JP3027540B2 - Manufacturing method of long fiber reinforced thermoplastic resin composite - Google Patents

Manufacturing method of long fiber reinforced thermoplastic resin composite

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Publication number
JP3027540B2
JP3027540B2 JP16372696A JP16372696A JP3027540B2 JP 3027540 B2 JP3027540 B2 JP 3027540B2 JP 16372696 A JP16372696 A JP 16372696A JP 16372696 A JP16372696 A JP 16372696A JP 3027540 B2 JP3027540 B2 JP 3027540B2
Authority
JP
Japan
Prior art keywords
continuous fiber
fiber bundle
thermoplastic resin
opening
fiber
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
Application number
JP16372696A
Other languages
Japanese (ja)
Other versions
JPH09323322A (en
Inventor
徹 水上
憲吾 尾崎
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Asahi Fiber Glass Co Ltd
Original Assignee
Asahi Fiber Glass Co Ltd
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Filing date
Publication date
Application filed by Asahi Fiber Glass Co Ltd filed Critical Asahi Fiber Glass Co Ltd
Priority to JP16372696A priority Critical patent/JP3027540B2/en
Publication of JPH09323322A publication Critical patent/JPH09323322A/en
Application granted granted Critical
Publication of JP3027540B2 publication Critical patent/JP3027540B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、FRTP(繊維強
化熱可塑性樹脂)の成形材料となる、熱可塑性樹脂の含
浸性を向上させた長繊維強化熱可塑性樹脂複合材料の製
造法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a long fiber reinforced thermoplastic resin composite material having improved thermoplastic resin impregnation, which is a molding material for FRTP (fiber reinforced thermoplastic resin).

【0002】[0002]

【従来の技術】連続長繊維で強化されたFRTP(繊維
強化熱可塑性樹脂)は、短繊維で強化された一般的なF
RTPより力学的特性に優れており、近年、盛んに利用
されるようになってきている。
2. Description of the Related Art FRTP (fiber reinforced thermoplastic resin) reinforced with continuous long fibers is made of general FRP reinforced with short fibers.
It has better mechanical properties than RTP, and has recently been used actively.

【0003】長繊維強化熱可塑性樹脂複合材料は、一般
的には、連続繊維束を、溶融した熱可塑性樹脂中に引き
込み、ダイを通して引き抜くプルトルージョン法により
製造され、場合によっては任意の長さに切断して使用さ
れている。長繊維強化熱可塑性樹脂複合材料は、力学的
特性を十分発揮させるため、また、外観、作業性の面か
らも、連続繊維束に熱可塑性樹脂を十分かつ均一に含浸
させる必要がある。
[0003] The long fiber reinforced thermoplastic resin composite material is generally produced by a pultrusion method in which a continuous fiber bundle is drawn into a molten thermoplastic resin and drawn through a die. Used by cutting. The long fiber reinforced thermoplastic resin composite material needs to sufficiently and uniformly impregnate the continuous fiber bundle with the thermoplastic resin in order to sufficiently exhibit the mechanical properties and also in view of appearance and workability.

【0004】樹脂の含浸性を向上させる方法の一つとし
て、連続繊維束に開繊処理を施した後に樹脂を含浸させ
る方法が知られており、開繊処理の方法について種々の
方法が行われている。例えば、テンションバー又はロー
ルにかけて開繊する方法、静電気による繊維間の反発を
利用して開繊する方法、エアージェットやウォータージ
ェットを吹き付けて開繊する方法等がとられている。
[0004] As one of the methods for improving the impregnating property of a resin, a method of impregnating a continuous fiber bundle with a resin after performing a fiber opening treatment is known, and various methods of the fiber opening treatment are performed. ing. For example, a method of opening with a tension bar or a roll, a method of opening by utilizing repulsion between fibers due to static electricity, a method of blowing with an air jet or a water jet, and the like are used.

【0005】一方、特開平7-216104号公報には、開繊工
程で連続繊維束を開繊し、次いで含浸工程で開繊連続繊
維束へ溶融樹脂を含浸させる長繊維強化樹脂構造物の製
造方法において、前記開繊連続繊維束の下記数式2で定
義される開繊指標Sが2.0 〜18.0の範囲にあることを特
徴とする長繊維強化樹脂構造物の製造方法が開示されて
いる。
[0005] On the other hand, Japanese Patent Application Laid-Open No. 7-216104 discloses the production of a long fiber reinforced resin structure in which a continuous fiber bundle is opened in a fiber opening step, and then a molten resin is impregnated in the continuous fiber bundle in an impregnation step. In the method, there is disclosed a method for producing a long fiber reinforced resin structure, wherein an opening index S defined by the following mathematical formula 2 of the opened continuous fiber bundle is in a range of 2.0 to 18.0.

【0006】[0006]

【数2】S=5×10-2・(T/L)・(1/R) (式中、Tは連続繊維束のテックス数を表し、Rは連続
繊維の繊維径(μm)を表し、Lは連続繊維束の幅(c
m)を表す。)
S = 5 × 10−2 · (T / L) · (1 / R) (where T represents the number of tex of the continuous fiber bundle, and R represents the fiber diameter (μm) of the continuous fiber. , L is the width of the continuous fiber bundle (c
m). )

【0007】[0007]

【発明が解決しようとする課題】しかしながら、本発明
者らの研究によると、特開平7-216104号公報に記載され
た上記開繊指標の範囲では、樹脂の含浸性が未だ十分と
は言えないことがわかった。このため、開繊の程度を更
に大きくすることを検討したが、その場合、従来の開繊
方法では、次のような問題点があった。
However, according to the study of the present inventors, within the range of the above-mentioned fiber opening index described in JP-A-7-216104, the impregnating property of the resin is not yet sufficient. I understand. For this reason, it was examined to further increase the degree of spreading, but in that case, the conventional spreading method had the following problems.

【0008】すなわち、テンションバー又はロールを用
いる方法においては、通過回数を増やすか又は張力を高
くすることが必要となり、連続繊維束に大きなダメージ
を与え、フィラメント切れ等を引き起こし、作業性を悪
化させるだけでなく、長繊維強化熱可塑性樹脂複合材料
とした場合に強度低下を生じるという問題があった。ま
た、テンションバー又はロールの表面形状をタイコ型に
して開繊効果を高めることも提案されているが、その場
合には、連続繊維束の開繊に偏りが生じるという問題が
あった。
That is, in the method using a tension bar or a roll, it is necessary to increase the number of passages or increase the tension, which causes a large damage to the continuous fiber bundle, causes a filament breakage, etc., and deteriorates workability. In addition, there has been a problem that when a long fiber reinforced thermoplastic resin composite material is used, the strength is reduced. Further, it has been proposed to increase the opening effect by making the surface shape of the tension bar or the roll into a Tyco shape, but in that case, there was a problem that the opening of the continuous fiber bundle was biased.

【0009】また、静電気を利用する方法においては、
開繊方向が二次元的となって、取扱いにくいという問題
があった。更に、エアージェットを利用した方法は、均
一な気体流を得ることが困難で、したがって、均一に開
繊しにくいという問題があった。更にまた、ウォーター
ジェットによる方法は、水を除去する工程が必要になる
という問題があった。
In the method using static electricity,
There has been a problem that the opening direction is two-dimensional and it is difficult to handle. Furthermore, the method using an air jet has a problem that it is difficult to obtain a uniform gas flow, and therefore it is difficult to uniformly open the fiber. Furthermore, the method using a water jet has a problem that a step of removing water is required.

【0010】本発明は、上記問題点に鑑みてなされたも
ので、その目的は、樹脂を十分かつ均一に含浸させるこ
とによって、力学的特性を十分発揮できるようにした長
繊維強化熱可塑性樹脂複合材料の製造法を提供すること
にある。
The present invention has been made in view of the above problems, and has as its object to provide a long fiber reinforced thermoplastic resin composite which can sufficiently exhibit mechanical properties by impregnating a resin sufficiently and uniformly. It is to provide a method for manufacturing a material.

【0011】[0011]

【課題を解決するための手段】上記目的を達成するた
め、本発明は、無撚りの連続繊維束を、平均流速10〜
50m/秒で流れる気体中に、この気体の流れ方向に対
してほぼ直交する方向から導入し、前記気体流中を通過
する際に、通過方向に沿った長さ10mm当たりに対し
て1〜50mmたるむようにたるみを与えて開繊処理を
施し、下記数式1で定義される開繊指数Fが0.5〜3
とされた開繊連続繊維束を得た後、この開繊連続繊維束
に熱可塑性樹脂を含浸させることを特徴とする長繊維強
化熱可塑性樹脂複合材料の製造法である。
In order to achieve the above object, the present invention provides a non-twisted continuous fiber bundle having an average flow rate of 10 to 10.
In a gas flowing at 50 m / sec,
And introduced in a direction substantially perpendicular to the gas flow
When doing, per 10mm length along the passing direction
1 to 50 mm to give a sag and open the fiber
And the opening index F defined by the following formula 1 is 0.5 to 3
A method for producing a continuous fiber reinforced thermoplastic resin composite material, comprising: obtaining a continuous fiber bundle of spread fiber obtained as described above; and impregnating the continuous fiber bundle of spread fiber with a thermoplastic resin.

【0012】[0012]

【数3】F=W/DN (数式中、Fは開繊指数、Wは連続繊維束の幅(mm)、
Dは連続繊維モノフィラメントの径(mm)、Nは連続繊
維モノフィラメントの本数を表し、連続繊維束の幅は、
巻糸においては有姿の状態で測定し、開繊処理直後のも
のは処理装置出口における状態で測定する。)
F = W / DN (where F is the opening index, W is the width (mm) of the continuous fiber bundle,
D represents the diameter (mm) of the continuous fiber monofilament, N represents the number of continuous fiber monofilaments, and the width of the continuous fiber bundle is
The wound yarn is measured in a tangible state, and the yarn immediately after the opening processing is measured in a state at the outlet of the processing apparatus. )

【0013】本発明において開繊指数Fとは、上記数式
3で定義するものであって、以下、開繊指数とのみ記載
する。
In the present invention, the fiber opening index F is defined by the above formula 3, and hereinafter, only the fiber opening index will be described.

【0014】[0014]

【0015】本発明の長繊維強化熱可塑性樹脂複合材料
の製造法によれば、無撚りの連続繊維束に開繊処理を施
すので開繊しやすく、工業的に作業性よく開繊指数が
0.5〜3となるように開繊することができる。また、
上記開繊指数とされた開繊連続繊維束に熱可塑性樹脂を
含浸させるので、熱可塑性樹脂が十分かつ均一に含浸さ
れる。したがって、力学的特性に優れ、外観に優れたF
RTP成形品を得ることができる長繊維強化熱可塑性樹
脂複合材料を作業性よく得ることができる。
[0015] The long fiber reinforced thermoplastic resin composite material of the present invention
According to the manufacturing method, the untwisted continuous fiber bundle is opened.
Easy to open, and industrially easy to open
The fiber can be spread so as to be 0.5 to 3. Also,
Since the opened continuous fiber bundle having the opening index is impregnated with the thermoplastic resin, the thermoplastic resin is sufficiently and uniformly impregnated. Therefore, F having excellent mechanical properties and excellent appearance
A long fiber reinforced thermoplastic resin composite material from which an RTP molded product can be obtained can be obtained with good workability.

【0016】上記開繊処理方法の原理は未だよくわかっ
ていないが、連続繊維束の幅方向の中央部と両端部とに
おける気体の流速の違いから発生する圧力差により、連
続繊維束が外側に広がって開繊するものと考えられる。
なお、この方法によると、フィラメント切れ等のダメー
ジを与えることがないので、長繊維強化熱可塑性樹脂複
合材料とした際に強度低下が生じず、また、開繊に用い
た水等の除去の必要もない。
Although the principle of the above-mentioned fiber opening treatment method is not yet well understood, the continuous fiber bundle is moved outward by a pressure difference generated due to a difference in gas flow rate between the center and both ends in the width direction of the continuous fiber bundle. It is thought that it spreads and spreads.
In addition, according to this method, since there is no damage such as filament breakage, the strength does not decrease when a long fiber reinforced thermoplastic resin composite material is used, and it is necessary to remove water and the like used for fiber opening. Nor.

【0017】[0017]

【発明の実施の形態】本発明において、連続繊維束を構
成する繊維としては、例えば、ガラス繊維、カーボン繊
維、セラミック繊維、金属繊維、アラミド繊維等から選
ばれた一種又は二種以上の混合物を使用することができ
るが、物性、価格等の点から、ガラス繊維を用いるのが
好ましい。なお、これらの繊維は、マトリックスとなる
熱可塑性樹脂とのヌレ性や接着性を高めるために、表面
処理を施しておいてもよい。
BEST MODE FOR CARRYING OUT THE INVENTION In the present invention, the fibers constituting a continuous fiber bundle include, for example, one or a mixture of two or more selected from glass fibers, carbon fibers, ceramic fibers, metal fibers, and aramid fibers. Although it can be used, it is preferable to use glass fiber from the viewpoint of physical properties, price, and the like. In addition, these fibers may be subjected to a surface treatment in order to enhance wettability and adhesiveness with a thermoplastic resin serving as a matrix.

【0018】連続繊維束の集束本数は、取扱性等を考慮
して、400 〜4000本程度とすることが好ましい。ガラス
繊維束の場合、好ましくはストランドが用いられるが、
シングルエンドロービング等のロービングを用いてもよ
い。また、連続繊維束は、実質的に無撚りのものを用い
る。撚りがかかったものは、開繊処理を施した際に、十
分開繊されないので好ましくない。
The number of continuous fiber bundles to be bundled is preferably about 400 to 4000 in consideration of handleability and the like. In the case of a glass fiber bundle, a strand is preferably used,
Roving such as single-ended roving may be used. In addition, a continuous fiber bundle is substantially non-twisted. Twisted fibers are not preferable because they are not sufficiently opened when subjected to the opening process.

【0019】本発明で用いる熱可塑性樹脂としては、F
RTPのマトリックスとして一般に用いられているもの
を使用することができ、例えば、ポリエチレン、ポリプ
ロピレン等のポリオレフィン樹脂、ナイロン6、ナイロ
ン6,6等のポリアミド樹脂、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等のポリエステル樹
脂、ポリカーボネイト、ポリアセタール等のその他の熱
可塑性樹脂、あるいはそれらの変性物を単独、あるいは
組み合わせて使用することができる。また、熱可塑性樹
脂には、必要に応じて酸化防止剤、帯電防止剤、難燃
剤、潤滑剤、離型剤、可塑剤、着色剤、体質フィラー等
の一般的な添加剤を添加してもよい。
The thermoplastic resin used in the present invention includes F
As the matrix of RTP, those generally used can be used, for example, polyethylene, polyolefin resins such as polypropylene, polyamide resins such as nylon 6, nylon 6,6, polyethylene terephthalate, polyester resins such as polybutylene terephthalate, Other thermoplastic resins such as polycarbonate and polyacetal, or modified products thereof can be used alone or in combination. Also, the thermoplastic resin may be added with general additives such as an antioxidant, an antistatic agent, a flame retardant, a lubricant, a release agent, a plasticizer, a coloring agent, and a filler as necessary. Good.

【0020】本発明の長繊維強化熱可塑性樹脂複合材料
の繊維含有率は、特に制限されないが、補強効果、物性
等の面から、8〜85容量%とすることが好ましく、15〜
75容量%がより好ましい。
The fiber content of the long-fiber-reinforced thermoplastic resin composite material of the present invention is not particularly limited, but is preferably from 8 to 85% by volume, from the viewpoint of the reinforcing effect and physical properties, and is preferably from 15 to 85% by volume.
75% by volume is more preferred.

【0021】図1、2には、本発明を実施するための製
造装置の一例が示されている。図1は同製造装置の概略
側面図、図2は同製造装置における開繊装置の概略平面
図である。
FIGS. 1 and 2 show an example of a manufacturing apparatus for carrying out the present invention. FIG. 1 is a schematic side view of the manufacturing apparatus, and FIG. 2 is a schematic plan view of a fiber opening apparatus in the manufacturing apparatus.

【0022】図1、2において、11は連続繊維束12
aの回巻体であるケーキ、13は連続繊維束12aを引
き出すための駆動ロール、14は吸引方式によって気体
流を形成する開繊装置、15は連続繊維束に樹脂を含浸
させるためのダイ、16は樹脂を含浸された連続繊維束
を引き取るための引き取り装置、17は得られた長繊維
強化熱可塑性樹脂複合材料をペレット化するペレタイザ
ーである。
1 and 2, reference numeral 11 denotes a continuous fiber bundle 12;
a is a wound roll of cake, 13 is a drive roll for drawing out the continuous fiber bundle 12a, 14 is a fiber opening device that forms a gas flow by a suction method, 15 is a die for impregnating the continuous fiber bundle with resin, Reference numeral 16 denotes a take-off device for taking out a continuous fiber bundle impregnated with a resin, and 17 denotes a pelletizer for pelletizing the obtained long fiber reinforced thermoplastic resin composite material.

【0023】この製造装置によれば、複数個の連続繊維
束のケーキ11を回転させつつ、その外側から、連続繊
維束12aがそれぞれ引き出され、駆動ロール13を経
て、開繊装置14に供給される。なお、連続繊維束12
aを、連続繊維束ケーキ11を回転させつつ、その外側
から引き出すのは、連続繊維束12aに撚りを与えない
ようにするためである。
According to this manufacturing apparatus, the continuous fiber bundles 12a are respectively pulled out from the outside while rotating the cake 11 of a plurality of continuous fiber bundles, and supplied to the fiber opening device 14 via the driving rolls 13. You. The continuous fiber bundle 12
The reason why a is pulled out from the outside while rotating the continuous fiber bundle cake 11 is to prevent the continuous fiber bundle 12a from being twisted.

【0024】開繊装置14は、例えば吸引手段によっ
て、平均流速10〜50m/秒で矢印イの方向に流れる気体
流を形成する。連続繊維束12aは、この気体流に対し
てほぼ直交する方向から導入され、通過方向に沿った長
さ10mm当たりに対して1〜50mmたるむようにたるみAを
与えられながら、上記気体流中を通過する。そして、連
続繊維束12aは、上記気体流中を通過する間に開繊処
理され、前記数式3で定義される開繊指数が0.5 〜3と
された開繊連続繊維束12bが得られる。
The opening device 14 forms a gas flow flowing in the direction of arrow A at an average flow velocity of 10 to 50 m / sec by, for example, suction means. The continuous fiber bundle 12a is introduced from a direction substantially perpendicular to the gas flow, and passes through the gas flow while being given a sag A so as to sag 1 to 50 mm per 10 mm in length in the passing direction. I do. Then, the continuous fiber bundle 12a is subjected to fiber opening processing while passing through the above gas stream, and an open fiber continuous fiber bundle 12b having a fiber opening index defined by the equation (3) of 0.5 to 3 is obtained.

【0025】次に、この開繊連続繊維束12bを、図示
しない溶融押出機から供給管15aを介して熱可塑性樹
脂を供給されるダイ15に導入して、熱可塑性樹脂を含
浸させる。こうして得られた長繊維強化熱可塑性樹脂複
合材料を引き取り装置16で引き取り、ペレタイザー1
7により所望のサイズに切断してペレット化する。
Next, the opened continuous fiber bundle 12b is introduced into a die 15 to which a thermoplastic resin is supplied from a melt extruder (not shown) via a supply pipe 15a, and is impregnated with the thermoplastic resin. The long fiber reinforced thermoplastic resin composite material thus obtained is taken out by the take-up device 16 and the pelletizer 1
7. Cut to desired size and pelletize.

【0026】なお、上記開繊装置14において、気体
は、空気、不活性ガス等の安全なガスであれば何でもよ
いが、平均流速10〜50m/秒で流れるようにすることが
必要である。気体の平均速度が10m/秒未満の場合、連
続繊維束12aが十分開繊されるまでに時間がかかる
か、又は十分に開繊されず、50m/秒を超えると、連続
繊維束12aを構成しているフィラメントが切れやすく
なるので好ましくない。
In the fiber opening device 14, any gas may be used as long as it is a safe gas such as air or an inert gas, but it is necessary that the gas flow at an average flow velocity of 10 to 50 m / sec. When the average velocity of the gas is less than 10 m / sec, it takes time until the continuous fiber bundle 12a is sufficiently opened, or when the gas is not sufficiently opened, and when it exceeds 50 m / sec, the continuous fiber bundle 12a is formed. This is not preferable because the filaments that are cut tend to break.

【0027】また、連続繊維束12aのたるみAは、通
過方向に沿った長さ10mm当たりに対して1〜50mmたるむ
ようにする。長さ10mm当たりに対するたるみ量が1mm未
満の場合、十分に開繊せず、50mmを超えると、連続繊維
束12aに過剰な振動が生じるため、導入、引き取りの
隣接部分、あるいは、複数の連続繊維束12a、12a
…を同時に並行して開繊処理している場合は隣の連続繊
維束12aに接触してダメージを受けやすくなるので好
ましくない。
The slack A of the continuous fiber bundle 12a is set so as to sag 1 to 50 mm per 10 mm length along the passing direction. If the slack amount per 10 mm length is less than 1 mm, the fiber is not sufficiently opened, and if it exceeds 50 mm, excessive vibration occurs in the continuous fiber bundle 12a. Bundles 12a, 12a
.. Are simultaneously unparalleled because they are likely to be damaged by contact with the adjacent continuous fiber bundle 12a.

【0028】開繊処理された連続繊維束12bの開繊指
数は0.5 〜3、好ましくは0.5 〜2とする。上記開繊指
数が0.5 未満の場合は、開繊が不十分で熱可塑性樹脂の
含浸性が悪くなり、十分に熱可塑性樹脂を含浸させるた
めには樹脂圧を高くしなければならなくなりなり、開繊
連続繊維束12bの損傷を招く。また、上記開繊指数が
3を超えると、開繊後の連続繊維束12bの取り扱いが
困難になる。
The opening index of the continuous fiber bundle 12b subjected to the opening processing is set to 0.5 to 3, preferably 0.5 to 2. When the fiber opening index is less than 0.5, the fiber opening is insufficient and the impregnating property of the thermoplastic resin is deteriorated, and the resin pressure must be increased to sufficiently impregnate the thermoplastic resin. This causes damage to the fine continuous fiber bundle 12b. On the other hand, if the fiber opening index exceeds 3, it becomes difficult to handle the continuous fiber bundle 12b after fiber opening.

【0029】[0029]

【0030】なお、図1、2の開繊装置14に連続繊維
束12aを導入する前に、連続繊維束を管状通路へ送り
ながら、この通路へ圧縮空気を噴出させて、生じる高速
空気流によって開繊する方法や、連続繊維束を複数個の
テンションバーの間を湾曲させて引っ張って開繊させる
方法等の従来の方法によって、連続繊維束12aにダメ
ージを与えない範囲で予備開繊を施しておいてもよい。
[0030] Note that before the introduction of the continuous fiber bundle 12a to the opening device 14 of FIGS. 1 and 2, sends a continuous fiber bundle into the tubular passage
While blowing compressed air into this passage,
The method of opening the fiber by air flow and the continuous fiber bundle
Curve between tension bars and pull to open
The pre-spreading may be performed by a conventional method such as a method within a range that does not damage the continuous fiber bundle 12a.

【0031】また、開繊連続繊維束12bに熱可塑性樹
脂を含浸させて長繊維強化熱可塑性樹脂複合材料を製造
する方法、上記方法に限定されず、他の方法を採用す
ることもできる。例えば、開繊連続繊維束12bを、2
枚の熱可塑性樹脂のフィルム又は不織布の間に挟み込ん
だ後、加熱ロールプレス、加熱カレンダー等を通してテ
ープ又はシート状の長繊維強化熱可塑性樹脂複合材料と
する方法であってもよい。また、開繊連続繊維束12b
を、熱可塑性樹脂に溶媒を加えて得られる溶液又はエマ
ルジョン中に引込み、加熱炉を通して乾燥すると共に熱
可塑性樹脂を溶融させた後、賦形ノズルを通してテー
プ、シート、あるいはロッド状の長繊維強化熱可塑性樹
脂複合材料とする方法を採用してもよい。
Further, a method for producing a long fiber-reinforced thermoplastic resin composite material to spread tow 12b was impregnated with a thermoplastic resin is not limited to the above method, it is possible to employ other methods. For example, the opened continuous fiber bundle 12b is
After sandwiching between two thermoplastic resin films or nonwoven fabrics, a tape or sheet-like long fiber reinforced thermoplastic resin composite material may be passed through a heated roll press, a heated calendar or the like. In addition, the spread continuous fiber bundle 12b
Into a solution or emulsion obtained by adding a solvent to a thermoplastic resin, dried through a heating furnace and melted the thermoplastic resin, and then passed through a shaping nozzle to form a tape, sheet, or rod-shaped long fiber reinforced heat. A method of forming a plastic resin composite material may be employed.

【0032】得られた長繊維強化熱可塑性樹脂複合材料
は、テープ、シート、あるいはロッド状のままの形で使
用することもでき、前記のようにペレタイザー等によっ
て所定の長さに切断して使用してもよい。
The obtained long fiber reinforced thermoplastic resin composite material can be used as it is in the form of a tape, sheet, or rod, and cut into a predetermined length with a pelletizer or the like as described above. May be.

【0033】本発明の長繊維強化熱可塑性樹脂複合材料
は、例えば、自動車、電気・電子部品のハウジングやケ
ーシング、一般雑貨等の広い分野における成形品に使用
することができる。
The long fiber reinforced thermoplastic resin composite material of the present invention can be used for molded articles in a wide range of fields, such as automobiles, housings and casings of electric and electronic parts, and general goods.

【0034】[0034]

【実施例】【Example】

実施例1 連続繊維束として、繊維径16μmのフィラメントを4000
本集束したガラス繊維ロービングを用いて、平均流速40
m/秒で流れる空気流中へ、空気の流れ方向に対してほ
ぼ直交する方向から、空気流中を通過する際に、通過方
向に沿った長さ30mmに対して60mm(10mmに対して20mm)
たるむようにたるみを与えながら導入して開繊処理を施
した。開繊されたガラス繊維ストランドの幅は77mmであ
り、開繊指数は1.2 であった。
Example 1 As a continuous fiber bundle, a filament having a fiber diameter of 16 μm was 4000
Using this bundled glass fiber roving, average flow rate of 40
When passing through the air flow from a direction substantially perpendicular to the air flow direction into the air flow flowing at m / sec, the length along the passing direction is 60 mm for 30 mm (20 mm for 10 mm) )
It was introduced while giving a slack so that the fiber was opened. The width of the opened glass fiber strand was 77 mm, and the opening index was 1.2.

【0035】次いで、得られた開繊ガラス繊維ストラン
ドを、その幅を維持したまま、溶融されたポリプロピレ
ンが供給されているダイの中に引き込んで、ポリプロピ
レンを含浸させた後、引き出してガラス含有率45容量%
のロッドを得た。
Next, the obtained opened fiber glass strand is drawn into a die to which molten polypropylene is supplied while maintaining the width thereof, and impregnated with polypropylene. 45% by volume
I got a rod.

【0036】次に、得られたロッドを、冷却槽を通した
後、引き取り機で引き取り、ペレタイザーで長さ6mmに
切断して、長繊維強化熱可塑性樹脂複合材料のペレット
を得た。
Next, the obtained rod was passed through a cooling bath, taken up by a take-up machine, and cut into a length of 6 mm with a pelletizer to obtain pellets of a long fiber reinforced thermoplastic resin composite material.

【0037】実施例2 実施例1において空気流の平均流速を20m/秒に代え、
あとは実施例1と同様にして、幅39mm、開繊指数0.6 の
開繊されたガラス繊維ストランドを得た。
Example 2 In Example 1, the average air velocity was changed to 20 m / sec.
Thereafter, in the same manner as in Example 1, an opened glass fiber strand having a width of 39 mm and an opening index of 0.6 was obtained.

【0038】得られた開繊ガラス繊維ストランドを、実
施例1と同様にしてロッドとし、次いで、ペレットにし
た。
The obtained opened fiber glass strand was formed into a rod in the same manner as in Example 1, and then into a pellet.

【0039】比較例 実施例1と同様のガラス繊維ロービングを、ロールバー
を用いて開繊させて、幅10mm、開繊指数0.15の開繊ガラ
ス繊維ストランドを得た。
Comparative Example The same glass fiber roving as in Example 1 was spread using a roll bar to obtain a spread glass fiber strand having a width of 10 mm and a fiber opening index of 0.15.

【0040】得られた開繊ガラス繊維ストランドを、実
施例1と同様にしてロッドとし、次いで、ペレットにし
た。
The obtained opened fiber glass strand was formed into a rod in the same manner as in Example 1, and then into a pellet.

【0041】試験例 実施例1、2、及び比較例で得られたペレットを、ガラ
ス含有率15容量%となるようにポリプロピレンで希釈
し、直接射出成形して試験片とし、ASTMに準拠した
強度試験を行い、引張強度、曲げ強度を測定した。ま
た、100 ×100 ×2.5mm の平板を成形し、目視によって
ガラス繊維ストランドの未分散の個数を数えた。この結
果を表1に示す。
Test Example The pellets obtained in Examples 1 and 2 and Comparative Example were diluted with polypropylene so as to have a glass content of 15% by volume, and directly injection-molded into test pieces to obtain a strength according to ASTM. A test was performed to measure the tensile strength and the bending strength. Further, a flat plate of 100 × 100 × 2.5 mm was formed, and the number of undispersed glass fiber strands was counted visually. Table 1 shows the results.

【0042】[0042]

【表1】 [Table 1]

【0043】表1の結果から、開繊指数を1.2 、0.6 と
した実施例1、2の長繊維強化熱可塑性樹脂複合材料
は、開繊指数が0.15と低い比較例の長繊維強化熱可塑性
樹脂複合材料より、ガラス繊維ストランドの未分散個数
が非常に少なく、また、引張強度、曲げ強度ともに優れ
ていることがわかる。なお、実施例1と2の比較におい
ては、開繊指数が高いほうがこれらの効果が大きいこと
がわかる。
From the results shown in Table 1, the long fiber reinforced thermoplastic resin composite materials of Examples 1 and 2 in which the opening index was set to 1.2 and 0.6 were the long fiber reinforced thermoplastic resins of Comparative Examples having an opening index as low as 0.15. It can be seen that the number of undispersed glass fiber strands is much smaller than that of the composite material, and that both the tensile strength and the bending strength are excellent. In addition, in the comparison between Examples 1 and 2, it can be seen that the higher the fiber opening index, the greater these effects.

【0044】[0044]

【発明の効果】以上説明したように、本発明によれば、
連続繊維束にダメージを与えることなく、かつ作業性よ
く開繊指数が0.5〜3となるように開繊することがで
き、このように大きく開繊させた連続繊維束に熱可塑性
樹脂を含浸させることによって、熱可塑性樹脂が十分か
つ均一に含浸された長繊維強化熱可塑性樹脂複合材料を
得ることができる。そして、この複合材料を用いること
によって、成形品の力学的特性や外観をより一層改善す
ることができる。
As described above, according to the present invention,
Workability without damaging the continuous fiber bundle
The fiber can be spread so that the spread index is 0.5-3.
Can, by impregnating a thermoplastic resin into a continuous fiber bundle is thus increased opening, Ru can be a thermoplastic resin to obtain a sufficient and evenly impregnated long fiber-reinforced thermoplastic resin composite material. Then, by using this composite material can be further improved mechanical properties and appearance of the molded article.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明を実施するための製造装置の一例を示す
概略側面図である。
FIG. 1 is a schematic side view showing an example of a manufacturing apparatus for carrying out the present invention.

【図2】同製造装置に用いられる開繊装置の概略平面図
である。
FIG. 2 is a schematic plan view of a fiber opening device used in the manufacturing apparatus.

【符号の説明】[Explanation of symbols]

11 連続繊維束のケーキ 12a 連続繊維束 12b 開繊連続繊維束 13 駆動ロール 14 開繊装置 15 ダイ 16 引き取り装置 17 ペレタイザー A 連続繊維束のたわみ Reference Signs List 11 cake of continuous fiber bundle 12a continuous fiber bundle 12b spread continuous fiber bundle 13 drive roll 14 fiber opening device 15 die 16 take-off device 17 pelletizer A deflection of continuous fiber bundle

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) B29B 15/08 - 15/14 B29B 11/16 C08J 5/24 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 7 , DB name) B29B 15/08-15/14 B29B 11/16 C08J 5/24

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 無撚りの連続繊維束を、平均流速10〜
50m/秒で流れる気体中に、この気体の流れ方向に対
してほぼ直交する方向から導入し、前記気体流中を通過
する際に、通過方向に沿った長さ10mm当たりに対し
て1〜50mmたるむようにたるみを与えて開繊処理を
施し、下記数式1で定義される開繊指数Fが0.5 〜3と
された開繊連続繊維束を得た後、この開繊連続繊維束に
熱可塑性樹脂を含浸させることを特徴とする長繊維強化
熱可塑性樹脂複合材料の製造法。 【数1】F=W/DN (数式中、Fは開繊指数、Wは連続繊維束の幅(m
m)、Dは連続繊維モノフィラメントの径(mm)、N
は連続繊維モノフィラメントの本数を表し、連続繊維束
の幅は、巻糸においては有姿の状態で測定し、開繊処理
直後のものは処理装置出口における状態で測定する。)
1. An untwisted continuous fiber bundle is produced at an average flow rate of 10 to 10.
In a gas flowing at 50 m / sec,
And introduced in a direction substantially perpendicular to the gas flow
When doing, per 10mm length along the passing direction
1 to 50 mm to give a sag and open the fiber
Subjected, after obtaining the opening continuous fiber bundle open繊指number F, which is defined by the following Equation 1 is as 0.5-3, long fibers, characterized in that impregnating the thermoplastic resin in the opening tow A method for producing a reinforced thermoplastic composite material. F = W / DN (where F is the opening index, W is the width of the continuous fiber bundle (m
m), D is the diameter of continuous fiber monofilament (mm), N
Represents the number of continuous fiber monofilaments, and the width of the continuous fiber bundle is measured in a tangible state in the wound yarn, and the width immediately after the opening processing is measured in a state at the outlet of the processing apparatus. )
JP16372696A 1996-06-04 1996-06-04 Manufacturing method of long fiber reinforced thermoplastic resin composite Expired - Lifetime JP3027540B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16372696A JP3027540B2 (en) 1996-06-04 1996-06-04 Manufacturing method of long fiber reinforced thermoplastic resin composite

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16372696A JP3027540B2 (en) 1996-06-04 1996-06-04 Manufacturing method of long fiber reinforced thermoplastic resin composite

Publications (2)

Publication Number Publication Date
JPH09323322A JPH09323322A (en) 1997-12-16
JP3027540B2 true JP3027540B2 (en) 2000-04-04

Family

ID=15779505

Family Applications (1)

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Country Status (1)

Country Link
JP (1) JP3027540B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006096966A (en) * 2004-09-02 2006-04-13 Daicel Chem Ind Ltd Long fiber-reinforced thermoplastic resin structure, its molding and production method thereof
JP2006167982A (en) * 2004-12-13 2006-06-29 Daicel Chem Ind Ltd Manufacturing method of long fiber reinforced thermoplastic resin structure
CN112976608B (en) * 2021-03-30 2022-11-29 郑州大学 VARTM (vacuum assisted transfer molding) forming die for large-tow continuous carbon fiber reinforced automobile floor

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Publication number Publication date
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