JPH0137503B2 - - Google Patents
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- JPH0137503B2 JPH0137503B2 JP54086900A JP8690079A JPH0137503B2 JP H0137503 B2 JPH0137503 B2 JP H0137503B2 JP 54086900 A JP54086900 A JP 54086900A JP 8690079 A JP8690079 A JP 8690079A JP H0137503 B2 JPH0137503 B2 JP H0137503B2
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Description
本発明は、ガラス繊維で補強された熱可塑性合
成樹脂複合シートに関し、詳しくは熱可塑性合成
樹脂の粉体を分散付着させた開繊されたガラス不
連続繊維の綿状体から形成されたマツトを熱可塑
性合成樹脂の融(軟化)点以上の温度に加熱しな
がら、あるいは加熱した後、マツト中の気体が存
在しなくなるか、少なくとも連続気孔として存在
しなくなるまで加圧することからなるガラス繊維
で補強された熱可塑性合成樹脂複合シートの製法
に関する。
本明細書において使用される用語「開繊」と
は、ガラス単繊維が数十本乃至数百本集束結合さ
れた繊維束すなわちストランドあるいは、このス
トランドによりをかけて所定本数を合撚したヤー
ンなどに外力をかけて解きほごす操作をいう。さ
らに、用語「開繊されたガラス繊維」には、スト
ランドやヤーンを製造中に中間製品として製造さ
れるガラス単繊維群(フイラメント)も包含され
る。
従来、ガラス繊維強化熱可塑性合成樹脂複合シ
ートの製法には、下記のような方法がある。
(イ) 切断したガラス繊維を熱可塑性合成樹脂と混
練し、押出機などを用いるシートに成形する方
法。
(ロ) 比較的ガラス繊維の織密度の低い織布(例え
ば、目抜平織クロス)などに、その開口部を通
して溶融した2枚の熱可塑性合成樹脂シートを
貼り合わせる方法。
(ハ) ガラス繊維の不織布(例えば、チヨツプドス
トランドマツトやコンテイニユアスストランド
マツトなど)に溶融した熱可塑性合成樹脂を含
浸させる方法。
しかしながら、上記の従来技術にはそれぞれ次
のような欠点がある。(イ)法は混練及びシート成形
工程でガラス繊維の破壊が起り、高強度の製品が
得られ難い。例えば、6mmの長さのガラス繊維
(チヨツプドストランド)をバンバリーミキサー
で熱可塑性合成樹脂と混練し、押出機で成形した
シートは、ガラス繊維の長さがほとんど2mm以下
に切断され、しかもこのような方法によるとガラ
ス繊維がほとんどシートの経方向に配向されるた
め、経緯強度の不釣合が生ずる。(ロ)法には(イ)法の
ような欠点はないが、ガラス繊維が密な織布では
熱可塑性合成樹脂の含浸が困難になるので、熱可
塑性合成樹脂には低溶融粘度のもの、ガラス繊維
には製織密度の粗なものの使用が必要になる。こ
のようなクロスは高価になるばかりでなく、熱可
塑性合成樹脂に対するガラス繊維の使用量が低く
おさえられるので強度の大きいシートが得られ難
くなる。(ハ)法では、熱可塑性合成樹脂の含浸をよ
くするために、ガラス繊維集束数の少ないストラ
ンドやチヨツプドストランドが一般に使用され、
含浸工程は(ロ)の方法より容易であるがまだ充分と
はいえず、厚手のマツトに含浸させることは至難
で、例えば2mm以上の厚手のシートを製造するた
めには、薄手のマツトに含浸させたシートを幾層
も積層することが必要になる。さらに、(ロ)、(ハ)両
法には表面の平滑なシートが得られ難いという共
通の欠点があるが、これは両法共にストランドや
ロービングというかなりの径のある繊維束を使用
するために溶融含浸された樹脂が固化する際に収
縮し、いわゆるヒケという現象が発生するためで
ある。
本発明者らは、従来技術に付帯する上記の欠点
を総合的に解消したガラス繊維補強熱可塑性合成
樹脂シートの製造方法を鋭意研究の結果本発明に
到達した。すなわち本発明は、粒径が1mm以下の
熱可塑性合成樹脂の粉体100重量部を、繊維長2
〜50mmの範囲の不連続なガラス繊維5〜300重量
部と開繊しながら混合撹拌するか、もしくは開繊
された該繊維と混合撹拌し、均一に分散せしめて
なる綿状体マツトを、該熱可塑性合成樹脂の融点
又は軟化点以上の温度に加熱しながら、あるいは
加熱後に、マツト中の気体(空気)が存在しなく
なるか、少なくとも連続気孔として存在しなくな
るまで加圧することを特徴とする平滑なガラス繊
維補強熱可塑性合成樹脂シートの製法である。
本発明の方法で得られるガラス繊維補強熱可塑
性合成樹脂シートには次のような特徴がある。
(1) 得られるシートは、開繊されたガラスの不連
続繊維が製造工程中に破壊されることなく均一
に分散されるので、表面は平滑で、経緯の強合
に不釣合がなく、しかも衝撃強度、引張強度な
どの機械的強度が優れている。
(2) ガラス繊維に対する合成樹脂の分散付着量を
広範囲に変動させることができるので、得られ
るシートのガラス繊維含有量も大巾に変更でき
る。例えば、合成樹脂100重量部に対してガラ
ス繊維を300重量部を混入させることも可能で、
従つて優れた強度を有するシートが容易に得ら
れる。
(3) 熱可塑性合成樹脂は粉体であることが条件
で、そのほかに特に限定がないので、樹脂の適
応範囲が広い。
(4) ガラス繊維として、市販の比較的安価なロー
ビング、ストランド及びあらかじめこれを切断
したチヨツプドストランドを使用できるので、
経済的に有利である。
(5) ガラスの不連続繊維と熱可塑性合成樹脂との
組合せであるので、成形された複合シートをさ
らにプレス成形(スタンピング成形)によつて
任意の形状に賦形することができる。
(6) 厚さ1mm以下の薄手のシートから、4mm以上
の厚手のシートまで、任意に、容易に製造でき
る。
以下、本発明の構成を詳細に記載する。
本発明に使用するガラス繊維には市販の製品が
用いられる。中でも、ガラスの単繊維(フイラメ
ント)を数十本乃至数百本引きそろえ、ポリ酢酸
ビニル、ポリエステル、エポキシ樹脂などの糊剤
で集束したストランド及びこれをさらに数本乃至
数十本引きそろえて巻取つたロービングが最も好
ましく、これらは所定の長さに切断して使用す
る。このほか、ストランドを各種の長さに切断し
た市販のチヨツプドストランドを利用するのも便
利である。その他ストランドによりをかけて所定
の本数を合撚したヤーンも使用できるが、開繊の
容易さの点からは前者の方が好ましい。
本発明の製品は、表面が平滑で均質の強度の大
きいシートを目的とするので、使用する集束され
たストランドはできるだけ解きほぐして綿状にす
るため、開繊する必要がある。従つて、ストラン
ドには集束剤の使用量の少ない、いわゆるソフト
タイプのストランドを使用するのが好ましく、ス
トランドが強固に集束されている場合には、あら
かじめ溶剤で集束剤を除去するのが良い。一方、
本発明には、一般には市販されていないストラン
ドなどの製造時に中間製品として得られるフイラ
メントを切断して使用することも可能である。こ
れらの使用にあたつては熱可塑性合成樹脂との結
合力を高めるために、あらかじめシラン系やボラ
ン系のカツプリング剤で表面処理するのが好まし
い。
本発明に使用するガラス繊維は比較的長めに切
断されたものを使用するが、その長さは少なくと
も2mm以上が必要で、好ましくは3mm以上であ
る。長さ2mm未満のガラス繊維を使用すると、そ
れを熱可塑性合成樹脂と混練して押出機で成形し
て得られる従来のシートと同程度の強度のものし
か得られなく好ましくない。一方、長さの上限に
ついては特に明確な限定はないが、ガラス繊維の
長さを50mmを超えるものにしても特に強度が増大
するものでもなく、例えばこの長さが100mm以上
にもなると、逆に開繊及び合成樹脂粉体の分散操
作が困難になるので好ましくない。
本発明に使用される熱可塑性合成樹脂には特に
限定はなく、ポリオレフイン系樹脂、ポリスチレ
ン系樹脂、ポリ塩化ビニル系樹脂、ポリアクリル
酸系樹脂、ポリアミド系樹脂、ポリエステル系樹
脂、ポリカーボネート系樹脂などが使用される。
ガラス繊維との結合力を更に高めるために、これ
ら樹脂を化学的に変成して使用することもでき
る。本発明の方法で得られるシートの付加価値を
高めるため、例えば難撚性を付与するには樹脂に
難燃化処理を施し、耐熱性を付与するには熱架橋
性の樹脂粉末をガラス繊維に分散付着させ成形時
に架橋させるなどの処理を施すことも可能であ
る。
本発明では、熱可塑性合成樹脂には必ず粉末を
使用するが、その粒径は1mm以下、好ましくは
0.5mm以下である。粒径が1mm以上を超えると、
合成樹脂はその自重で沈降し、ガラス繊維の綿状
体中に均一に分散されない。この合成樹脂粉体に
は、一般のペレツト状、ビーズ状製品あるいは成
形品の廃棄物などを機械粉砕して使用してもよい
が、合成樹脂の製造工程中で得られる粉末を使用
するのが経済性から考えて最も有利である。
本発明の方法に使用されるガラス繊維量は熱可
塑性合成樹脂100重量部に対し、5〜300重量部、
好ましくは10〜200重量部である。この量が5重
量部未満ではガラス繊維による補強効果がほとん
ど認められず、300重量部を超えるとガラス繊維
が合成樹脂によつて完全に包まれたシートが得ら
れない。
次に、本発明のガラス繊維で補強された熱可塑
性合成樹脂複合シートの製法の実施態様を記載す
る。本発明の方法は、ガラスの連続繊維を切断、
開繊した後、熱可塑性合成樹脂粉体を付着させ、
あるいは切断したガラス繊維を開繊しながら熱可
塑性合成樹脂粉体と混合撹拌して熱可塑性合成樹
脂粉体を分散付着させた綿状体を、ほぼ均一な厚
みのマツト状に整形した後、熱可塑性合成樹脂の
融(軟化)点以上の温度に加熱し、少なくとも空
気の連続気孔が存在しなくなるまで加圧し、冷却
する方法である。ガラス繊維、例えばチヨツプド
ストランドをあらかじめ開繊したもの、あるいは
切断したストランドヤーンを開繊したものなどを
2軸のリボンブレンダーのような混合機に装入
し、これに熱可塑性合成樹脂粉体を添加して撹拌
しながら混合付着させるか、またはチヨツプドス
トランドと合成樹脂粉末を同時に混合撹拌して、
チヨツプドストランドが開繊される過程で合成樹
脂粉体が徐々に混合付着させる方法で、熱可塑性
合成樹脂粉体を綿状体に分散付着させる。このよ
うに、ガラス繊維の綿状体に熱可塑性合成樹脂粉
体が均一に分散付着される機構は、ガラス繊維綿
状体の繊維の絡み合いの中に合成樹脂粉体が包み
込まれる効果のほかに、混合中に摩擦によつて発
生した静電気的な力が作用しているとも推定され
る。従つて、本発明に帯電防止剤処理を施したガ
ラス繊維の使用は避けるべきである。
次に、得られたガラス綿状体に熱可塑性合成樹
脂粉体が分散付着されたマツトを合成樹脂の融
(軟化)点以上の温度に加熱しながら、あるいは
加熱後に加圧する。この際の加圧の程度はできる
だけ高いのが好ましく、実際的にはマツト中に存
在している気体(空気)が完全に追い出されてマ
ツト中に存在しなくなるか、少なくとも連続気孔
として存在しなくなるまで、すなわち通気性がな
くなるまで溶融加圧する。シート中に残存する空
隙(独立気孔)はシートの物性、すなわち機械的
強度を劣化させるので、溶融加圧はできるだけ高
温、高圧で行なうのが好ましい。
上述した、合成樹脂粉体を分散、付着させたガ
ラス繊維の綿状体をマツト状に成形して加熱、加
圧してシートとする方法は、回分法、連続法いず
れによつても実施できる。回分法で行なう場合
は、所定の寸法の金型に合成樹脂粉体を分散、付
着させたガラス繊維の綿状体を充てんし、外部か
ら加熱、加圧した後冷却して取り出す方法が採用
される。連続法で行なう場合は、例えばベルトコ
ンベヤーの上にガラス繊維の綿状体を連続して供
給してマツト状にし、外部から加熱しながら上部
に設置した無端ベルトで暫時圧縮したり、あるい
は数本の加熱ロールを通して圧縮してシートに成
形した後、冷却ロールで冷却して引き取る方法な
どが採用される。
以上詳述したように、本発明の方法によつて得
られるガラス繊維で補強された熱可塑性合成樹脂
の複合シートは、表面が平滑で均質の機械的強度
の大きいシートであるので、板材として広範囲の
用途に利用されるほか、ガラスの不連続繊維が均
一に分散されているので、マツトドメタルダイな
どを用いてさらに熱成形して種々の形状の製品に
賦形する原材料、すなわちスタンパブルシートに
供することもできる。
以下、実施例を挙げて本発明を具体的に説明す
る。
実施例 1
熱可塑性合成樹脂にポリプロピレン(商品名:
「三井ノーブレンJHH(G)」・三井東圧化学社製)
の粉体(粒径20メツシユ以下)100重量部とガラ
ス繊維に長さ6mmのチヨツプドストランド(商品
名「CS6PE−612」・日東紡積社製)20重量部を
使用し、両者をビーカーの中に入れて2本の撹拌
棒でチヨツプドストランドに摩擦力を与えながら
撹拌混合したところ、チヨツプドストランドは
徐々に開繊されて綿状体となり、これにポリプロ
ピレン粉体がほぼ均一に分散付着された混合物が
得られた。
次に、長辺250mm、短辺150mm、深さ3.5mmの金
枠に前記混合物135gをほぼ同じ厚みのマツト状
に積み上げ、その上下を2枚のおさえ鉄板でふた
をした。それを100トンの油圧プレスに装入し、
220℃で5分間予熱した後、220℃で5分間100
Kg/cm2Gの圧力で加圧し、次いでこれを別の油圧
プレスに移して100Kg/cm2Gの圧力で5分間35℃
で冷却した。得られたシートは、開繊された長さ
6mmのガラス繊維がほぼ均一に分散されたポリプ
ロピレンシート(厚さ3.5×長さ250×幅150mm)
であつた。このシートについて測定した引張強度
とアイゾツト衝撃強度の結果を第1表に示す。
比較例 1
実施例1と同一のガラス繊維とポリプロピレン
を実施例1と同一比率でブラベンダープラストグ
ラフミキサーに装入し、180℃で5分間混練した。
得られた混練物を実施例1と同じ方法でプレス成
形したところ、混練中にほとんど0.2〜1mmの長
さに切断されたガラス繊維が均一に分散されたポ
リプロピレンシートが得られた。このシートの引
張強度とアイゾツト衝撃強度を第1表に示した
が、いずれも実施例1よりも著しく劣る値であつ
た。
実施例 2
実施例1で使用したのと同一のポリプロピレン
粉体100重量部とチヨツプドストランド67重量部
を、実施例1と同一の方法で撹拌混合し、その
160gを用いて実施例1と同様にしてシートを作
成した。得られたシートは開繊された長さ6mmの
ガラス繊維がほぼ均一に分散されたポリプロピレ
ンシートであつた。この引張強度とアイゾツト衝
撃強度を第1表に示したが、その値は実施例1を
幾分上回わる値であつた。
実施例 3
実施例1で使用したのと同一のポリプロピレン
100重量部とガラス繊維に長さ25mmのチヨツプド
ストランド(商品名:「CS−25Z−700」・日東紡
績社製)の集束剤をアセトンで除去したストラン
ド67重量部を使用して、実施例1と同様にして撹
拌混合し、その160gを用いて実施例1と同様の
方法でシートを作成した。得られたシートは開繊
された長さ25mmのガラス繊維がほぼ均一に分散さ
れたポリプロピレンシートであつた。この引張強
度とアイゾツト衝撃強度を第1表に示したが、い
ずれも最高値を示した。
実施例 4
熱可塑性合成樹脂に高密度ポリエチレン(商品
名:「スタフレンE−891」・日本石油化学社製)
の粉体(粒径20メツシユ以下)100重量部と実施
例1で使用したのと同一のチヨツプドストランド
100重量部を使用し、実施例1と同様の方法で撹
拌混合し、その180gを用いて実施例1と同様の
方法でシートを作成した。得られたシートは開繊
された長さ6mmのガラス繊維がほぼ均一に分散さ
れたポリエチレンシートであつた。この引張強度
とアイゾツト衝撃強度を第1表に示した。
実施例 5
熱可塑性合成樹脂にポリスチレンの成形品を機
械粉砕し20メツシユの篩を通した粉体100重量部
と実施例1で使用したのと同一のチヨツプドスト
ランド300重量部を使用して実施例1と同様にし
て撹拌混合し、その240gを用いて実施例1と同
様の方法でシートを作成した。得られたシートは
開繊された長さ6mmのガラス繊維がほぼ均一に分
散されたポリスチレンシートであつた。
The present invention relates to a thermoplastic synthetic resin composite sheet reinforced with glass fibers, and more specifically, a mat formed from a cotton-like body of opened glass discontinuous fibers to which thermoplastic synthetic resin powder is dispersed and adhered. Reinforced with glass fibers, which consists of heating to a temperature above the melting (softening) point of the thermoplastic synthetic resin, or after heating, and applying pressure until the gas in the mat ceases to exist or at least does not exist as continuous pores. The present invention relates to a method for producing a thermoplastic synthetic resin composite sheet. The term "spreading" as used herein refers to fiber bundles or strands in which tens to hundreds of single glass fibers are bundled together, or yarns in which a predetermined number of fibers are twisted together by twisting these strands. An operation in which an external force is applied to loosen the material. Furthermore, the term "opened glass fibers" also includes glass single fibers (filaments) produced as intermediate products during the production of strands and yarns. Conventionally, there are the following methods for manufacturing glass fiber-reinforced thermoplastic synthetic resin composite sheets. (a) A method in which cut glass fibers are kneaded with thermoplastic synthetic resin and formed into a sheet using an extruder or the like. (b) A method of bonding two molten thermoplastic synthetic resin sheets through the openings of a woven fabric made of glass fibers with a relatively low weave density (for example, a plain weave cloth). (c) A method of impregnating a glass fiber nonwoven fabric (for example, chopped strand pine, continuous strand pine, etc.) with a molten thermoplastic synthetic resin. However, each of the above conventional techniques has the following drawbacks. In method (a), glass fibers break during the kneading and sheet forming steps, making it difficult to obtain high-strength products. For example, a sheet made by kneading 6 mm long glass fibers (chopped strands) with thermoplastic synthetic resin in a Banbury mixer and molding them in an extruder has most of the glass fibers cut to 2 mm or less in length, and According to such a method, most of the glass fibers are oriented in the warp direction of the sheet, resulting in an imbalance in warp and warp strength. Method (b) does not have the disadvantages of method (a), but it is difficult to impregnate thermoplastic synthetic resin in a woven fabric with dense glass fibers, so thermoplastic synthetic resins with low melt viscosity, It is necessary to use glass fibers with a coarse weaving density. Such cloths are not only expensive, but because the amount of glass fiber used relative to the thermoplastic synthetic resin is kept low, it is difficult to obtain sheets with high strength. In method (c), strands with a small number of glass fiber bundles or chopped strands are generally used to improve impregnation with thermoplastic synthetic resin.
The impregnation process is easier than method (b), but it is still not sufficient, and it is extremely difficult to impregnate thick pine. For example, in order to manufacture a thick sheet of 2 mm or more, it is necessary to impregnate thin pine. It is necessary to laminate many layers of sheets. Furthermore, both methods (b) and (c) have a common drawback in that it is difficult to obtain a sheet with a smooth surface, but this is because both methods use fiber bundles with a considerable diameter, such as strands or rovings. This is because the resin melted and impregnated into the resin shrinks when it solidifies, causing a phenomenon called sink marks. The present inventors have arrived at the present invention as a result of intensive research into a method for manufacturing a glass fiber-reinforced thermoplastic synthetic resin sheet that comprehensively eliminates the above-mentioned drawbacks associated with the prior art. That is, in the present invention, 100 parts by weight of thermoplastic synthetic resin powder with a particle size of 1 mm or less is mixed with a fiber length of 2
A flocculent mat is prepared by mixing and stirring with 5 to 300 parts by weight of discontinuous glass fibers in the range of ~50 mm, or by mixing and stirring with the opened fibers to uniformly disperse the fibers. Smoothing characterized by applying pressure while heating to a temperature higher than the melting point or softening point of the thermoplastic synthetic resin, or after heating, until gas (air) in the mat ceases to exist or at least ceases to exist as continuous pores. This is a method for producing glass fiber reinforced thermoplastic synthetic resin sheets. The glass fiber reinforced thermoplastic synthetic resin sheet obtained by the method of the present invention has the following characteristics. (1) Because the opened discontinuous glass fibers are uniformly dispersed during the manufacturing process without being broken, the resulting sheet has a smooth surface, no unbalanced strength in the weft and weft, and is resistant to impact. Excellent mechanical strength such as strength and tensile strength. (2) Since the amount of the synthetic resin dispersed and adhered to the glass fibers can be varied over a wide range, the glass fiber content of the resulting sheet can also be varied over a wide range. For example, it is possible to mix 300 parts by weight of glass fiber with 100 parts by weight of synthetic resin.
Therefore, a sheet having excellent strength can be easily obtained. (3) Thermoplastic synthetic resins must be in the form of powder, and there are no other limitations, so the resin can be used in a wide range of applications. (4) Commercially available relatively inexpensive rovings, strands, and chopped strands that have been cut in advance can be used as glass fibers, so
Economically advantageous. (5) Since it is a combination of glass discontinuous fibers and thermoplastic synthetic resin, the molded composite sheet can be further shaped into any desired shape by press molding (stamping molding). (6) Can be easily manufactured into any desired sheet, from thin sheets with a thickness of 1 mm or less to thick sheets with a thickness of 4 mm or more. The configuration of the present invention will be described in detail below. Commercially available products are used as the glass fibers used in the present invention. Among these, strands are made by pulling tens to hundreds of single glass fibers (filaments) together and bundled with a glue such as polyvinyl acetate, polyester, or epoxy resin, and winding several tens to dozens of these filaments. Preferably, the rovings are cut to a predetermined length. In addition, it is convenient to use commercially available chopped strands that are cut into various lengths. Alternatively, a yarn obtained by twisting the strands and twisting a predetermined number of yarns can also be used, but the former is preferable from the viewpoint of ease of opening. Since the product of the present invention is intended to be a sheet with a smooth, homogeneous surface and high strength, the bundled strands used need to be opened to loosen them as much as possible and make them fluffy. Therefore, it is preferable to use a so-called soft type strand that uses a small amount of sizing agent, and if the strand is tightly bundled, it is preferable to remove the sizing agent with a solvent beforehand. on the other hand,
In the present invention, it is also possible to cut and use filaments obtained as intermediate products during the production of strands, etc., which are not generally commercially available. When using these materials, it is preferable to pre-treat the surface with a silane-based or borane-based coupling agent in order to increase the bonding strength with the thermoplastic synthetic resin. The glass fibers used in the present invention are cut into relatively long lengths, and the length must be at least 2 mm, preferably 3 mm or more. The use of glass fibers with a length of less than 2 mm is undesirable because the strength of the glass fibers is comparable to that of conventional sheets obtained by kneading the glass fibers with a thermoplastic synthetic resin and molding them using an extruder. On the other hand, there is no clear limit on the upper limit of the length, but even if the length of the glass fiber exceeds 50 mm, the strength will not particularly increase. This is not preferable because it makes opening the fibers and dispersing the synthetic resin powder difficult. The thermoplastic synthetic resin used in the present invention is not particularly limited, and examples include polyolefin resins, polystyrene resins, polyvinyl chloride resins, polyacrylic acid resins, polyamide resins, polyester resins, and polycarbonate resins. used.
In order to further increase the bonding strength with glass fibers, these resins can be chemically modified and used. In order to increase the added value of the sheet obtained by the method of the present invention, for example, to impart twist resistance, flame retardant treatment is applied to the resin, and to impart heat resistance, thermally crosslinkable resin powder is applied to glass fibers. It is also possible to carry out treatments such as dispersion and adhesion and crosslinking during molding. In the present invention, powder is always used for the thermoplastic synthetic resin, and the particle size thereof is 1 mm or less, preferably
It is 0.5mm or less. If the particle size exceeds 1 mm or more,
The synthetic resin settles under its own weight and is not uniformly dispersed in the glass fiber floc. This synthetic resin powder may be machine-pulverized from general pellet-like, bead-like products, or molded product waste, but it is preferable to use powder obtained during the synthetic resin manufacturing process. This is the most advantageous in terms of economy. The amount of glass fiber used in the method of the present invention is 5 to 300 parts by weight per 100 parts by weight of the thermoplastic synthetic resin.
Preferably it is 10 to 200 parts by weight. If this amount is less than 5 parts by weight, almost no reinforcing effect by the glass fibers will be observed, and if it exceeds 300 parts by weight, it will not be possible to obtain a sheet in which the glass fibers are completely wrapped in the synthetic resin. Next, an embodiment of the method for producing a glass fiber-reinforced thermoplastic synthetic resin composite sheet of the present invention will be described. The method of the present invention involves cutting continuous glass fibers,
After opening, thermoplastic synthetic resin powder is attached,
Alternatively, cut glass fibers are mixed and stirred with thermoplastic synthetic resin powder while being opened, and the thermoplastic synthetic resin powder is dispersed and adhered to the cotton-like material, which is shaped into a pine-like material with almost uniform thickness, and then heated. This is a method in which the plastic synthetic resin is heated to a temperature higher than its melting (softening) point, pressurized until at least continuous air pores no longer exist, and then cooled. Glass fibers, such as chopped strands that have been opened in advance, or cut strand yarns that have been opened, are charged into a mixer such as a twin-screw ribbon blender, and thermoplastic synthetic resin powder is added to the mixer. Add the resin powder and mix and adhere while stirring, or mix and stir chopped strands and synthetic resin powder at the same time.
The thermoplastic synthetic resin powder is dispersed and adhered to the flocculent body by a method in which the synthetic resin powder is gradually mixed and adhered to the chopped strands during the opening process. In this way, the mechanism by which the thermoplastic synthetic resin powder is uniformly distributed and adhered to the glass fiber flocculent body is due to the effect that the synthetic resin powder is wrapped in the entanglement of the fibers of the glass fiber flocculent body. It is also assumed that electrostatic force generated by friction during mixing is acting. Therefore, the use of glass fibers treated with antistatic agents in the present invention should be avoided. Next, the mat in which thermoplastic synthetic resin powder is dispersed and adhered to the obtained glass flocculent is heated to a temperature higher than the melting (softening) point of the synthetic resin, or is pressed after heating. The degree of pressurization at this time is preferably as high as possible, and in practice, the gas (air) existing in the pine is completely expelled and no longer exists in the pine, or at least no longer exists as continuous pores. The material is melted and pressurized until it loses air permeability. Since the voids (independent pores) remaining in the sheet deteriorate the physical properties of the sheet, that is, the mechanical strength, it is preferable to carry out melting and pressing at as high a temperature and pressure as possible. The above-mentioned method of forming a flocculent body of glass fiber in which synthetic resin powder is dispersed and adhered into a mat shape, heating and pressurizing it to form a sheet can be carried out by either a batch method or a continuous method. When using the batch method, a mold of a predetermined size is filled with flocculent glass fibers in which synthetic resin powder is dispersed and adhered, heated and pressurized from the outside, and then cooled and taken out. Ru. When using a continuous method, for example, a flocculent body of glass fibers is continuously fed onto a belt conveyor to form a mat, which is then temporarily compressed with an endless belt placed above it while being heated from the outside, or several fibers are The method used is to compress the material through heating rolls, form it into a sheet, cool it with cooling rolls, and then take it off. As detailed above, the glass fiber-reinforced thermoplastic synthetic resin composite sheet obtained by the method of the present invention has a smooth, homogeneous surface and high mechanical strength, so it can be used widely as a plate material. In addition, since the discontinuous glass fibers are uniformly dispersed, it can be used as a raw material that can be further thermoformed into products of various shapes using matted metal dies, that is, stampable sheets. It can also be served. The present invention will be specifically described below with reference to Examples. Example 1 Polypropylene (product name:
"Mitsui Noblen JHH (G)" manufactured by Mitsui Toatsu Chemical Co., Ltd.)
Using 100 parts by weight of powder (particle size of 20 mesh or less) and 20 parts by weight of chopped glass fiber with a length of 6 mm (trade name "CS6PE-612", manufactured by Nitto Boseki Co., Ltd.), both were combined. When the chopped strands were placed in a beaker and stirred and mixed using two stirring rods while applying frictional force to the chopped strands, the chopped strands were gradually opened into a cotton-like material, into which polypropylene powder was added. A mixture was obtained in which the particles were almost uniformly dispersed and adhered. Next, 135 g of the mixture was piled up in a mat shape of approximately the same thickness in a metal frame with a long side of 250 mm, a short side of 150 mm, and a depth of 3.5 mm, and the top and bottom of the pile was covered with two pressing iron plates. Load it into a 100 ton hydraulic press,
Preheat at 220℃ for 5 minutes, then heat at 220℃ for 5 minutes at 100℃.
Pressurized at a pressure of Kg/cm 2 G, then transferred to another hydraulic press and heated at 35°C for 5 minutes at a pressure of 100 Kg/cm 2 G.
It was cooled down. The obtained sheet is a polypropylene sheet (thickness 3.5 x length 250 x width 150 mm) in which opened glass fibers with a length of 6 mm are almost uniformly dispersed.
It was hot. Table 1 shows the tensile strength and Izod impact strength results measured for this sheet. Comparative Example 1 The same glass fibers and polypropylene as in Example 1 were charged into a Brabender plastograph mixer in the same ratio as in Example 1, and kneaded at 180°C for 5 minutes.
When the obtained kneaded product was press-molded in the same manner as in Example 1, a polypropylene sheet was obtained in which glass fibers cut into lengths of approximately 0.2 to 1 mm during kneading were uniformly dispersed. The tensile strength and Izod impact strength of this sheet are shown in Table 1, and both values were significantly inferior to those of Example 1. Example 2 100 parts by weight of the same polypropylene powder used in Example 1 and 67 parts by weight of chopped strands were stirred and mixed in the same manner as in Example 1.
A sheet was prepared in the same manner as in Example 1 using 160 g. The obtained sheet was a polypropylene sheet in which opened glass fibers having a length of 6 mm were almost uniformly dispersed. The tensile strength and Izot impact strength are shown in Table 1, and the values were somewhat higher than those of Example 1. Example 3 The same polypropylene used in Example 1
Using 100 parts by weight and 67 parts by weight of a chopped strand of glass fiber with a length of 25 mm (product name: "CS-25Z-700" manufactured by Nittobo Co., Ltd.) from which the sizing agent was removed with acetone, The mixture was stirred and mixed in the same manner as in Example 1, and a sheet was prepared in the same manner as in Example 1 using 160 g of the mixture. The obtained sheet was a polypropylene sheet in which opened glass fibers having a length of 25 mm were almost uniformly dispersed. The tensile strength and Izot impact strength are shown in Table 1, and both showed the highest values. Example 4 Thermoplastic synthetic resin and high-density polyethylene (product name: "Stafrene E-891", manufactured by Nippon Petrochemicals Co., Ltd.)
100 parts by weight of powder (particle size of 20 mesh or less) and the same chopped strand as used in Example 1
Using 100 parts by weight, the mixture was stirred and mixed in the same manner as in Example 1, and 180 g thereof was used to prepare a sheet in the same manner as in Example 1. The obtained sheet was a polyethylene sheet in which opened glass fibers having a length of 6 mm were almost uniformly dispersed. The tensile strength and Izot impact strength are shown in Table 1. Example 5 100 parts by weight of powder obtained by mechanically crushing a polystyrene molded product into a thermoplastic synthetic resin and passing it through a 20-mesh sieve, and 300 parts by weight of the same chopped strands used in Example 1 were used. The mixture was stirred and mixed in the same manner as in Example 1, and a sheet was prepared in the same manner as in Example 1 using 240 g of the mixture. The obtained sheet was a polystyrene sheet in which opened glass fibers having a length of 6 mm were almost uniformly dispersed.
【表】
比較例 2
実施例5と同じポリスチレン粉体100重量部を
市販のガラス繊維チヨツプドストランドマツト
(商品名「MC450A−104」日東紡績社製)300重
量部の上に均一にのせ、これを鉄製の2枚の押さ
え板ではさんで実施例1と同じプレス条件でシー
トを作成した。得られたシート(厚さ0.4mm×200
mm×200mm)はチヨツプドストランドマツトに対
するポリスチレンの浸透が不充分で下面はガラス
繊維がむき出しになつていた。[Table] Comparative Example 2 100 parts by weight of the same polystyrene powder as in Example 5 was uniformly placed on 300 parts by weight of commercially available glass fiber chopped strand mat (trade name "MC450A-104" manufactured by Nittobo Co., Ltd.). This was sandwiched between two iron pressing plates to produce a sheet under the same pressing conditions as in Example 1. Obtained sheet (thickness 0.4mm x 200
mm x 200 mm), the penetration of the polystyrene into the chopped strand pine was insufficient, and the glass fibers were exposed on the bottom surface.
Claims (1)
100重量部を、繊維長2〜50mmの範囲の不連続な
ガラス繊維5〜300重量部と開繊しながら混合撹
拌するか、もしくは開繊された該繊維と混合撹拌
し、均一に分散せしめてなる綿状体マツトを、該
熱可塑性合成樹脂の融点又は軟化点以上の温度に
加熱しながら、あるいは加熱後に、マツト中の気
体(空気)が存在しなくなるか、少なくとも連続
気孔として存在しなくなるまで加圧することを特
徴とする平滑なガラス繊維補強熱可塑性合成樹脂
シートの製法。1 Thermoplastic synthetic resin powder with a particle size of 1 mm or less
100 parts by weight is mixed and stirred with 5 to 300 parts by weight of discontinuous glass fibers having a fiber length in the range of 2 to 50 mm while being opened, or mixed and stirred with the opened fibers to uniformly disperse the fibers. While heating the flocculent pine to a temperature equal to or higher than the melting point or softening point of the thermoplastic synthetic resin, or after heating, until the gas (air) in the pine ceases to exist or at least ceases to exist as continuous pores. A method for manufacturing smooth glass fiber reinforced thermoplastic synthetic resin sheets, which is characterized by pressurization.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8690079A JPS5611229A (en) | 1979-07-11 | 1979-07-11 | Manufacture of glass fiber reinforced thermoplastic synthetic resin sheet |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8690079A JPS5611229A (en) | 1979-07-11 | 1979-07-11 | Manufacture of glass fiber reinforced thermoplastic synthetic resin sheet |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5611229A JPS5611229A (en) | 1981-02-04 |
| JPH0137503B2 true JPH0137503B2 (en) | 1989-08-08 |
Family
ID=13899701
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8690079A Granted JPS5611229A (en) | 1979-07-11 | 1979-07-11 | Manufacture of glass fiber reinforced thermoplastic synthetic resin sheet |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5611229A (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6140359A (en) * | 1984-08-02 | 1986-02-26 | Idemitsu Petrochem Co Ltd | Glass fiber-containing thermoplastic resin |
| JPS6264516A (en) * | 1985-09-18 | 1987-03-23 | Aisin Seiki Co Ltd | Fiber-reinforced thermoplastic resin molded part |
| JPH02169632A (en) * | 1988-12-22 | 1990-06-29 | Nkk Corp | Method for producing plastic sheet with fibrous filler dispersed |
| JPH03294338A (en) * | 1990-04-11 | 1991-12-25 | Sekisui Chem Co Ltd | Production of fiber-reinforced vinyl chloride resin molded article |
| JPH0767705B2 (en) * | 1992-01-29 | 1995-07-26 | ゼネラル・エレクトリック・カンパニイ | Method for improving surface shape of composite structure |
| JP5275476B2 (en) * | 2009-12-25 | 2013-08-28 | Ykk株式会社 | Upper mold for button mounting |
| JP5576147B2 (en) * | 2010-03-01 | 2014-08-20 | 帝人株式会社 | Carbon fiber composite material |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5070693A (en) * | 1973-11-01 | 1975-06-12 | ||
| US3908591A (en) * | 1974-04-29 | 1975-09-30 | Owens Corning Fiberglass Corp | Apparatus for treating sheet material |
-
1979
- 1979-07-11 JP JP8690079A patent/JPS5611229A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5611229A (en) | 1981-02-04 |
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