JPH0369701B2 - - Google Patents
Info
- Publication number
- JPH0369701B2 JPH0369701B2 JP63117549A JP11754988A JPH0369701B2 JP H0369701 B2 JPH0369701 B2 JP H0369701B2 JP 63117549 A JP63117549 A JP 63117549A JP 11754988 A JP11754988 A JP 11754988A JP H0369701 B2 JPH0369701 B2 JP H0369701B2
- Authority
- JP
- Japan
- Prior art keywords
- shaping
- fiber
- mold
- reinforced resin
- resin molded
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000007493 shaping process Methods 0.000 claims description 83
- 238000007906 compression Methods 0.000 claims description 55
- 230000006835 compression Effects 0.000 claims description 55
- 238000001816 cooling Methods 0.000 claims description 37
- 238000010438 heat treatment Methods 0.000 claims description 37
- 229920005989 resin Polymers 0.000 claims description 31
- 239000011347 resin Substances 0.000 claims description 31
- 238000000034 method Methods 0.000 claims description 30
- 230000001788 irregular Effects 0.000 claims description 11
- 239000000463 material Substances 0.000 description 68
- 239000000546 pharmaceutical excipient Substances 0.000 description 19
- 238000000748 compression moulding Methods 0.000 description 18
- 239000000835 fiber Substances 0.000 description 17
- 229920005992 thermoplastic resin Polymers 0.000 description 10
- 230000009477 glass transition Effects 0.000 description 8
- 238000005452 bending Methods 0.000 description 6
- 238000000465 moulding Methods 0.000 description 5
- 230000014759 maintenance of location Effects 0.000 description 4
- 238000003825 pressing Methods 0.000 description 4
- 229920000049 Carbon (fiber) Polymers 0.000 description 3
- 239000004917 carbon fiber Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000012778 molding material Substances 0.000 description 3
- -1 polypropylene Polymers 0.000 description 3
- 239000002759 woven fabric Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000006082 mold release agent Substances 0.000 description 2
- 239000004745 nonwoven fabric Substances 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 229920005668 polycarbonate resin Polymers 0.000 description 2
- 239000004431 polycarbonate resin Substances 0.000 description 2
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- 229920000271 Kevlar® Polymers 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 239000004696 Poly ether ether ketone Substances 0.000 description 1
- 239000004697 Polyetherimide Substances 0.000 description 1
- 239000004734 Polyphenylene sulfide Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 229920004738 ULTEM® Polymers 0.000 description 1
- 229920001646 UPILEX Polymers 0.000 description 1
- 239000004760 aramid Substances 0.000 description 1
- 229920006231 aramid fiber Polymers 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 229920001903 high density polyethylene Polymers 0.000 description 1
- 239000004700 high-density polyethylene Substances 0.000 description 1
- 150000003949 imides Chemical class 0.000 description 1
- 239000012784 inorganic fiber Substances 0.000 description 1
- 239000004761 kevlar Substances 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 229920002492 poly(sulfone) Polymers 0.000 description 1
- 229920001707 polybutylene terephthalate Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 229920006393 polyether sulfone Polymers 0.000 description 1
- 229920002530 polyetherether ketone Polymers 0.000 description 1
- 229920001601 polyetherimide Polymers 0.000 description 1
- 229920000139 polyethylene terephthalate Polymers 0.000 description 1
- 239000005020 polyethylene terephthalate Substances 0.000 description 1
- 229920000069 polyphenylene sulfide Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 239000012783 reinforcing fiber Substances 0.000 description 1
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 1
- 229910010271 silicon carbide Inorganic materials 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000002966 varnish Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 230000037303 wrinkles Effects 0.000 description 1
Landscapes
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
- Moulding By Coating Moulds (AREA)
Description
[産業上の利用分野]
本発明は、繊維補強樹脂成形体の連続賦形方法
及びその方法を実施するのに適切な装置に関す
る。
[従来の技術]
従来、平面形状を有する繊維補強樹脂成形体を
連続的に一定形状の断面を有する異形成形品に賦
形する方法としては、鋼管を製造する方法として
広く採用されているロールフオーミング法に準じ
た方法が知られている。即ち、複数対の一連の異
形断面を有する成形ロール間を連続的に通すこと
により、加熱された上記成形体を徐々に目的とす
る断面形状に迄曲げ加工し、次いで目的とする断
面形状と同一の断面を有する複数体のロール間を
通過させながら加圧冷却することにより賦形しよ
うとするものである。
[発明が解決しようとする課題]
しかしながら、上記方法では加圧冷却をロール
間で行う為、該成形体が対を形成するロール間に
挟まれている間は加圧されるが、該ロールを離脱
すると該成形体は開放状態、即ち無圧となる為、
該成形体のスプリングバツクにより材料中の空気
が十分に脱泡できず得られる異形成形品の機械強
度が大幅に低下する等の欠点がある。
そこで、本発明者らは、先に昭和63年05年13日
付けの特許願(発明の名称:繊維補強樹脂成形体
の連続賦形方法及びその装置)において、平面形
状を有する繊維補強樹脂成形体を一定形状の断面
を有する異形成形品に加熱圧縮賦形する方法及び
その装置において、その成形体を断続的に移動せ
しめ、該成形体が停止している間に異形断面を有
する上下金型間で加熱圧縮賦形し、次いで加圧冷
却せしめる技術を提案した(以下、これを先提案
技術という)。
本発明者等は更に研究を継続した結果、先提案
技術においては、予備賦形される際、予備賦形ロ
ールの巾方向において当該ロール各部の周長が異
る為、予備賦形ロール各部での周速、即ち賦形材
料の巾方向での各部の移動速度が異なり、このた
め賦形材料が蛇行して安定した賦形が困難なこと
さらに予備賦形後の繊維配向に乱れを生じ、得ら
れる賦形品の機械強度が低下するといつた問題が
あることが判明した。
そこで本発明の目的は、賦形材料の蛇行がなく
従つて安定した賦形が可能である繊維補強樹脂成
形体の連続賦形方法及びその装置を提供すること
にある。
又本発明の他の目的は、繊維配向の乱れがな
く、従つて優れた機械強度を持つ賦形品を製造し
得る繊維補強樹脂成形体の連続賦形方法及びその
装置を提供することにある。
[課題を解決するための手段]
本発明者らは上記目的を達成するため、鋭意検
討を重ねた結果、本発明を完成するに至つたもの
である。
即ち、本発明の繊維補強樹脂成形体の連続賦形
方法は、平面形状を有する繊維補強樹脂成形体を
断続的に予熱・予備賦形し、次いで異形断面を有
する上下金型間で加熱圧縮賦形、圧縮冷却せしめ
ることにより実質的に一定形状の断面を有する異
形成形品に賦形する方法において、当該予備賦形
において上記平面形状を有する繊維補強樹脂成形
体の両端と中央部の高さの差を連続的、又は断続
的に変化せしめることを特徴とする。
また本発明の繊維補強樹脂成形体の連続賦形装
置は、繊維補強樹脂成形体を予熱、予備賦形する
ための予備賦形部と、加熱圧縮賦形のための異形
断面形状を有する上下金型及び圧縮冷却のための
異形断面形状を有する上下金型とを具備する繊維
補強樹脂成形体の連続賦形装置において、当該予
備賦形部が予熱する為の予熱ヒーターと当該繊維
補強樹脂成形体の両端と中央部の高さの差を連続
的、又は断続的に変化させるための端部保持部及
び中央保持部とを具備することを特徴とする。
[発明の構成]
以下、本発明について詳説する。
本発明で用いる賦形材料としては、連続繊維を
一方向に引揃えた繊維シートに熱可塑性樹脂を含
浸させた一方向繊維強化樹脂シート(以下、UD
プリプレグという)、平織、朱子織、綾織等の織
布に上記樹脂を含浸させた多方向繊維強化樹脂シ
ート(以下、織布プリプレグという)、マツト等
の不織布に含浸させた不織布プリプレグがある。
上記プリプレグは単独で、或いは組合せて所望す
る繊維配向、厚みとなる様に積層し、或いは加熱
圧縮成形して、本発明の繊維補強樹脂成形体に供
することができる。特に本発明の連続賦形の前に
加熱圧縮成形することはプリプレグ間に存在する
空気の脱気が可能となり得られる賦形成形品の物
性向上の面から好ましい。
上記加熱圧縮成形する方法としては、例えば特
願昭61−207618号に示すような方法が挙げられ
る。即ち、上記プリプレグを積層しながら寸動移
動する上下ベルト間に送り、次いで当該ベルト間
に挟んだ状態で予熱、加熱圧縮成形、圧縮冷却し
て実際上連続的に成形する方法である。このよう
な方法と本発明とを組合せることによりプリプレ
グを連続的に積層、成形、賦形することも可能で
ある。
本発明で用いる繊維としては、ガラス繊維、炭
素繊維、アラミド繊維(登録商標「ケブラー」
等)等の合成樹脂繊維、炭化ケイ素繊維等の無機
繊維、チタン繊維、ボロン繊維、ステンレス等の
金属繊維等が挙げられるが、これらに限定される
ものではない。
一方、熱可塑性樹脂としては、ポリスチレン、
ポリ塩化ビニル、高密度ポリエチレン、ポリプロ
ピレン、ナイロン、ポリカーボネート、ポリブチ
レンテレフタレート、ポリエチレンテレフタレー
ト、ポリエーテルサルフオン、ポリサルフオン、
ポリエーテルイミド(商標「ULTEM」等)、ポ
リエーテルエーテルケトン、ポリフエニレンサル
フアイド等が挙げられるが、これらに限定される
ものではない。
上記積層されたプリプレグ、又は加熱圧縮成形
して一体化された賦形材料は、予備賦形部へ送ら
れ、先ず予熱されることが好ましい。予熱温度は
熱可塑性樹脂のガラス転移点以上に設定されるの
が一般的である。
予熱された賦形材料は次いで加熱下に例えば当
該材料の両端をピンチロールで挟むかあるいは固
定溝内に保持する等して高さ方向へ移動しないよ
うにし、かつ賦形材料の中央部は上記ピンチロー
ル又は固定溝に対して高さ方向が連続的に又は段
階的に変化し、最終的には目標とする賦形品の端
部と中央部の高さの差と同一となる様に配置した
ガイドロール、ニツプロール等のロール群、平
板、曲板等の板体、丸棒、角棒等の棒状体等と接
触させた状態で長手方向に引取ながら徐々に予備
賦形する。又上記とは逆に賦形材料の両端を高さ
方向に移動せしめ、賦形材料の中央部を高さ方向
に固定することにより予備賦形することも可能で
ある。
上記ピンチロール、ガイドロール等を駆動する
ことは勿論可能である。
以上のようにして予備賦形された賦形材料はつ
いで加熱圧縮賦形のための異形断面を有する上下
金型内に送られ加熱圧縮賦形が開始される。
上記上下金型は当該賦形材料が移動している間
は開いており、当該材料が停止すると同時に当該
上下金型が閉じ、加熱圧縮賦形を行うものであ
る。従つて当該材料は寸動により移動するもので
ある。この一回の移動量を調節することにより当
該材料の同一部分を所望する回数だけ加熱圧縮賦
形することが可能となる。
従つて該金型内で一回の加熱圧縮賦形を受けた
後、次の加圧冷却工程に送られてもよいが、該賦
形材料の脱泡の面からは、複数回同一個所を加熱
圧縮することが好ましい。
尚、賦形材料の移動は、例えば予備賦形部内に
設けられたロール及び/若しくは加圧冷却金型出
口に設けられた引取ロールによつて行われるが、
当該寸動は当該ロールの駆動時間、停止時間を例
えば後述する様にタイマー制御することによつて
達せられる。
加熱温度は熱可塑性樹脂のガラス転移点、好ま
しくは軟化点以上であり、脱泡の面からは高温側
が一般に好ましいが、金型からの離型性を考慮し
て各樹脂毎に実験的に決定されるべきである。
尚、金型に対して運転前、若しくは運転中に離
型剤で処理することは賦形材料の上下金型からの
離型性向上の面から特に好ましい。
又、加圧力については脱泡の面からは高圧が望
ましいが軟化樹脂の流動による繊維配向の乱れを
考慮しなければならない。従つて賦形材料中の繊
維含有率によつて実験的に決定することが望まし
いが、一般に繊維含有率が高くなるに従い高圧に
設定することが可能となる。
加熱圧縮賦形された賦形材料は圧縮冷却用金型
へ送られ、1回若しくは複数回圧縮冷却されるこ
とにより、実際上連続的に繊維補強樹脂成形体を
得ることができる。
冷却温度は熱可塑性樹脂のガラス転移点未満に
設定することが好ましい。ガラス転移点を越える
温度での脱型では一般に賦形品のソリ、賦形品表
面に気泡が残る等の問題を生じるからである。
又、加圧力は前記加熱加圧賦形時の加圧力とは別
に単独に設定してもよいが、通常同圧力に設定さ
れている。
尚、上記加熱圧縮賦形金型及び圧縮冷却金型内
に例えばノツクアウトピン等を付設することは賦
形品の金型からの離脱に対して特に有効である。
該ノツクアウトピンは、加圧時は金型内に納ま
つており金型が開くと同時にピンが金型面から突
出することにより機能するものであるから、該ピ
ンの動きは金型の動きと連動させるべきである。
このようなピンの動きは例えばスプリング、空気
圧等によつて達せられるが、特に空気圧の場合、
例えばエアシリンダーの作動を金型の開閉と連動
することにより可能となる。
次に本発明の詳細を添付図面に示す代表的な実
施例に基き説明する。
第1図は本発明の一実施態様を示す概略側図面
であり、同図に示す如く本発明を実施するための
連続賦形装置は賦形材料Mを供給するためのガイ
ドロール1を有する供給部A、賦形材料を移送す
るためのガイドロール2と賦形材料の両端を保持
して高さ方向に該両端を移動する為のコ字型の溝
を有するガイドレール3、賦形材料の中央部の高
さが上記両端の移動に伴つて変化しないよう保持
する為の平板4及び予熱するための遠赤外線ヒー
ター(図示せず)とを有する予備賦形部B、加熱
圧縮賦形金型5と圧縮冷却金型6と油圧ユニツト
7とを有する圧縮賦形部C、及び賦形後の成形品
を引取るための引取ロール8を有する引取部Dに
より構成される。
賦形材料Mは供給部Aのガイドロール1間を経
由して予備賦形部Bへ送られる。予備賦形部Bに
入ると熱可塑性樹脂のガラス転移点以上、好まし
くは軟化点以上に加熱された賦形材料Mは、第5
図に示す様なコ字型の溝を有するガイドレール
3、平板4を通過させる間の所望の形状に予備賦
形される。
また本発明においては、第6〜8図に示すピン
チロール21、ニツプロール22,23間を通過
する際所望の形状に予備賦形するようにしてもよ
い。また、第9〜11図に示す予備賦形金型62
と賦形材料の両端を押えるためのロール61及び
賦形材料の中央部を押えるためのロール63の間
を通過させる間に所望の形状に予備賦形するよう
にしてもよい。予備賦形金型62はシーズヒータ
ー等によつて熱可塑性樹脂のガラス転移点、好ま
しくは軟化点以上に加熱してもよく、又加熱圧縮
賦形金型内に設けることも可能である。またロー
ル61はその中心軸が賦形材料の引取方向に対し
て図に示すようにある角度θをとるように配置す
ることにより賦形材料の巾方向に張力が発生し、
シワの発生防止の面から好ましい。勿論角度θは
0度であつてもかまわない。
なお上記態様における各ロール対の間隔、予備
賦形金型とロールとの間隔は賦形材料の厚みに合
せて調整できる様に構成されることが好ましい。
又、例えばエアシリンダー等を用いることによ
り加圧下で賦形材料を予備賦形することも可能で
ある。上記加圧力は賦形材料を予備賦形するに足
る圧力であれば十分であり、実験的に決定される
べきである。
このようにして予備賦形された賦形材料は次に
圧縮賦形部Cの加熱圧縮賦形金型5に送られ油圧
ユニツト7により圧縮賦形される。金型の加熱温
度はヒーター又は蒸気等によつて熱可塑性樹脂の
ガラス転移点以上に保たれることが好ましい。
一方、加熱圧縮賦形された当該部分は次いで圧
縮冷却金型6に送られ、油圧ユニツト7により熱
可塑性樹脂のガラス転移点未満まで圧縮冷却され
る。冷却方法としては空冷、水冷、スチーム冷却
等の冷媒を用いる方式が採用される。
油圧ユニツト7は加熱加圧成形と併用する形と
なつているが、勿論加熱加圧成形及び圧縮冷却
各々別個に油圧ユニツトを設け、単独に加圧力を
設定することも可能である。加圧力は0.1〜500
Kg/cm2が好ましい。
本発明において賦形材料の移送は供給部A内の
ガイドロール1、予備賦形部内のガイドロール
2、ピンチロール21(設けられる場合)、ニツ
プロール22,23(設けられる場合)、引取部
D内の引取ロール8のいずれかのロール若しくは
これらを組合せたロール群を寸動移動することに
より行われる。従つて、当該賦形材料は寸動移動
されるものである。即ち、圧縮賦形部Cにおいて
加熱圧縮賦形金型5、及び圧縮冷却金型6が閉じ
る直前にその駆動を停止し、一定時間賦形し、両
金型が開くと同時にその駆動を再開し、当該動作
を繰り返すことにより実際上連続的に賦形材料を
移動するものである。上記寸動駆動の制御は、例
えば上記ロール駆動用及び圧縮賦形用の2つのタ
イマーにより行うことができる。即ち、ロール駆
動用タイマーにより一定時間賦形材料が移動し、
当該タイマーが切れると同時に圧縮賦形用タイマ
ーが作動し、一定時間圧縮賦形して当該タイマー
が切れる。それと同時に再びロール駆動用タイマ
ーが作動し、賦形材料の移動を再開する。尚、上
記方式は一例であり、これに限定されず、マイク
ロコンピユータを用いて自動制御することもでき
る。
本発明で用いるロールのうち予備賦形部B内に
存在するガイドロール2、ピンチロール21、ニ
ツプロール22,23等賦形材料と接する部分、
及び圧縮賦形部Cの加熱圧縮賦形金型5、圧縮冷
却金型6の表面は樹脂との離型性を考慮すること
が好ましい。
従つてこれらの表面は鏡面仕上げをするか、若
しくは適当な離型処理を行うことが望まれる。具
体的にはロール表面にテフロン加工を施すか、若
しくはイミド樹脂(宇部興産社製「UPiLEX
UBE Uワニス」等)等を焼き付ける等の処理を
行うが、その選択に際しては賦形温度を考慮する
必要がある。
又、適当な離型剤、例えばFREKOTE(米国
FREKOTE社製)等を運転前又は運転中に塗布
することも可能である。
本実施例において、加熱圧縮成形金型5、圧縮
冷却金型6には、第12図に示すノツクアウトピ
ンを設けることが好ましく、例えば当該ノツクア
ウトピンを該金型の長さ方向に複数対設けること
は賦形材料の該金型からの離脱を容易ならしめ好
ましい。当該ノツクアウトピンは該金型が閉じて
いる時は金型内に収められているが、該金型が開
くと同時に該金型から突出し、賦形材料を該金型
から離脱する様機能する。
同図においては、例えばノツクアウトピンを下
金型に有する場合、金型が開くと同字にエアシリ
ンダー(図示せず)によつて押板31を経由して
押棒32が移動し、これによりノツクアウトピン
33が上昇して賦形材料を該金型から離脱する。
一方、金型が閉じると同時にエアシリンダーは退
き、スプリング34及び賦形材料による押し下げ
力により、押棒32、ノツクアウトピン33、押
板31は元の位置に戻ることによつて機能する。
又、ノツクアウトピンを上金型に有する場合、
金型が閉じている時は賦形材料の押し上げ力によ
つてノツクアウトピン35は押し上げられている
が、金型が開くと同時にスプリング36の力によ
り賦形材料を押し下げ、該金型から離脱させるも
のである。
尚、上記の方法は一例であり、これらに限定さ
れるものではない。
又、上記加熱圧縮賦形金型5両端のうち、予備
賦形部B側の端を丸くする(Rをとる)ことは賦
形材料の移動を容易ならしめ好ましい。
加熱圧縮賦形金型5と圧縮冷却金型6は各々別
個の金型対により構成することもできる。この場
合、加熱圧縮成形された当該部分が圧縮冷却金型
6に移動するまでに温度低下をきたさないように
加熱圧縮賦形金型5と圧縮冷却金型6を隣接させ
ることが好ましい。
また第13図に示すように一対の上下金型内を
複数個の温度区分に分け、温度制御することによ
り加熱、冷却の両機能を具備させることも可能で
ある。同図において、T−1〜T−10は温度区分
を表す記号である。例えば予備賦形部BをT−1
〜T−2に分け、T−1を200℃、T−2を210℃
に各々温度調節する様にしてもよく、そして予備
賦形後、加熱圧縮賦形部C1をT−3〜T−6に
分け各々を200℃に温度調節し、次いで圧縮冷却
部C2をT−7〜T−10に分け、各々を100℃に温
度調節することもできる。
本発明においては、賦形材料の同一部分を複数
回圧縮成形することができるが、その回数は賦形
材料の移動時間、即ち賦形材料移動タイマーを調
整することにより決定される。即ち、加熱圧縮賦
形金型長さをl(cm)、賦形材料の移動速度をS
(cm/秒)、賦形材料の移動時間をT(秒)とすれ
ば、成形回数Nはl/(S・T)で表される。
又、一回の圧縮成形時間は圧縮成形タイマーを調
整することにより決定される。
尚、加熱圧縮成形回数及び時間は圧縮冷却回数
及び時間と異つていてもよく、この場合、加熱圧
縮成形金型5と圧縮冷却金型6との長さを変える
等の手段を用いればよい。
以上、述べた様に賦形材料を寸動により移動さ
せることにより、賦形材料は実際上連続的に予
熱、予備賦形、加熱圧縮賦形、圧縮冷却され、連
続的に一定形状の断面を有する異形成形品に賦形
することができる。
尚、予備賦形部に用いるロール等の位置、形状
及び加熱圧縮賦形金型、圧縮冷却金型の断面形状
を変えることにより、例えばアングル、チヤンネ
ルの様な異形断面に賦形できることは無論であ
る。
[実施例]
以下、本発明を実施例により説明する。
実施例 1
第1図に示した装置の各部の仕様及び条件を以
下のようにした。
駆動ロール:予備賦形部内のガイドロール2、引
取部内の引取ロール8
駆動ロールの周速:5cm/秒
予備賦形部加熱方式:遠赤外線ヒーターにより第
13図のように2区分で温度調節
加熱圧縮賦形金型、圧縮冷却金型:長さ100cmの
一対の上下金型を各々4分割して温度調節する
ことにより、同一金型内に加熱圧縮賦形部と圧
縮冷却部を形成させた。尚、加熱方式はシーズ
ヒーターによつて行つた。
尚、上記予熱部、加熱圧縮賦形部、圧縮冷却部
の各々の温度区分は第13図に示す様にした。
ポリカーボネート樹脂を40容量%含み、平織炭
素繊維織で強化した平板状の厚み2mmの積層成形
品、即ち賦形材料Mを供給部Aのガイドロール1
を経由して予備賦形部B内に導入した。導入され
た賦形材料MはT−1及びT−2が各々180℃、
200℃に温度調節された予備賦形部Bで予熱され
る。
次いで第2図及び第4,5図に示すような形で
ガイドレール3、平板4を通過する間に予備賦形
がなされた。なお賦形材料の移動のためのロール
駆動用タイマーは1秒に設定された。
予備賦形された賦形材料はT−3〜T−6が
180℃に加熱された加熱圧縮賦形部C1に送られ、
圧縮賦形タイマー30秒、賦形圧力20Kg/cm2に調節
された油圧ユニツト7によつて加熱賦形された。
次いで加熱賦形後、T−7〜T−8が100℃、
T9〜T−10が50℃に温度調節された圧縮冷却部
C2へ送られ、上記ユニツト7により圧縮冷却後、
引取ロール8で引取つて第14図に示す様な異形
断面を有する賦形品を得た。
上記各部の設定条件における加熱圧縮賦形部
C1並びに圧縮冷却部C2各々での賦形材料の滞留
時間T及び加圧回数Nを次式により求めた。
滞留時間T=(a×b)/(c×d)
加圧回数N=a/(c×d)
ここでa=加熱圧縮賦形部(圧縮冷却部)長さ
b=圧縮成形タイマー設定値
c=駆動ロールの周速
d=ロール駆動時間
その結果、滞留時間、加圧回数は各々5分、10
回であつた。なお運転時予備賦形部での賦形材料
の蛇行もなく順調に予備賦形することができ、又
繊維の配列状態を軟X線により観察したが、繊維
の乱れは見られなかつた。
得られた賦形品の曲げ強度保持率、曲げ弾性率
保持率(賦形材料の曲げ強度、曲げ弾性率を100
とした時の賦形品の曲げ強度、曲げ弾性率の相対
百分率)を求めた結果、各々90%、95%であつ
た。
比較例
実施例1において第1図に示すガイドレール
3、平板4の代わりに、第15図に示す賦形ロー
ル91〜95を配列し、該予備賦形ロール対の間
に賦形材料を通過させて予備賦形させた以外は、
実施例1と同様にして第14図に示す賦形品を得
ようとした。
しかし予備賦形ロール対の間を通過する際、当
該賦形材料が蛇行して順調な予備賦形をすること
ができなかつた。又賦形品の繊維の配列状態を軟
X線で観察したが乱れが見られた。
賦形品の曲げ強度保持率、曲げ弾性率を求めた
所、各々85%、90%と実施例1と比較して低い値
となつた。
実施例 2
一方向炭素繊維/ポイカーボネート樹脂プリプ
レグを繊維方向が表層から0℃/90℃/0℃/90
℃/0℃/90℃/0℃/0℃/90℃/0℃/90
℃/0℃/90℃/0℃と順に積層成形した繊維含
有容量%が60%の平板を賦形材料として用いた以
外は全て実施例1と同様に処理して賦形品を得
た。曲げ強度保持率、曲げ弾性率を求めた所、
各々92%、95%であつた。
実施例 3〜6
実施例1で用いた装置において、表1に示す樹
脂及び強化繊維織布の組合せによる平板を表1に
示す条件で実施例1と同様にして賦形品を得た。
[Industrial Field of Application] The present invention relates to a method for continuously shaping a fiber-reinforced resin molded article and an apparatus suitable for carrying out the method. [Prior Art] Conventionally, as a method for continuously shaping a fiber-reinforced resin molded article having a planar shape into a irregularly shaped article having a constant cross-section, a roll-form method, which is widely adopted as a method for manufacturing steel pipes, has been used. A method similar to the mixing method is known. That is, the heated molded body is gradually bent into the desired cross-sectional shape by passing it continuously between a series of pairs of forming rolls having irregular cross-sections, and then the heated molded body is bent into the desired cross-sectional shape. This method attempts to shape the material by cooling it under pressure while passing it between a plurality of rolls having a cross section of . [Problems to be Solved by the Invention] However, in the above method, pressure cooling is performed between the rolls, so the molded body is pressurized while it is sandwiched between the pair of rolls. When separated, the molded body is in an open state, that is, there is no pressure, so
Due to the springback of the molded body, air in the material cannot be sufficiently degassed, resulting in a disadvantage that the mechanical strength of the obtained irregularly shaped article is significantly reduced. Therefore, in a patent application dated 13, 1985 (title of invention: continuous shaping method and apparatus for fiber-reinforced resin moldings), the present inventors previously proposed a fiber-reinforced resin molding having a planar shape. A method and apparatus for heating and compressing a body into an irregular shaped article having a fixed cross section, in which the molded article is moved intermittently, and upper and lower molds having an irregular cross section are provided while the molded article is stopped. We proposed a technology in which the material is heated, compressed, and then cooled under pressure (hereinafter referred to as the "previously proposed technology"). As a result of further research, the present inventors found that in the previously proposed technology, when preforming is performed, the circumference of each part of the roll differs in the width direction of the roll. The circumferential speed of the material, that is, the moving speed of each part in the width direction of the material to be shaped, is different, and this causes the material to meander, making it difficult to form it stably.Furthermore, the fiber orientation after pre-shaping is disturbed. It has been found that there is a problem in that the mechanical strength of the obtained excipient is reduced. SUMMARY OF THE INVENTION Therefore, an object of the present invention is to provide a method and apparatus for continuously forming a fiber-reinforced resin molded article, which does not cause meandering of the forming material and therefore enables stable forming. Another object of the present invention is to provide a method and apparatus for continuously forming a fiber-reinforced resin molded article, which can produce a shaped article with excellent mechanical strength without disordered fiber orientation. . [Means for Solving the Problems] In order to achieve the above object, the present inventors have made extensive studies and have completed the present invention. That is, in the continuous forming method of a fiber-reinforced resin molded article of the present invention, a fiber-reinforced resin molded article having a planar shape is intermittently preheated and pre-shaped, and then heated and compressed between upper and lower molds having irregular cross sections. In a method of forming a irregularly shaped article having a cross section of a substantially constant shape by compressing and cooling, the heights of both ends and the center of a fiber-reinforced resin molded article having the above-mentioned planar shape are determined in the pre-shaping. It is characterized by changing the difference continuously or intermittently. Further, the continuous shaping device for fiber-reinforced resin molded bodies of the present invention includes a pre-shaping section for preheating and pre-shaping the fiber-reinforced resin molded bodies, and upper and lower metal molds having irregular cross-sectional shapes for heating and compression shaping. In a continuous shaping device for a fiber-reinforced resin molded body, which is equipped with a mold and upper and lower molds having irregular cross-sectional shapes for compression cooling, a preheating heater for preheating the pre-shaping section and the fiber-reinforced resin molded body are provided. It is characterized by comprising an end holding part and a center holding part for continuously or intermittently changing the difference in height between both ends and the center part. [Structure of the Invention] The present invention will be explained in detail below. The excipient material used in the present invention is a unidirectional fiber-reinforced resin sheet (hereinafter referred to as UD
There are multi-directional fiber-reinforced resin sheets (hereinafter referred to as woven prepreg) made by impregnating a woven fabric such as plain weave, satin weave, or twill weave with the above resin (hereinafter referred to as woven fabric prepreg), and nonwoven fabric prepreg made by impregnating a nonwoven fabric such as matte.
The prepregs described above can be used alone or in combination to form a fiber-reinforced resin molded article of the present invention by laminating them so as to have a desired fiber orientation and thickness, or by heat compression molding. In particular, it is preferable to carry out hot compression molding before the continuous shaping of the present invention, since this makes it possible to remove the air present between the prepregs, thereby improving the physical properties of the resulting shaped article. Examples of the method of hot compression molding include the method shown in Japanese Patent Application No. 61-207618. That is, this is a method in which the prepreg is stacked and sent between upper and lower belts that move in small increments, and then, while being sandwiched between the belts, preheating, heating compression molding, and compression cooling are performed to continuously mold the prepreg. By combining such a method with the present invention, it is also possible to continuously laminate, mold, and shape prepregs. The fibers used in the present invention include glass fibers, carbon fibers, and aramid fibers (registered trademark "Kevlar").
etc.), inorganic fibers such as silicon carbide fibers, titanium fibers, boron fibers, metal fibers such as stainless steel, etc., but are not limited to these. On the other hand, thermoplastic resins include polystyrene,
Polyvinyl chloride, high density polyethylene, polypropylene, nylon, polycarbonate, polybutylene terephthalate, polyethylene terephthalate, polyether sulfon, polysulfon,
Examples include, but are not limited to, polyetherimide (trademark "ULTEM", etc.), polyetheretherketone, polyphenylene sulfide, and the like. It is preferable that the laminated prepregs or the shaping material integrated by heating compression molding be sent to a pre-shaping section and first preheated. The preheating temperature is generally set to be higher than the glass transition point of the thermoplastic resin. The preheated shaping material is then heated so that it does not move in the height direction, for example by pinching both ends of the material with pinch rolls or holding it in a fixed groove, and the central part of the shaping material is The height direction changes continuously or stepwise with respect to the pinch roll or fixed groove, and is arranged so that the final height is the same as the difference in height between the end and center of the target shaped product. It is gradually preformed while being brought into contact with a group of rolls such as a guide roll or nip roll, a plate body such as a flat plate or a curved plate, or a rod-shaped body such as a round bar or square bar, while being pulled in the longitudinal direction. In addition, contrary to the above, it is also possible to perform preliminary shaping by moving both ends of the shaping material in the height direction and fixing the central part of the shaping material in the height direction. Of course, it is possible to drive the pinch rolls, guide rolls, etc. The material to be preshaped as described above is then fed into upper and lower molds having irregular cross sections for heating and compression shaping, and heating and compression shaping is started. The upper and lower molds are open while the material to be shaped is moving, and as soon as the material stops, the upper and lower molds are closed to perform heating compression shaping. Therefore, the material moves by inching. By adjusting the amount of movement at one time, it becomes possible to heat and compress the same portion of the material a desired number of times. Therefore, after being heated and compressed once in the mold, it may be sent to the next pressurization and cooling process, but from the viewpoint of degassing the material, it is necessary to apply the same portion multiple times. It is preferable to heat and compress. Note that the movement of the shaped material is performed, for example, by a roll provided in the pre-shaped section and/or a take-up roll provided at the outlet of the pressurized cooling mold.
The inching is achieved by, for example, controlling the driving time and stopping time of the roll with a timer as described later. The heating temperature is higher than the glass transition point, preferably the softening point, of the thermoplastic resin, and from the viewpoint of defoaming, a higher temperature is generally preferable, but it is determined experimentally for each resin in consideration of releasability from the mold. It should be. It is particularly preferable to treat the mold with a mold release agent before or during operation in order to improve the releasability of the excipient material from the upper and lower molds. As for the pressing force, high pressure is desirable from the viewpoint of defoaming, but it is necessary to take into account the disturbance of fiber orientation due to the flow of the softened resin. Therefore, it is desirable to determine the pressure experimentally based on the fiber content in the excipient material, but generally the higher the fiber content, the higher the pressure can be set. The shaped material that has been heated and compressed is sent to a compression cooling mold and compressed and cooled once or multiple times, so that a fiber-reinforced resin molded article can actually be obtained continuously. The cooling temperature is preferably set below the glass transition point of the thermoplastic resin. This is because demolding at a temperature exceeding the glass transition point generally causes problems such as warping of the excipient and bubbles remaining on the surface of the excipient.
Further, the pressurizing force may be set independently from the pressurizing force at the time of heating and pressurizing shaping, but it is usually set to the same pressure. Incidentally, it is particularly effective to provide a knockout pin or the like in the heating compression shaping mold and the compression cooling mold, for example, to prevent the molded product from coming out of the mold. The knockout pin is housed in the mold when pressurized, and functions by protruding from the mold surface as soon as the mold opens, so the movement of the pin is the same as the movement of the mold. It should be linked with
Such movement of the pin can be achieved, for example, by springs, air pressure, etc., but in particular when using air pressure,
For example, this is possible by linking the operation of an air cylinder with the opening and closing of a mold. Next, details of the present invention will be explained based on typical embodiments shown in the accompanying drawings. FIG. 1 is a schematic side view showing one embodiment of the present invention, and as shown in the figure, a continuous shaping apparatus for carrying out the present invention has a guide roll 1 for supplying a shaping material M. Part A, a guide roll 2 for transferring the shaped material, a guide rail 3 having a U-shaped groove for holding both ends of the shaped material and moving the both ends in the height direction, and a guide rail 3 for transferring the shaped material; A preforming part B having a flat plate 4 for holding the height of the center portion so that it does not change with the movement of both ends, and a far infrared heater (not shown) for preheating, and a heating compression molding mold. 5, a compression shaping section C having a compression cooling mold 6, and a hydraulic unit 7, and a taking-off section D having taking-off rolls 8 for taking off the molded product after shaping. The shaped material M is sent to the preliminary shaping section B via between the guide rolls 1 of the supply section A. When entering the pre-shaping section B, the shaping material M heated above the glass transition point of the thermoplastic resin, preferably above the softening point, is heated to a temperature above the softening point of the thermoplastic resin.
It is preformed into a desired shape while passing through a guide rail 3 and a flat plate 4 having a U-shaped groove as shown in the figure. Further, in the present invention, the material may be preformed into a desired shape when passing between the pinch rolls 21 and nip rolls 22 and 23 shown in FIGS. 6 to 8. In addition, a preliminary shaping mold 62 shown in FIGS. 9 to 11
The material may be pre-shaped into a desired shape while being passed between a roll 61 for pressing both ends of the material and a roll 63 for pressing the center of the material. The preforming mold 62 may be heated to a temperature above the glass transition point, preferably the softening point, of the thermoplastic resin using a sheathed heater or the like, or it may be provided in a heating compression mold. In addition, by arranging the roll 61 so that its central axis takes a certain angle θ with respect to the drawing direction of the shaped material as shown in the figure, tension is generated in the width direction of the shaped material.
Preferable from the viewpoint of preventing wrinkles. Of course, the angle θ may be 0 degrees. In the above embodiment, it is preferable that the spacing between each pair of rolls and the spacing between the preforming mold and the rolls can be adjusted in accordance with the thickness of the shaping material. It is also possible to pre-shape the shaping material under pressure, for example by using an air cylinder or the like. The above-mentioned pressing force is sufficient as long as it is a pressure sufficient to pre-shape the shaping material, and should be determined experimentally. The material thus preformed is then sent to the heating compression mold 5 of the compression shaping section C and compressed and shaped by the hydraulic unit 7. The heating temperature of the mold is preferably maintained at a temperature equal to or higher than the glass transition point of the thermoplastic resin using a heater, steam, or the like. On the other hand, the heated and compressed portion is then sent to a compression cooling mold 6, where it is compressed and cooled by a hydraulic unit 7 to below the glass transition point of the thermoplastic resin. As a cooling method, a method using a refrigerant such as air cooling, water cooling, or steam cooling is adopted. Although the hydraulic unit 7 is designed to be used in combination with hot press molding, it is of course possible to provide separate hydraulic units for hot press molding and compression cooling, and set the pressurizing force independently. Pressure force is 0.1~500
Kg/cm 2 is preferred. In the present invention, the shaping material is transferred by the guide roll 1 in the supply section A, the guide roll 2 in the preforming section, the pinch roll 21 (if provided), the nip rolls 22 and 23 (if provided), and the guide roller 2 in the take-up section D. This is carried out by moving one of the take-up rolls 8 or a group of rolls in combination. Therefore, the shaping material is moved by an inch. That is, in the compression shaping section C, the driving of the heating compression shaping mold 5 and the compression cooling mold 6 is stopped immediately before they are closed, shaping is continued for a certain period of time, and the driving is restarted as soon as both molds are opened. By repeating this operation, the excipient material is actually moved continuously. The above-mentioned inching drive can be controlled by, for example, two timers, one for driving the roll and one for compression shaping. That is, the excipient material is moved for a certain period of time by a roll drive timer,
At the same time as the timer expires, the compression and shaping timer is activated, and the compression and shaping is performed for a certain period of time, and then the timer expires. At the same time, the roll drive timer is activated again and the movement of the shaping material is resumed. Note that the above method is an example, and the method is not limited to this, and automatic control can also be performed using a microcomputer. Among the rolls used in the present invention, portions that come into contact with the shaping material, such as the guide roll 2, pinch roll 21, and nip rolls 22 and 23 existing in the preforming section B,
It is preferable that the surfaces of the heating compression molding mold 5 and the compression cooling mold 6 of the compression molding section C take into consideration mold releasability from the resin. Therefore, it is desirable that these surfaces be mirror-finished or subjected to an appropriate mold release treatment. Specifically, the roll surface is treated with Teflon, or imide resin (“UPiLEX” manufactured by Ube Industries, Ltd.) is used.
UBE U varnish, etc.), etc.), but when selecting it, it is necessary to consider the imprinting temperature. A suitable mold release agent may also be used, such as FREKOTE (USA).
FREKOTE) etc. can be applied before or during operation. In this embodiment, it is preferable that the heating compression molding mold 5 and the compression cooling mold 6 be provided with knockout pins as shown in FIG. Providing this is preferable because it facilitates the removal of the shaping material from the mold. The knockout pin is housed in the mold when the mold is closed, but functions to protrude from the mold as soon as the mold is opened, and to release the excipient material from the mold. . In the figure, for example, when a knock-out pin is provided in the lower mold, when the mold is opened, the push rod 32 is moved via the push plate 31 by an air cylinder (not shown), and thereby The knockout pin 33 rises to remove the shaping material from the mold.
On the other hand, at the same time as the mold is closed, the air cylinder retreats, and the push rod 32, knockout pin 33, and push plate 31 function by returning to their original positions due to the downward force exerted by the spring 34 and the shaping material. In addition, when the knockout pin is provided in the upper mold,
When the mold is closed, the knockout pin 35 is pushed up by the pushing force of the molding material, but as soon as the mold is opened, the molding material is pushed down by the force of the spring 36 and removed from the mold. It is something that makes you Note that the above method is an example, and the method is not limited thereto. Further, it is preferable to round the end of the heating compression molding mold 5 on the side of the preforming section B (to form an R) to facilitate the movement of the molding material. The heating compression molding mold 5 and the compression cooling mold 6 may each be configured as a separate pair of molds. In this case, it is preferable that the heating compression shaping mold 5 and the compression cooling mold 6 are placed adjacent to each other so that the temperature of the heated compression molded part does not decrease before the part is transferred to the compression cooling mold 6. Further, as shown in FIG. 13, it is also possible to provide both heating and cooling functions by dividing the inside of the pair of upper and lower molds into a plurality of temperature zones and controlling the temperature. In the figure, T-1 to T-10 are symbols representing temperature divisions. For example, the preforming part B is T-1
~Divided into T-2, T-1 at 200℃ and T-2 at 210℃
After preforming, the heating compression shaping section C 1 is divided into T-3 to T-6 and the temperature of each is adjusted to 200°C, and then the compression cooling section C 2 is divided into T-3 to T-6. It is also possible to divide it into T-7 to T-10 and adjust the temperature of each to 100°C. In the present invention, the same portion of the excipient material can be compression molded multiple times, and the number of times is determined by adjusting the excipient material movement time, that is, the excipient material movement timer. That is, the length of the heating compression shaping mold is l (cm), and the moving speed of the shaping material is S.
(cm/sec) and the moving time of the shaping material is T (sec), the number of molding times N is expressed as l/(S·T).
Further, the time for one compression molding is determined by adjusting the compression molding timer. Note that the number of times and time of heating compression molding may be different from the number and time of compression cooling, and in this case, means such as changing the lengths of the heating compression molding mold 5 and the compression cooling mold 6 may be used. . As mentioned above, by moving the shaping material by inching, the shaping material is actually continuously preheated, preshaped, heated and compressed, and compressed and cooled to continuously form a cross section of a constant shape. It can be shaped into a differently shaped article having the following characteristics. It goes without saying that by changing the position and shape of the rolls used in the pre-shaping section and the cross-sectional shape of the heating compression shaping mold and compression cooling mold, it is possible to shape irregular cross sections such as angles and channels. be. [Example] Hereinafter, the present invention will be explained with reference to Examples. Example 1 The specifications and conditions of each part of the apparatus shown in FIG. 1 were as follows. Driving rolls: Guide roll 2 in the preforming section, take-up roll 8 in the take-up section Circumferential speed of drive roll: 5 cm/sec Pre-forming section heating method: Temperature-controlled heating in two sections as shown in Figure 13 using a far-infrared heater Compression molding mold, compression cooling mold: A pair of upper and lower molds with a length of 100 cm are each divided into four parts and the temperature is adjusted to form a heating compression molding part and a compression cooling part in the same mold. . The heating method used was a sheathed heater. The temperature divisions of the preheating section, heating compression shaping section, and compression cooling section were as shown in FIG. 13. A flat plate-like 2 mm thick laminate molded product containing 40% by volume of polycarbonate resin and reinforced with plain-woven carbon fiber weave, that is, excipient material M, is placed on the guide roll 1 of supply section A.
It was introduced into the preforming section B via the. The introduced shaping material M has T-1 and T-2 of 180°C, respectively.
It is preheated in preforming section B whose temperature is controlled to 200°C. Next, preliminary shaping was performed while passing through the guide rail 3 and flat plate 4 in the form shown in FIGS. 2 and 4 and 5. Note that the roll drive timer for moving the shaping material was set to 1 second. The pre-shaped material is T-3 to T-6.
It is sent to heating compression shaping section C1 heated to 180℃,
Heat shaping was carried out by the hydraulic unit 7, which was adjusted to a compression shaping timer of 30 seconds and a shaping pressure of 20 kg/cm 2 . Then, after heat shaping, T-7 to T-8 were heated to 100°C.
Compression cooling section where T9 to T-10 are temperature controlled to 50℃
After being compressed and cooled by the unit 7 ,
The product was taken up with a take-up roll 8 to obtain a shaped article having an irregularly shaped cross section as shown in FIG. Heat compression forming section under the setting conditions of each section above
The residence time T and the number of pressurization times N of the shaping material in each of C 1 and compression cooling section C 2 were determined using the following equations. Residence time T = (a x b) / (c x d) Number of times of pressurization N = a / (c x d) where a = length of heating compression shaping section (compression cooling section) b = compression molding timer setting value c = Circumferential speed of the drive roll d = Roll drive time As a result, the residence time and number of pressurizations are 5 minutes and 10 minutes, respectively.
It was hot. During operation, the preforming material could be smoothly preformed without meandering in the preforming section, and when the arrangement of the fibers was observed using soft X-rays, no disorder of the fibers was observed. The flexural strength retention rate and flexural modulus retention rate of the obtained excipients (the flexural strength and flexural modulus of the excipient material are 100
The relative percentages of bending strength and bending elastic modulus of the excipient were found to be 90% and 95%, respectively. Comparative Example In Example 1, instead of the guide rail 3 and flat plate 4 shown in FIG. 1, shaping rolls 91 to 95 shown in FIG. 15 were arranged, and the shaping material was passed between the pair of preliminary shaping rolls. Except for preforming by letting
An attempt was made to obtain the shaped product shown in FIG. 14 in the same manner as in Example 1. However, when passing between the pair of preforming rolls, the material to be shaped meandered and could not be preformed smoothly. Furthermore, when the arrangement of fibers in the excipient was observed using soft X-rays, disorder was observed. When the bending strength retention rate and bending elastic modulus of the excipient were determined, they were 85% and 90%, respectively, which were lower values compared to Example 1. Example 2 Unidirectional carbon fiber/polycarbonate resin prepreg with the fiber direction from the surface layer at 0°C/90°C/0°C/90
℃/0℃/90℃/0℃/0℃/90℃/0℃/90
A shaped product was obtained in the same manner as in Example 1, except that a flat plate having a fiber content of 60% by volume, which was laminated in the order of 0°C/0°C/90°C/0°C, was used as the shaping material. When bending strength retention rate and bending elastic modulus were determined,
The percentages were 92% and 95%, respectively. Examples 3 to 6 Using the apparatus used in Example 1, flat plates made of the combinations of the resins and reinforcing fiber woven fabrics shown in Table 1 were obtained in the same manner as in Example 1 under the conditions shown in Table 1.
【表】
表1に示す様に実施例1〜3は加圧回数の賦形
品物性に及ぼす影響を示すものであるが、加圧回
数の多い方が曲げ強度保持率、曲げ弾性率保存率
とも高い結果を得た。
又、実施例5及び6は他の熱可塑性樹脂及び繊
維織布の組合せによる賦形を行つたものである
が、何れも良好な結果を得た。
[発明の効果]
本発明によれば、予備賦形する際、賦形材料の
蛇行の問題が解消されるため、安定した賦形が可
能となるばかりか、得られる賦形品中の繊維配列
の乱れが少なく、従つて機械強度の優れた賦形品
を提供し得るという効果を発揮する。[Table] As shown in Table 1, Examples 1 to 3 show the influence of the number of times of pressurization on the physical properties of excipients. Both obtained high results. Further, in Examples 5 and 6, shaping was performed using a combination of other thermoplastic resins and fibrous fabrics, and good results were obtained in both cases. [Effects of the Invention] According to the present invention, the problem of meandering of the material to be shaped is solved when preforming, so not only stable shaping is possible, but also the fiber arrangement in the obtained shaped product is improved. This has the effect of providing a shaped product with less disturbance in the structure and excellent mechanical strength.
第1図は本発明に用いられる装置の一実施態様
を示す概略側面図、第2図は同上の予備賦形部の
概略側面図、第3図は同上の実施態様に用いられ
る下加熱圧縮賦形金型を示す断面図、第4図は第
1図に示す装置の予熱賦形部のうちガイドレー
ル、平板の概略平面図、第5図は同上の−線
断面図、第6図は予備賦形部の他の実施態様を示
す概略側面図、第7図は同上の−線断面図、
第8図は同上の−線断面図、第9図は予備賦
形部の他の実施態様を示す概略側面図、第10図
は同上の概略平面図、第11図は同上の概略正面
図、第12図は加熱圧縮賦形部、圧縮冷却金型及
びノツクアウトピンの一例を示す断面図、第13
図は予備賦形部、加熱圧縮賦形部及び圧縮冷却部
を複数個の温度区分に分けた状態を示す概略側面
図、第14図は本発明で得られる賦形品の一例を
示す断面図、第15図は先提案技術において予備
賦形部分の一実施態様を示す概略側面図である。
Fig. 1 is a schematic side view showing one embodiment of the apparatus used in the present invention, Fig. 2 is a schematic side view of the preforming section of the same, and Fig. 3 is a bottom heating compression forming device used in the above embodiment. FIG. 4 is a schematic plan view of the guide rail and flat plate of the preheating and forming part of the apparatus shown in FIG. 1, FIG. A schematic side view showing another embodiment of the shaping part, FIG. 7 is a sectional view taken along the line -
FIG. 8 is a cross-sectional view taken along the line ``--'', FIG. 9 is a schematic side view showing another embodiment of the preforming section, FIG. 10 is a schematic plan view of the same, and FIG. 11 is a schematic front view of the same; FIG. 12 is a cross-sectional view showing an example of a heating compression forming part, a compression cooling mold, and a knockout pin;
The figure is a schematic side view showing the pre-shaping section, heating compression shaping section, and compression cooling section divided into a plurality of temperature zones, and FIG. 14 is a cross-sectional view showing an example of a shaped product obtained by the present invention. , FIG. 15 is a schematic side view showing an embodiment of the preforming part in the previously proposed technique.
Claims (1)
的に予熱・予備賦形し、次いで異形断面を有する
上下金型間で加熱圧縮賦形、圧縮冷却せしめるこ
とにより実質的に一定形状の断面を有する異形成
形品に賦形する方法において、当該予備賦形にお
いて上記平面形状を有する繊維補強樹脂成形体の
両端と中央部の高さの差を連続的、又は断続的に
変化せしめることを特徴とする繊維補強樹脂成形
体の連続賦形方法。 2 維維補強樹脂成形体を予熱、予備賦形するた
めの予備賦形部と、加熱圧縮賦形のための異形断
面形状を有する上下金型及び圧縮冷却のための異
形断面形状を有する上下金型とを具備する維維補
強樹脂成形体の連続賦形装置において、当該予備
賦形部が予熱する為の予熱ヒーターと当該繊維補
強樹脂成形体の両端と中央部の高さの差を連続
的、又は断続的に変化させるための端部保持部及
び中央保持部とを具備することを特徴とする繊維
補強樹脂成形体の連続賦形装置。[Claims] 1. A fiber-reinforced resin molded article having a planar shape is intermittently preheated and preformed, and then heated and compressed between upper and lower molds having irregular cross sections, and compressed and cooled. In a method of shaping into a irregularly shaped article having a cross section of a constant shape, the difference in height between both ends and the center of the fiber-reinforced resin molded article having the above-mentioned planar shape is continuously or intermittently changed during the pre-shaping. A continuous shaping method for a fiber-reinforced resin molded article. 2. A preforming section for preheating and preshaping a fiber-reinforced resin molded body, upper and lower molds having irregular cross-sectional shapes for heating compression shaping, and upper and lower molds having irregular cross-sectional shapes for compression cooling. In a continuous forming device for a fiber-reinforced resin molded article, the pre-forming section is equipped with a preheating heater for preheating the fiber-reinforced resin molded object, and the difference in height between both ends and the center of the fiber-reinforced resin molded object is continuously measured. , or a continuous shaping device for a fiber-reinforced resin molded article, characterized in that it comprises an end holding part and a central holding part for changing the shape intermittently.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63117549A JPH01286823A (en) | 1988-05-14 | 1988-05-14 | Continuous shaping method of fiber-reinforced resin molded body and its device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63117549A JPH01286823A (en) | 1988-05-14 | 1988-05-14 | Continuous shaping method of fiber-reinforced resin molded body and its device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01286823A JPH01286823A (en) | 1989-11-17 |
| JPH0369701B2 true JPH0369701B2 (en) | 1991-11-05 |
Family
ID=14714560
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63117549A Granted JPH01286823A (en) | 1988-05-14 | 1988-05-14 | Continuous shaping method of fiber-reinforced resin molded body and its device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01286823A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPWO2016002470A1 (en) * | 2014-07-01 | 2017-04-27 | 帝人株式会社 | Manufacturing method of fiber reinforced plastic |
| WO2021140561A1 (en) * | 2020-01-07 | 2021-07-15 | 三菱重工業株式会社 | Shaping method and shaping device |
| DE102021102764A1 (en) | 2020-02-19 | 2021-08-19 | Daido Kogyo Co., Ltd. | PROFILE ROLLING DEVICE AND METHOD FOR MANUFACTURING A FIBER REINFORCED PLASTIC ROLLED PROFILE PART |
-
1988
- 1988-05-14 JP JP63117549A patent/JPH01286823A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01286823A (en) | 1989-11-17 |
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