using the drawings. An example of this is as shown in Figure 1.2, a film consisting of a plurality of porous fibrous sheets (3) and a thermoplastic resin (A) and a thermoplastic resin (B) that has adhesive properties under pressure. Alternatively, after placing the sheet (4) in a closed or unclosed mold, the molten thermoplastic resin (A) is supplied between the layers of the porous fibrous sheet (3), and the resin supply pressure and/or This is a method in which a molten resin is permeated through the voids of a porous fibrous sheet by press pressure, and is bonded to a sheet or film (4) made of a thermoplastic resin (B) to form the sheet.
また第3.4図は、金型内に熱可塑性樹脂(A)を供給
し、多孔性繊維質シート(3)及び熱可塑性樹脂(B)
よりなるシート又はフィルム(4)を重ねて、多孔性繊
維質シート(3)が溶融した熱可塑性樹脂(A)に面す
る向きとして金型を閉し、多孔性繊維質シート(3)の
空隙を通し溶融した熱可塑性樹脂(A)を浸透させ、熱
可塑性樹脂(B)よりなるシート又はフィルム(4)と
接着させて成形する方法である。In addition, Figure 3.4 shows that the thermoplastic resin (A) is supplied into the mold, and the porous fibrous sheet (3) and the thermoplastic resin (B) are
The mold is closed so that the porous fibrous sheet (3) faces the molten thermoplastic resin (A), and the voids in the porous fibrous sheet (3) are stacked. This is a method in which a molten thermoplastic resin (A) is infiltrated through a thermoplastic resin (B), and then adhered to a sheet or film (4) made of a thermoplastic resin (B) to form the resin.
第5.6図は、未閉鎖の金型内に、熱可塑性樹脂(B)
よりなるフィルム又はシート(4)をi!置し、次いで
熱可塑性樹脂(A)をマトリックス材料とする溶融した
繊維強化熱可塑性樹脂を金型内に供給しながら、又は供
給終了後、金型を閉じ加圧冷却して成形を行う方法であ
る。Figure 5.6 shows thermoplastic resin (B) in an unclosed mold.
A film or sheet (4) consisting of i! Then, after supplying a molten fiber-reinforced thermoplastic resin containing the thermoplastic resin (A) as a matrix material into the mold, or after the supply is finished, the mold is closed and cooled under pressure. be.
本願発明に用いられる熱可塑性樹脂(B)よりなるシー
ト又はフィルムは、ポリエチレン、ポリプロピレン、ポ
リスチレン、アクリロニトリル・スチレン・ブタジェン
共重合体、ポリ塩化ビニル、ポリアミド、ポリカーボネ
ート、ポリエステル、ポリエチレンテレフタレート、ポ
リブチレンテレフタレート、ポリフェニレンエーテル等
の熱可塑性樹脂、及びこれらの混合物、これらの熱可塑
性樹脂を用いたポリマーアロイ等よりなるシート又はフ
ィルムである。The sheet or film made of the thermoplastic resin (B) used in the present invention includes polyethylene, polypropylene, polystyrene, acrylonitrile-styrene-butadiene copolymer, polyvinyl chloride, polyamide, polycarbonate, polyester, polyethylene terephthalate, polybutylene terephthalate, These are sheets or films made of thermoplastic resins such as polyphenylene ether, mixtures thereof, and polymer alloys using these thermoplastic resins.
本発明に用いられる多孔性繊維質シートの材質は、ガラ
ス繊維、カーボン繊維、ステンレス繊維等の無機繊維、
又ボリア瑞ド繊維、ポリエステル繊維、アラミド繊維等
の有機繊維及び無機、有機繊維の混合物を使用すること
ができる。特にガラス繊維の場合は低コストで高い補強
効果が得られる。繊維の直径は1μm〜50μ黴の一般
的に得られる繊維を使用することができる。The material of the porous fibrous sheet used in the present invention includes inorganic fibers such as glass fiber, carbon fiber, and stainless steel fiber;
Also, organic fibers such as boria fibers, polyester fibers, aramid fibers, and mixtures of inorganic and organic fibers can be used. Especially in the case of glass fiber, a high reinforcing effect can be obtained at low cost. Generally available fibers having a diameter of 1 μm to 50 μm can be used.
本願発明における多孔性繊維質シートはシート形状を保
持するため0.5〜50w LXのポリビニルアルコー
ル、エポキシ樹脂等の凝結剤を用いたものを使用しても
よい、又単純シート形状のものを用いてもよいし、あら
かじめ成形品の形に予備賦形されたシートを用いてもよ
い、一方不連続の単繊維シートの繊維の長さは100m
m以下であり、単繊維シートの製造上、又得られる機械
的強度から、さらに好ましくは1〜50m+−である0
本願発明で成形に用いる複数の繊維質シートは同質のも
のの組合せでも、又異質のものの組合せでも良く、用途
、要求性能に応じて組合せ方を選択することができる。The porous fibrous sheet in the present invention may be one using a coagulant such as 0.5 to 50w LX polyvinyl alcohol or epoxy resin in order to maintain the sheet shape, or it may be a simple sheet shape. Alternatively, a sheet preformed into the shape of a molded article may be used; on the other hand, the fiber length of the discontinuous monofilament sheet may be 100 m.
m or less, and more preferably from 1 to 50 m+- from the viewpoint of manufacturing the single fiber sheet and the mechanical strength obtained.
The plurality of fibrous sheets used for molding in the present invention may be a combination of the same or different types, and the combination can be selected depending on the application and required performance.
本願発明に用いられる熱可塑性樹脂(A)はポリエチレ
ン、ポリプロピレン、ポリスチレン、アクリロニトリル
・スチレン・ブタジェン共重合体、ポリ塩化ビニル、ポ
リアミド、ポリカーボネート、ポリエチレンテレフタレ
ート、ポリブチレンテレフタレート、ポリフェニレンエ
ーテル、スチレン・アクリロニトリル重合体等の熱可塑
性樹脂、及びこれらの混合物、これらの熱可塑性樹脂を
用いたポリマーアロイ等が用いられる。又さらにこれら
の熱可塑性樹脂にクルク、ワラストナイト、ガラス繊維
等の無機充填剤などを含有させて成形収縮率を10/1
000以下、及び曲げ弾性率を24000kg/cm”
以上にしたものも用いられる。これらの熱可塑性樹脂に
は熱安定剤、紫外線防止剤、などの添加剤、また着色剤
、ゴムなどを含んでいてもよい。The thermoplastic resin (A) used in the present invention is polyethylene, polypropylene, polystyrene, acrylonitrile/styrene/butadiene copolymer, polyvinyl chloride, polyamide, polycarbonate, polyethylene terephthalate, polybutylene terephthalate, polyphenylene ether, styrene/acrylonitrile polymer. Thermoplastic resins such as, mixtures thereof, polymer alloys using these thermoplastic resins, etc. are used. Furthermore, by incorporating inorganic fillers such as curk, wollastonite, and glass fiber into these thermoplastic resins, the molding shrinkage rate can be reduced to 10/1.
000 or less, and the bending elastic modulus is 24,000 kg/cm”
The above may also be used. These thermoplastic resins may contain additives such as heat stabilizers and ultraviolet inhibitors, as well as colorants, rubbers, and the like.
繊維強化熱可塑性樹脂を用いる場合には、好ましくは1
m+i〜50+im長さの比較的長い繊維を分散した樹
脂を用いる。このような樹脂を得るには、中繊維長の繊
維を分散したベレットを用いる方法があるが、この場合
成形機の可塑化工程で繊維の切断が著しく、機械的強度
の向上が期待できない。When using a fiber-reinforced thermoplastic resin, preferably 1
A resin in which relatively long fibers having a length of m+i to 50+im are dispersed is used. In order to obtain such a resin, there is a method of using pellets in which medium-length fibers are dispersed, but in this case, the fibers are significantly cut during the plasticization process of the molding machine, and no improvement in mechanical strength can be expected.
このため本願発明者らは第7図に示す可塑化装置を考案
した。可塑化装置は(12)の加熱シリンダーと(II
)のスクリューから成っている。For this reason, the inventors of the present invention devised a plasticizing device shown in FIG. The plasticizing device consists of a heating cylinder (12) and a heating cylinder (II).
) consists of a screw.
(8)は熱可塑性樹脂供給口、(9)は繊維供給口で外
側にロービングカッター等の繊維の定量的供給装置をも
うける。(10)は脱気口で、繊維と共にとりこまれた
空気等を脱気する。(13)は可塑化装置のノズルであ
る。スクリュー長さ/スクリュー径の比は少なくとも1
5以上で、シリンダー中央部に繊維供給口、及びそれよ
りノズル側に脱気口をそれぞれ設ける。さらにノズルの
先端をアキュームレーター(第8図)に接続した装置(
第9図)を用いる。第8図のアキュームレターにおいて
、(21)は可塑化装置との接続口で、溶融樹脂が供給
される。(14)は油圧のピストン・シリンダーで、(
15)は溶融樹脂シリンダーで(16)、(17)部分
はピストンを示す。(18)は(14)及び(15)を
支える支持架である。(19)(20)の出入口を通し
て出入する油でピストンを動かしくI5)のシリンダー
に貯えられた溶融樹脂を(22)の吐出口から射出する
。(8) is a thermoplastic resin supply port, and (9) is a fiber supply port, and a quantitative fiber supply device such as a roving cutter is provided on the outside. (10) is a deaeration port, which deaerates air, etc. taken in with the fibers. (13) is the nozzle of the plasticizing device. The screw length/screw diameter ratio is at least 1
5 or more, a fiber supply port is provided in the center of the cylinder, and a deaeration port is provided closer to the nozzle than the fiber supply port. Furthermore, a device (see Fig. 8) with the tip of the nozzle connected to an accumulator (
Figure 9) is used. In the accumulation letter of FIG. 8, (21) is a connection port with a plasticizing device, through which molten resin is supplied. (14) is a hydraulic piston cylinder, (
15) is a molten resin cylinder, and (16) and (17) are pistons. (18) is a support frame that supports (14) and (15). (19) The piston is moved by the oil flowing in and out through the inlet and outlet port in (20).The molten resin stored in the cylinder in I5) is injected from the discharge port in (22).
本装置(第9図)を用いることにより、従来にない長い
繊維の分散した熔融樹脂を得ることが可能であり、機械
的強度が著しく高く、かつ低コストの製品を得ることが
できる。スクリュー長さ/スクリュー径の比がI5以下
の場合、中央I&i1m供給口から脱気口までの長さ、
及び繊維供給口からノズル先端までの長さが短すぎ熔融
樹脂中に投入された繊維が十分分散せず、また脱気も不
十分となる。By using this apparatus (FIG. 9), it is possible to obtain a molten resin in which long fibers are dispersed, which is unprecedented, and a product with extremely high mechanical strength and low cost can be obtained. If the screw length/screw diameter ratio is I5 or less, the length from the central I & i1m supply port to the deaeration port,
Also, the length from the fiber supply port to the nozzle tip is too short, resulting in insufficient dispersion of the fibers introduced into the molten resin and insufficient deaeration.
本願発明で可塑化装置の繊維供給口から投入される繊維
は単繊維および数十本から数百本の単繊維を集束剤で集
束した集束繊維のいずれも使用することができ、又1m
mから50mmにあらかしめ切断した繊維でも、又長い
繊維を繊維供給口で切断して供給してもよい、材質は、
ガラス繊維、カーボン繊維、ステンレス繊維等の無機繊
維、又ポリアミド繊維、ポリエステル繊維、アラミド繊
維等の有機繊維及び無機、有機繊維の混合物を使用する
ことができる。In the present invention, the fibers inputted from the fiber supply port of the plasticizing device can be either single fibers or bundled fibers made by binding tens to hundreds of single fibers with a binding agent, and 1 m
The fibers may be roughly cut from m to 50 mm, or long fibers may be cut and fed at the fiber supply port.The materials are as follows:
Inorganic fibers such as glass fibers, carbon fibers and stainless steel fibers, organic fibers such as polyamide fibers, polyester fibers and aramid fibers, and mixtures of inorganic and organic fibers can be used.
本願発明において、その成形過程で熔融樹脂は多孔性繊
維シートの間隙を圧力により流動していくが流動抵抗が
大きくかつ特に無機繊維の場合は繊維により熱をうばわ
れ樹脂温度の低下が大きいため流動性が低下し、成形品
表面までの樹脂の浸透性が不充分となることがあるが、
これを防ぐためには用いる繊維質シートを金型内に載置
する前に例えば60°C以上に予備加熱しておくことが
効果的である。In the present invention, during the molding process, the molten resin flows through the gaps between the porous fiber sheets due to pressure, but the flow resistance is large, and especially in the case of inorganic fibers, the heat is carried away by the fibers, resulting in a large drop in resin temperature, so the molten resin flows. However, the permeability of the resin to the surface of the molded product may be insufficient.
In order to prevent this, it is effective to preheat the fibrous sheet to, for example, 60° C. or higher before placing it in the mold.
〈実施例〉
以下、本発明の実施例を示すが、本発明はこれに限定さ
れるものではない、なお、実施例中の成形品の試験法は
以下のとおりである。<Examples> Examples of the present invention will be shown below, but the present invention is not limited thereto. The test methods for molded products in the examples are as follows.
曲げ試験:JIS K7203に準拠し、三点支持法
で行なった。なおテストピースは第11図の箱型成形品
の底面部及びリブ部から切り出した2IIIO+厚×1
0閣巾X90mn長のものを用い23°Cの条件下でテ
ストを実施した。Bending test: Conducted in accordance with JIS K7203 using a three-point support method. The test piece was 2IIIO + thickness x 1 cut out from the bottom and rib parts of the box-shaped molded product shown in Figure 11.
The test was carried out under the condition of 23°C using a piece with a width of 0 mm and a length of 90 mm.
落錘衝撃試験:第12図に示す装置を用いて実施した。Falling weight impact test: Conducted using the apparatus shown in FIG.
ガラス繊維強化成形品から切り出した50oiX50+
+wX2+am厚のテストピース(30)上に撃芯(2
つ)を置き、荷重(28)を上方から撃芯(29)上に
落下させ、テストピースが破壊される時の荷重(28)
の最低高さをもって破壊高さとし、下式により得られた
破壊エネルギーをもって衝撃強度とした。50oiX50+ cut out from glass fiber reinforced molded product
+wX2+am thick test piece (30) with striking core (2
), and a load (28) is dropped from above onto the striking core (29), and the load (28) at which the test piece is destroyed is
The lowest height of the specimen was taken as the fracture height, and the fracture energy obtained by the formula below was taken as the impact strength.
破壊エネルギー(Kg−cm)=荷重(Kg)X破壊高
さ(cs+)成形品の変形;第10図の箱型成形品の底
面を下にして平板上に置き4つの角部をおのおの別々に
平板上に押さえつけた時、残りの角部で最も平板より離
れた高さをもって成形品の変形量とした。Fracture energy (Kg-cm) = Load (Kg) x Fracture height (cs+) Deformation of the molded product: Place the box-shaped molded product shown in Figure 10 on a flat plate with the bottom facing down, and separate each of the four corners separately. When pressed onto a flat plate, the height of the remaining corners farthest from the flat plate was defined as the amount of deformation of the molded product.
成形品の表面外観:表面粗さ計(東洋精密■製、超粗さ
計StlRFCOM )を用いて成形品の表面粗さを測
定した。Surface appearance of molded product: The surface roughness of the molded product was measured using a surface roughness meter (super roughness meter StlRFCOM, manufactured by Toyo Seimitsu ■).
(実施例1)
200トンの型締力を有する竪型ブレス成形機を使用し
成形テストを実施した。金型は上型及び下型の2つの部
分からなり、下型には中央部に直径2mmの熔融樹脂の
全型内供給口とそれにつながる部分としてマニホールド
を有する。用いた金型は製品向yL2.0IIIl、製
品寸法200mm長さx 200m県巾X 40111
11高さの箱型成形品(第10図)の型を用いた。(Example 1) A molding test was conducted using a vertical press molding machine having a mold clamping force of 200 tons. The mold consists of two parts, an upper mold and a lower mold, and the lower mold has a 2 mm diameter in-mold supply port for the molten resin in the center and a manifold as a part connected thereto. The mold used was product direction L2.0III, product dimensions 200mm length x 200m prefecture width x 40111
A box-shaped molded product (FIG. 10) with a height of 11 was used.
最初にpp/EPDM/ナイロン6からなる300μの
厚みの押出しシート(住友化学工業(株)製フレックス
ロイ@D−2000)を2枚置き、多孔性繊維質シート
として日本バイリーン社製のキュムラス・シートVHM
5075を8枚重ねて載置した。このうち下側の押出シ
ート2枚及び繊維質シート4枚は熔融樹脂供給口の位置
に直径10mmの穴を作成した。繊維質ソートは60°
Cに予熱したものを用いた。さらにその上にフレックス
ロイ@D−2000を2枚置き、該穴を通して繊維質シ
ートの層間に溶融した熱可塑性樹脂(住友化学工業(株
)製ポリプロピレン樹脂、住友ノーブレン@AX568
(エチレン−プロピレン共重合体、メルトフローインデ
ックス 65g710分)を供給し、樹脂にかかる圧力
を100kg/cm”で成形をおこなった。第1表に示
す如く、表面光沢、寸法安定性、機械的強度の優れた成
形品が得られた。First, two 300μ thick extruded sheets made of pp/EPDM/nylon 6 (Flexroy@D-2000 manufactured by Sumitomo Chemical Co., Ltd.) were placed, and Cumulus sheet manufactured by Nippon Vilene Co., Ltd. was used as a porous fibrous sheet. V.H.M.
Eight sheets of 5075 were placed one on top of the other. Among these, two extruded sheets and four fibrous sheets on the lower side had a hole with a diameter of 10 mm at the position of the molten resin supply port. Fiber sorting is 60°
The one preheated to C was used. Furthermore, two sheets of Flexloy@D-2000 were placed on top of it, and a thermoplastic resin (polypropylene resin manufactured by Sumitomo Chemical Co., Ltd., Sumitomo Noblen@AX568) was melted between the layers of the fibrous sheet through the holes.
(ethylene-propylene copolymer, melt flow index: 65 g, 710 minutes) was supplied, and molding was performed at a pressure of 100 kg/cm" on the resin. As shown in Table 1, surface gloss, dimensional stability, and mechanical strength were obtained. An excellent molded product was obtained.
(実施例2)
熱可塑性樹脂に住友化学工業(株)製ポリプロピレン樹
脂、住友ノープレン@BWH44(タルク40%含有、
成形収縮率8/1000、曲げ弾性率52000Kg/
cj)を用いて成形を行った。他の条件はすべて実施例
1と同一条件でテストを実施した。第1表に示す如く、
表面光沢、寸法安定性、機械的強度の優れた成形品が得
られた。(Example 2) The thermoplastic resin was polypropylene resin manufactured by Sumitomo Chemical Co., Ltd., Sumitomo Noprene@BWH44 (containing 40% talc,
Molding shrinkage rate 8/1000, bending elastic modulus 52000Kg/
The molding was carried out using a molding method (cj). All other conditions were the same as in Example 1, and the test was conducted. As shown in Table 1,
A molded article with excellent surface gloss, dimensional stability, and mechanical strength was obtained.
(実施例3)
下金型上に樹脂供給口より溶融した熱可塑性樹脂(住友
ノーブレン@BWH44)を供給し、次いで、多孔性繊
維質シート(日本バイリーン社製のキュムラス・シート
VHM5075)8枚、及び熱可塑性樹脂よりなるシー
ト(住友化学工業■製フレックスロイ■D−2000)
2枚を順次重ねで置き、金型を閉して成形を行った。第
1表に示す通り成形品の外観、機械的強度共に優れたも
のであった。(Example 3) Melted thermoplastic resin (Sumitomo Noblen@BWH44) was supplied from the resin supply port onto the lower mold, and then 8 porous fibrous sheets (Cumulus Sheet VHM5075 manufactured by Nippon Vilene Co., Ltd.) were and a sheet made of thermoplastic resin (Flexroy D-2000 manufactured by Sumitomo Chemical Co., Ltd.)
The two sheets were placed one on top of the other, the mold was closed, and molding was performed. As shown in Table 1, the molded product had excellent appearance and mechanical strength.
(実施例4)
まず、金型内にフレックスロイ@ D −2000(樹
脂供給口の位置に直径10祁の穴を作成)2枚を載置し
た。(Example 4) First, two sheets of Flexloy@D-2000 (a hole with a diameter of 10 mm was created at the position of the resin supply port) were placed in a mold.
直径50Iifflのフルフラクト・クイブのスクリュ
ーをもち、スクリュー長さ/スクリュー直径の比は29
、シリンダー後方にマトリックス樹脂供給口、中央部に
は繊維材料供給口、繊維材料供給口とノズルの中間部に
脱気口を有する構造から成っている可塑化装置を用い、
ポリプロピレン樹脂住友ノーブレンAX56B(メルト
フローインデックス 65g/io分)をマトリックス
樹脂供給口より投入し、繊維材料として日本硝子繊維■
製ガラスファイバー・ロービング RER231−3M
14をロービングカッターを用いて13o長さに切断し
、繊維材料供給口よりポリプロピレン樹脂に対し30重
量パーセントの充填量となる量を投入し、得られた長繊
維分散溶融樹脂をアキュームレーターに充填し、金型内
の溶融樹脂供給口を通じて、すでに載置した熱可塑性樹
脂よりなるシート上に、該シートに設けた穴を通して上
記溶融樹脂を供給し金型を閉し成形を行った。第1表に
示す通り成形品の外観、機械的強度共に優れたものであ
った。It has a full-fract quib screw with a diameter of 50 Iiffl and a screw length/screw diameter ratio of 29.
, using a plasticizing device consisting of a matrix resin supply port at the rear of the cylinder, a fiber material supply port in the center, and a deaeration port in the middle of the fiber material supply port and the nozzle.
Polypropylene resin Sumitomo Noblen AX56B (melt flow index 65 g/io min) was introduced from the matrix resin supply port, and Nippon Glass Fiber ■ was added as a fiber material.
Made of glass fiber roving RER231-3M
14 was cut into a length of 13o using a roving cutter, and an amount of polypropylene resin with a filling amount of 30% by weight was added from the fiber material supply port, and the obtained long fiber-dispersed molten resin was filled into an accumulator. The molten resin was supplied through a hole provided in the sheet onto a sheet of thermoplastic resin already placed through a molten resin supply port in the mold, and the mold was closed to perform molding. As shown in Table 1, the molded product had excellent appearance and mechanical strength.
(比較例1)
熱可塑性樹脂よりなるシート(フレックスロイ@D−2
0(10)を使用せずに成形を行った。他の条件はすべ
て実施例1と同一条件でテストを実施した。(Comparative Example 1) Sheet made of thermoplastic resin (Flexroy@D-2
Molding was carried out without using 0(10). All other conditions were the same as in Example 1, and the test was conducted.
(比較例2)
多孔性繊維質シート及び熱可塑性P4脂よりなるシート
を使用せずに成形を行った。他の条件はすべて実施例1
と同一条件でテストを実施した。(Comparative Example 2) Molding was performed without using a porous fibrous sheet or a sheet made of thermoplastic P4 resin. All other conditions are Example 1
The test was conducted under the same conditions.
〈発明の効果〉
本発明の様に、最外層に熱可塑性樹脂(A)と接着性を
有する熱可塑性樹脂(B)よりなるフィルム又はシート
を用い、繊維質シート又は繊維強化熱可塑性樹脂と組み
合わせることにより、高剛性で変形がなく、かつ美しい
樹脂表面外観を有する製品を得ることが可能である。又
、得られる製品の成形収縮率は異方性がなくきわめて小
さい。<Effects of the Invention> As in the present invention, a film or sheet made of a thermoplastic resin (A) and a thermoplastic resin (B) having adhesive properties is used as the outermost layer, and is combined with a fibrous sheet or a fiber-reinforced thermoplastic resin. By doing so, it is possible to obtain a product with high rigidity, no deformation, and a beautiful resin surface appearance. Furthermore, the molding shrinkage rate of the obtained product is extremely small and has no anisotropy.
上述の如く、本発明による繊維強化成形技術を用いると
成形と同時に強化でき、従来法に比較しきわめて低コス
トで、特に表面外観が美しくかつ機械的強度の優れた繊
維強化成形品を容易に得ることができ、また製品の要求
性能に応して各種の繊維の組合せが可能で自動車部品、
家電部品、建築用材料等の広範囲な用途分野の繊維強化
製品を提供することが可能とな、った。As mentioned above, by using the fiber-reinforced molding technology of the present invention, reinforcement can be achieved at the same time as molding, and fiber-reinforced molded products with particularly beautiful surface appearance and excellent mechanical strength can be easily obtained at extremely low cost compared to conventional methods. It is also possible to combine various fibers according to the required performance of the product.
This makes it possible to provide fiber-reinforced products for a wide range of applications, such as home appliance parts and building materials.
第1〜6図は、本発明の成形方法を示す装置の縦の断面
図である。
(1)上金型 (2)下金型(3)多孔性繊
維質シート
(4)熱可塑性樹脂(B)よりなるフィルム又はシート
(5a)溶融した熱可塑性樹脂
(5b)溶融した繊維強化熱可塑性樹脂(6)溶融樹脂
供給口
(7)ポータプル押出機
第7図は本発明におけるマトリックス樹脂と繊維の混練
用可塑化装置の断面図を示す。
(8)マトリックス樹脂供給口
(9)繊維材料供給口
(10)脱気口
(11)スクリュー
(12)シリンダー
(13)ノズル
第8図は本発明の実施例で用いたアキュームレーターの
断面図である。
(14)油圧シリンダー
(15)溶融樹脂シリンダー
(16)油圧用ピストン
(17)溶融樹脂用ピストン
(18)シリンダー固定具
(19)オイル出入口
(20〉オイル出入口
(21)溶融樹脂供給口
(22)熔融樹脂シリンダーノズル
第9図は本発明の実施例に用いられた可塑化装置−アキ
ュームレ−ター−金型の接続図である。
(23)可塑化混練装置
(24)アキュームレーク−
(25)上金型
(26)下金型
(27)マニホールド部
第10図は本発明の実施例の方法でつくった、リブのな
い箱型成形品の斜視図で、第11図はリブを有する箱型
成形品の斜視図である。
第12図は落錘衝撃試験に用いた装置である。
(28)荷重
(29)撃芯
(30)テストピース
(31)テストピース支持具
(32) i!芯先端R(1/2インチ)(a)
(1))
第
図
(6)
(fi)
(6)
(1))
第
図
(J)
(1))
第
図
(d)
(1))
第
図
(a)
(1))
第
図
8
25
第
図
第
関1 to 6 are longitudinal cross-sectional views of an apparatus illustrating the molding method of the present invention. (1) Upper mold (2) Lower mold (3) Porous fibrous sheet (4) Film or sheet made of thermoplastic resin (B) (5a) Melted thermoplastic resin (5b) Melted fiber reinforced heat Plastic resin (6) Molten resin supply port (7) Portable extruder FIG. 7 shows a sectional view of a plasticizing device for kneading matrix resin and fibers in the present invention. (8) Matrix resin supply port (9) Fiber material supply port (10) Deaeration port (11) Screw (12) Cylinder (13) Nozzle Figure 8 is a cross-sectional view of the accumulator used in the example of the present invention. be. (14) Hydraulic cylinder (15) Molten resin cylinder (16) Hydraulic piston (17) Molten resin piston (18) Cylinder fixture (19) Oil inlet/outlet (20> Oil inlet/outlet (21) Molten resin supply port (22) Molten resin cylinder nozzle Figure 9 is a connection diagram of the plasticizing device, accumulator, and mold used in the embodiment of the present invention. (23) Plasticizing and kneading device (24) Accumulator rake - (25) Top Mold (26) Lower mold (27) Manifold portion FIG. 10 is a perspective view of a box-shaped molded product without ribs, made by the method of the embodiment of the present invention, and FIG. 11 is a box-shaped molded product with ribs. Fig. 12 is the device used for the falling weight impact test. (28) Load (29) Percussion core (30) Test piece (31) Test piece support (32) i! Core tip R (1/2 inch) (a) (1)) Fig. (6) (fi) (6) (1)) Fig. (J) (1)) Fig. (d) (1)) Fig. ( a) (1)) Figure 8 25 Figure No.
Claims (4)
質シートの層間に供給し、樹脂供給圧力及び/又はプレ
ス圧力により多孔性繊維質シートの空隙を通し該熱可塑
性樹脂(A)を浸透させて、多孔性繊維質シートの最外
層面に位置した、熱可塑性樹脂(A)と接着性を有する
熱可塑性樹脂(B)よりなるシート又はフィルムと接着
させることを特徴とする繊維強化熱可塑性樹脂成形品の
製造方法。(1) A molten thermoplastic resin (A) is supplied between the layers of a plurality of porous fibrous sheets, and the thermoplastic resin (A) is passed through the voids of the porous fibrous sheets by resin supply pressure and/or press pressure. The fiber reinforcement is characterized in that it is bonded to a sheet or film made of a thermoplastic resin (B) which is located on the outermost layer surface of a porous fibrous sheet and has adhesive properties with the thermoplastic resin (A). Method for manufacturing thermoplastic resin molded products.
供給し、多孔性繊維質シート及び熱可塑性樹脂(A)と
接着性を有する熱可塑性樹脂(B)よりなるシート又は
フィルムを重ねて、多孔性繊維質シートが溶融した熱可
塑性樹脂(A)に面する向きに載置し、金型を閉じ多孔
性繊維質シートの空隙を通し溶融した熱可塑性樹脂(A
)を浸透させ、熱可塑性樹脂(B)よりなるシート又は
フィルムと接着させることを特徴とする繊維強化熱可塑
性樹脂成形品の製造方法。(2) A sheet or film made of a porous fibrous sheet and a thermoplastic resin (B) that has adhesive properties with the thermoplastic resin (A) by supplying the molten thermoplastic resin (A) into an unclosed mold. The porous fibrous sheets are stacked and placed so that they face the molten thermoplastic resin (A), the mold is closed, and the molten thermoplastic resin (A) is passed through the voids of the porous fibrous sheets.
) and adhering it to a sheet or film made of thermoplastic resin (B).
率が24000kg/cm^2以上である熱可塑性樹脂
(A)を用いることを特徴とする特許請求の範囲第1項
又は第2項記載の繊維強化熱可塑性樹脂成形品の製造方
法。(3) A thermoplastic resin (A) having a molding shrinkage rate of 10/1000 or less and a flexural modulus of 24000 kg/cm^2 or more is used. A method for manufacturing a fiber-reinforced thermoplastic resin molded product.
を有する熱可塑性樹脂(B)よりなるフィルム又はシー
トを載置し、次いで熱可塑性樹脂(A)をマトリックス
材料とする溶融した繊維強化熱可塑性樹脂を金型内に供
給しながら又は供給した後、金型を閉じ加圧冷却して成
形することを特徴とする繊維強化熱可塑性樹脂成形品の
製造方法。(4) A film or sheet made of a thermoplastic resin (A) and a thermoplastic resin (B) having adhesive properties is placed in an unclosed mold, and then the thermoplastic resin (A) is used as a matrix material. A method for producing a fiber-reinforced thermoplastic resin molded article, which comprises supplying or after supplying a molten fiber-reinforced thermoplastic resin into a mold, closing the mold and cooling under pressure.
Priority Applications (11)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2059428A JP2917372B2 (en) | 1990-03-09 | 1990-03-09 | Method for producing fiber-reinforced thermoplastic resin molded article |
| ES90912373T ES2077684T3 (en) | 1989-08-21 | 1990-08-21 | METHOD TO PRODUCE A MOLDED ARTICLE OF THERMOPLASTIC RESIN REINFORCED WITH FIBER. |
| CA002039160A CA2039160C (en) | 1989-08-21 | 1990-08-21 | Method for producing molded article of fiber-reinforced thermoplastic resin |
| DE69021361T DE69021361T2 (en) | 1989-08-21 | 1990-08-21 | METHOD FOR PRODUCING A FIBER REINFORCED THERMOPLASTIC PLASTIC MOLDED PRODUCT. |
| US07/684,912 US5275776A (en) | 1989-08-21 | 1990-08-21 | Method for producing molded article of fiber-reinforced thermoplastic resin |
| PCT/JP1990/001060 WO1991002639A1 (en) | 1989-08-21 | 1990-08-21 | Method of manufacturing fiber-reinforced thermoplastic resin molded product |
| KR1019910700396A KR0181510B1 (en) | 1989-08-21 | 1990-08-21 | Manufacturing method of fiber-reinforced thermoplastic molded article |
| EP90912373A EP0439625B1 (en) | 1989-08-21 | 1990-08-21 | Method of manufacturing fiber-reinforced thermoplastic resin molded product |
| EP19900119733 EP0423676A3 (en) | 1989-10-16 | 1990-10-15 | Method for producing molded article of fiber-reinforced thermoplastic resin |
| CA002027741A CA2027741A1 (en) | 1989-10-16 | 1990-10-16 | Method for producing molded article of fiber-reinforced thermoplastic resin |
| US08/080,119 US5424020A (en) | 1989-08-21 | 1993-06-23 | Method for producing molded article of fiber-reinforced thermoplastic resin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2059428A JP2917372B2 (en) | 1990-03-09 | 1990-03-09 | Method for producing fiber-reinforced thermoplastic resin molded article |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11002808A Division JP3006609B2 (en) | 1999-01-08 | 1999-01-08 | Method for producing fiber-reinforced thermoplastic resin molded article |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03261519A true JPH03261519A (en) | 1991-11-21 |
| JP2917372B2 JP2917372B2 (en) | 1999-07-12 |
Family
ID=13112985
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2059428A Expired - Fee Related JP2917372B2 (en) | 1989-08-21 | 1990-03-09 | Method for producing fiber-reinforced thermoplastic resin molded article |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2917372B2 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2012172982A1 (en) * | 2011-06-16 | 2012-12-20 | 東レ株式会社 | Method for manufacturing fiber-reinforced plastic |
| JP2014138993A (en) * | 2013-01-21 | 2014-07-31 | Japan Steel Works Ltd:The | Method for producing fiber-reinforced resin base material or resin molded body, and plasticization discharging machine used for production method |
| JP2015094995A (en) * | 2013-11-08 | 2015-05-18 | 富士通株式会社 | Housing parts and manufacturing method thereof |
| JP2020528845A (en) * | 2017-07-24 | 2020-10-01 | エアライト、インコーポレイテッド. | Fiber reinforced molding compound and its formation and usage |
-
1990
- 1990-03-09 JP JP2059428A patent/JP2917372B2/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2012172982A1 (en) * | 2011-06-16 | 2012-12-20 | 東レ株式会社 | Method for manufacturing fiber-reinforced plastic |
| JPWO2012172982A1 (en) * | 2011-06-16 | 2015-02-23 | 東レ株式会社 | Manufacturing method of fiber reinforced plastic |
| US9011747B2 (en) | 2011-06-16 | 2015-04-21 | Toray Industries, Inc. | Method for manufacturing fiber-reinforced plastic |
| JP2014138993A (en) * | 2013-01-21 | 2014-07-31 | Japan Steel Works Ltd:The | Method for producing fiber-reinforced resin base material or resin molded body, and plasticization discharging machine used for production method |
| JP2015094995A (en) * | 2013-11-08 | 2015-05-18 | 富士通株式会社 | Housing parts and manufacturing method thereof |
| JP2020528845A (en) * | 2017-07-24 | 2020-10-01 | エアライト、インコーポレイテッド. | Fiber reinforced molding compound and its formation and usage |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2917372B2 (en) | 1999-07-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5275776A (en) | Method for producing molded article of fiber-reinforced thermoplastic resin | |
| KR0159510B1 (en) | Method of preparing thermoplastic resin product reinforced with fibers | |
| JP7023963B2 (en) | Combined primary and carbon fiber components in the production of reinforced polymer articles | |
| JPH0440373B2 (en) | ||
| EP0423676A2 (en) | Method for producing molded article of fiber-reinforced thermoplastic resin | |
| JPH03261519A (en) | Manufacture of fiber reinforced thermoplastic resin molded product | |
| EP0296611B1 (en) | Stamping-moldable material | |
| Bigg | Manufacturing methods for long fiber reinforced polypropylene sheets and laminates | |
| WO2000037243A9 (en) | Low pressure compression molded parts having nano-particle reinforced protrusions and method of making the same | |
| JP2748604B2 (en) | Method for producing fiber-reinforced thermoplastic resin molded article | |
| JP3019527B2 (en) | Fiber-reinforced thermoplastic resin molded article and molding method thereof | |
| JP2822465B2 (en) | Method for producing fiber reinforced thermoplastic resin product | |
| EP1790454B1 (en) | Process for producing an exterior body comprising long fiber reinforced thermoplastic resin | |
| JPH032011A (en) | Method for manufacturing fiber-reinforced thermoplastic resin molded products | |
| JP2697077B2 (en) | Method for producing fiber-reinforced thermoplastic resin molded article | |
| JPH10211667A (en) | Thermoplastic polymer composite panel for plywood replacement | |
| JP2697107B2 (en) | Method for producing fiber-reinforced thermoplastic resin molded article | |
| JP3006609B2 (en) | Method for producing fiber-reinforced thermoplastic resin molded article | |
| EP0646684A1 (en) | Water-permeable concrete formwork | |
| JP3032582B2 (en) | Method for improving appearance of fiber-reinforced thermoplastic resin molded product | |
| JPH0332836A (en) | Composite molding sheet | |
| Bigg | Manufacturing methods for long fiber reinforced polypropylene | |
| JP2007112028A (en) | Method and apparatus for manufacture of recycle plastic panel | |
| JPH06210782A (en) | Fiber-reinforced thermoplastic resin porous molded article and molding method thereof | |
| JPH11182030A (en) | Resin concrete casting formwork |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| S531 | Written request for registration of change of domicile |
Free format text: JAPANESE INTERMEDIATE CODE: R313531 |
|
| S533 | Written request for registration of change of name |
Free format text: JAPANESE INTERMEDIATE CODE: R313533 |
|
| R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080423 Year of fee payment: 9 |
|
| RD05 | Notification of revocation of power of attorney |
Free format text: JAPANESE INTERMEDIATE CODE: R3D05 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090423 Year of fee payment: 10 |
|
| LAPS | Cancellation because of no payment of annual fees |