JPH09157415A - Production of prepreg and apparatus for producing the same - Google Patents

Production of prepreg and apparatus for producing the same

Info

Publication number
JPH09157415A
JPH09157415A JP31697995A JP31697995A JPH09157415A JP H09157415 A JPH09157415 A JP H09157415A JP 31697995 A JP31697995 A JP 31697995A JP 31697995 A JP31697995 A JP 31697995A JP H09157415 A JPH09157415 A JP H09157415A
Authority
JP
Japan
Prior art keywords
resin liquid
sheet
prepreg
resin
heating
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP31697995A
Other languages
Japanese (ja)
Other versions
JP3150591B2 (en
Inventor
Toshio Ishioumaru
利雄 石王丸
Kenji Sugiyama
賢治 杉山
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.)
Sumitomo Bakelite Co Ltd
Original Assignee
Sumitomo Bakelite Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sumitomo Bakelite Co Ltd filed Critical Sumitomo Bakelite Co Ltd
Priority to JP31697995A priority Critical patent/JP3150591B2/en
Publication of JPH09157415A publication Critical patent/JPH09157415A/en
Application granted granted Critical
Publication of JP3150591B2 publication Critical patent/JP3150591B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Reinforced Plastic Materials (AREA)
  • Laminated Bodies (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Abstract

PROBLEM TO BE SOLVED: To produce a prepreg containing an extremely small amount of bubbles in a sheetlike substrate comprising a fibrous material even when using a resin liquid at a high concentration. SOLUTION: This method for producing a prepreg comprises coating one surface side of a sheetlike substrate 1 with a resin liquid (3a), then heating the resultant sheetlike substrate 1 from the side of the surface coated with the resin liquid (3a) at a lower temperature than the boiling point of a solvent used in the resin liquid (3a) and subsequently drying the substrate by heating thereof at a higher temperature than the boiling point of the solvent when impregnating the sheetlike substrate 1 comprising a fibrous material with the resin liquid (3a), then drying the resultant substrate and thereby producing the prepreg. Furthermore, the apparatus adopts the method for producing the prepreg.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は産業機器用や電子機器用
等のプリント配線板の基板などの電気絶縁板、化粧板等
の積層板の製造に用いられる紙、布等の繊維材からなる
シート状基材に樹脂液を含浸して得られるプリプレグの
製造方法及びその装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention comprises a fibrous material such as paper or cloth used for manufacturing an electric insulating board such as a substrate of a printed wiring board for industrial equipment or electronic equipment, or a laminated board such as a decorative board. The present invention relates to a method for manufacturing a prepreg obtained by impregnating a sheet-shaped base material with a resin liquid and an apparatus for the same.

【0002】[0002]

【従来の技術】従来、繊維材からなるシート状基材に樹
脂液を含浸させる場合、シート状基材を樹脂液に浸漬さ
せ、樹脂液中に通して樹脂液をシート状基材に含浸させ
る操作がおこなわれるが、この時シート状基材の繊維質
内の気泡が抜けず、プリプレグ内に気泡が残存したまま
であるのが普通であるため、このプリプレグを積層して
得られる積層板にボイドが発生していることが多い。ボ
イドが発生せず、電気特性や外観が損われないようにす
るためには高い圧力で積層成形することが必要である。
しかしながら、このように高い圧力で積層成形して得ら
れた電気絶縁板、化粧板等の積層板は寸法安定性が悪く
なったり、積層板に反りやねじれを発生させるという問
題がある。
2. Description of the Related Art Conventionally, when a sheet-shaped base material made of a fibrous material is impregnated with a resin liquid, the sheet-shaped base material is immersed in the resin liquid and passed through the resin liquid to impregnate the sheet-shaped base material with the resin liquid. The operation is performed, but at this time it is normal that the air bubbles in the fibrous material of the sheet-shaped substrate do not escape and the air bubbles remain in the prepreg. Voids are often generated. In order to prevent generation of voids and deterioration of electrical characteristics and appearance, it is necessary to carry out lamination molding at high pressure.
However, a laminated plate such as an electric insulating plate and a decorative plate obtained by laminating and molding at such a high pressure has problems that the dimensional stability is deteriorated and that the laminated plate is warped or twisted.

【0003】寸法安定性に優れ、反りやねじれの小さい
積層板を得るには低い圧力で積層成形する必要がある
が、このように低い圧力で積層成形するには積層板にボ
イドが生じないように気泡の残存がほとんどないプリプ
レグを用いることが必要である。気泡の残存がほとんど
ないプリプレグを得る方法としては、シート状基材を樹
脂液中に長時間(約10分以上)浸漬させて樹脂液がシ
ート状基材の繊維材内まで含浸させる方法があるが、生
産能率が極めて悪く、設備も長大化する等、非実用的で
ある。特に高濃度樹脂液の場合には不可能に近い。ま
た、樹脂液を満たした樹脂含浸槽に超音波発振装置を付
設し、樹脂液を超音波振動させることにより基材と樹脂
液の振動によってシート状基材に対する樹脂液の含浸性
を高める方法が提案されているが、超音波振動により樹
脂液が高温となり、樹脂液中の溶剤が気化するため、樹
脂液の粘度が急激に上昇し、含浸性を低下させてしまう
こととなる。これを防ぐために、常時溶剤を添加して樹
脂液を一定の濃度に保つ必要が生ずるが、粘度調整装置
が必要であること、更には溶剤添加によりコストが高く
なる問題がある。
In order to obtain a laminated plate having excellent dimensional stability and small warpage and twist, it is necessary to carry out laminating and molding at a low pressure. However, when laminating and molding at such a low pressure, voids do not occur in the laminated plate. It is necessary to use a prepreg in which almost no air bubbles remain. As a method of obtaining a prepreg in which almost no air bubbles remain, there is a method of immersing a sheet-shaped base material in a resin liquid for a long time (about 10 minutes or more) to impregnate the resin liquid into the fiber material of the sheet-shaped base material. However, it is impractical because the production efficiency is extremely poor and the equipment is lengthened. Especially in the case of high-concentration resin liquid, it is almost impossible. Further, there is a method in which an ultrasonic oscillator is attached to a resin impregnation tank filled with a resin liquid, and the resin liquid is ultrasonically vibrated to increase the impregnation property of the resin liquid into the sheet-shaped substrate due to the vibration of the substrate and the resin liquid. Although proposed, ultrasonic vibration causes the temperature of the resin liquid to rise and the solvent in the resin liquid evaporates, so that the viscosity of the resin liquid sharply increases and the impregnation property is deteriorated. In order to prevent this, it is necessary to constantly add a solvent to keep the resin liquid at a constant concentration, but there is a problem that a viscosity adjusting device is required and that the addition of a solvent increases the cost.

【0004】[0004]

【発明が解決しようとする課題】本発明は、従来のプリ
プレグ製造方法では高濃度樹脂液を繊維材からなるシー
ト状基材に含浸させると繊維材内に多量の気泡が残存し
たプリプレグとなる問題点を解決するため種々の検討の
結果なされたもので、その目的とするところはシート状
基材の繊維材への樹脂液の含浸を向上させ、かつ均一に
行い得ることにより、高濃度樹脂液を使用した場合でも
繊維材からなるシート状基材中の気泡が極めて少ないプ
リプレグを得る樹脂液含浸方法と、これを最適に実施す
る装置を提供することにある。
SUMMARY OF THE INVENTION According to the present invention, in the conventional prepreg manufacturing method, when a sheet-shaped base material made of a fiber material is impregnated with a high-concentration resin liquid, a large amount of air bubbles remain in the fiber material. It was made as a result of various investigations in order to solve the problem, and the purpose is to improve the impregnation of the resin liquid into the fiber material of the sheet-shaped base material and to perform it uniformly, thereby making it possible to obtain a high-concentration resin liquid. It is an object of the present invention to provide a resin liquid impregnation method for obtaining a prepreg having extremely few air bubbles in a sheet-shaped substrate made of a fibrous material even when the above method is used, and an apparatus for optimally implementing the method.

【0005】[0005]

【課題を解決するための手段】本発明は、繊維材よりな
るシート状基材に樹脂液を含浸させ、しかる後これを乾
燥させることによってプリプレグを製造するにあたり、
前記シート状基材の片面側に樹脂液を塗布した後、まず
樹脂液に使用した溶剤の沸点より低い温度で樹脂液を塗
布した面の反対面側より加熱し、しかる後前記溶剤の沸
点より高い温度で加熱乾燥することを特徴とするプリプ
レグの製造方法、に関するものである。 即ち、本発明のプリプレグ製造方法は繊維材からなるシ
ート状基材の片面側に樹脂液を塗布する塗布工程、該工
程を経たシート状基材を加温することにより、樹脂液を
低粘度化し、シート状基材の繊維質内部まで含浸させる
加熱工程、及び樹脂液中に含まれる溶剤を気化させると
ともに、樹脂を半硬化の状態にする加熱乾燥工程を必須
工程とするものである。
Means for Solving the Problems In the present invention, when a sheet-like base material made of a fiber material is impregnated with a resin liquid and then dried, a prepreg is produced.
After applying the resin liquid on one side of the sheet-shaped substrate, first heat from the opposite side of the surface coated with the resin liquid at a temperature lower than the boiling point of the solvent used for the resin liquid, and then from the boiling point of the solvent. The present invention relates to a method for producing a prepreg, which comprises heating and drying at a high temperature. That is, the prepreg manufacturing method of the present invention is a coating step of applying a resin liquid on one side of a sheet-shaped base material made of a fibrous material, by heating the sheet-shaped base material that has undergone the step, to reduce the viscosity of the resin liquid. The heating step of impregnating the inside of the fibrous material of the sheet-shaped substrate and the heating and drying step of vaporizing the solvent contained in the resin liquid and making the resin semi-cured are indispensable steps.

【0006】さらに、繊維材からなるシート状基材及び
これに使用する樹脂液の種類、性状によっては、シート
状基材の片面側に塗布する工程だけでは樹脂の付着量が
所定の量に満たない場合がある。この場合は加熱乾燥工
程後に連続して樹脂付着量を調整する為の付着量調整工
程を加え、次いで始めに塗布した樹脂液と付着量調整の
ための樹脂液を加熱乾燥する加熱乾燥工程を設けること
が好ましい。樹脂付着量調整工程は最初に樹脂液を含浸
するために塗布した面と異なる他の一方の面だけでも、
或いは両面からでもよく、シート状基材及び含浸させる
樹脂液の種類、性状及び得ようとするプリプレグの要求
品質により選択することができるが、装置の費用、両面
の付着量のバランスを考慮した場合、前者の方が好まし
い。なお、樹脂付着量調整工程はその前の工程と連続し
ている必要はなく、一且巻取った後、時間を経て実施し
ても良いが、巻取りの為の装置及び工数が必要となるの
で好ましくはない。
Further, depending on the type and properties of the sheet-shaped base material made of the fibrous material and the resin liquid used for the sheet-shaped base material, the amount of resin adhering to the predetermined amount can be satisfied only by the step of applying it to one side of the sheet-shaped base material. May not be. In this case, after the heating / drying step, a deposition amount adjusting step for continuously adjusting the resin deposition amount is added, and then a heating drying step for heating and drying the applied resin liquid and the resin liquid for adjusting the deposition amount is provided. It is preferable. In the resin adhesion amount adjustment process, even if only one other surface different from the surface applied to impregnate the resin liquid at the beginning,
Alternatively, it may be selected from both sides, and it can be selected depending on the type and properties of the sheet-shaped base material and the resin liquid to be impregnated and the required quality of the prepreg to be obtained, but when considering the cost of the device and the balance of the amount of adhesion on both sides. The former is preferable. It should be noted that the resin adhesion amount adjusting step does not have to be continuous with the preceding step, and may be carried out after a certain time after winding once, but a winding device and man-hours are required. Therefore, it is not preferable.

【0007】一方、かかる方法を実施するための本発明
のプリプレグ製造装置は、繊維材からなるシート状基材
に樹脂液を片面から塗布する装置、樹脂液が含浸したシ
ート状基材を樹脂液が塗布された面の反対面側より加熱
する装置、及び樹脂液が含浸したシート状基材を加熱乾
燥する装置を順次通過するように構成し、使用するシー
ト状基材及び含浸させる樹脂液の種類、性状等によって
は、更に樹脂量調整装置を、乾燥装置の前に設置したプ
リプレグの製造装置である。
On the other hand, the prepreg manufacturing apparatus of the present invention for carrying out such a method is an apparatus for applying a resin liquid to a sheet-shaped base material made of a fiber material from one side, and a sheet-shaped base material impregnated with the resin liquid for the resin liquid. Of the sheet-shaped substrate to be used and the resin liquid to be impregnated, which is configured to sequentially pass through a device for heating from the side opposite to the surface coated with and a device for heating and drying the sheet-shaped substrate impregnated with the resin liquid. Depending on the type and properties, it is a prepreg manufacturing apparatus in which a resin amount adjusting device is further installed in front of the drying device.

【0008】本発明に用いる繊維材よりなるシート状基
材としては、ガラスクロス、ガラス不繊布、ガラスペー
パー等のガラス繊維基材の他、紙、合成繊維等からなる
織布や、不織布、金属繊維、カーボン繊維からなる織布
やマット類等が挙げられ、これらの基材の原料は単独又
は混合して使用してもよい。これらのシート状基材に樹
脂液を含浸・乾燥してプリプレグを製造する。本発明に
用いる樹脂液としては、一般的に、エポキシ樹脂、ポリ
イミド樹脂、およびこれらの変性樹脂が好ましく使用さ
れるが、その他、熱可塑性樹脂、天然樹脂等の樹脂も使
用される。それらに限定されるものではない。また、充
填材、着色剤、補強材を配合することができ、水酸化ア
ルミニウム、シリカ、タルク、炭酸カルシウム等も本発
明の目的に反しない範囲において、必要により適宜配合
することができる。
Examples of the sheet-like base material made of the fiber material used in the present invention include glass fiber base materials such as glass cloth, glass non-woven cloth and glass paper, as well as woven cloth, non-woven cloth and metal made of paper, synthetic fiber and the like. Examples thereof include woven fabrics and mats made of fibers and carbon fibers, and the raw materials for these base materials may be used alone or as a mixture. A resin liquid is impregnated into these sheet-shaped base materials and dried to produce a prepreg. As the resin liquid used in the present invention, generally, an epoxy resin, a polyimide resin, and a modified resin thereof are preferably used, but other resins such as a thermoplastic resin and a natural resin are also used. It is not limited to them. Further, a filler, a colorant and a reinforcing material can be blended, and aluminum hydroxide, silica, talc, calcium carbonate and the like can also be blended appropriately as necessary within the range not deviating from the object of the present invention.

【0009】こうして得られた樹脂液は繊維材よりなる
シート状基材に含浸しやすいように溶剤を混合して粘度
調整されている。一般的には固形分50%前後に調整し
て含浸槽に貯溜し、シート状基材をこの樹脂液中を通過
させることにより、繊維材中の空気と樹脂液の置換を行
い、含浸を行っている。固形分55%を越えると樹脂液
の粘度が高くなり繊維材への樹脂液の含浸性が低下し、
繊維材中の空気との置換が行われにくく、気泡が十分に
抜けないまま乾燥され、気泡が多く残存したプリプレグ
が得られることとなる。通常、固形分が高くなっても樹
脂液を加温し、粘度を下げる処理が行われるが、樹脂液
中に低溶点溶剤が含まれている場合には、溶剤が徐々に
気化し、含浸槽での塗布条件の管理が難しくなる。その
ため高沸点溶剤を使用して、沸点以下で加温する方法が
とられているが、必要以上に高温化すると溶剤が蒸発し
易くなるので、一般的には常温から40℃程度で加温さ
れる。この条件下でも溶剤は徐々に気化し、高濃度化、
高粘度化となる為、樹脂液の濃度管理、粘度管理装置を
付設し、溶剤を適宜添加することが行われている。これ
は高濃度樹脂液を使用することによる原材料コストの低
減を図るという目的に反するものである。本発明は固形
分55%以上の樹脂液を使用しても従来の低濃度の樹脂
液を使用した場合と同等以上の含浸性を有し、乾燥工程
を経てもボイドの少ないプリプレグを提供するものであ
る。
The resin liquid thus obtained is mixed with a solvent to adjust its viscosity so that it can be easily impregnated into a sheet-like base material made of a fibrous material. Generally, the solid content is adjusted to about 50% and stored in an impregnation tank, and the air in the fiber material is replaced with the resin solution by passing the sheet-shaped base material through the resin solution to perform impregnation. ing. If the solid content exceeds 55%, the viscosity of the resin liquid becomes high and the impregnating property of the resin liquid into the fiber material decreases,
It is difficult to replace the air in the fibrous material, and the prepreg can be obtained in which air bubbles are dried without being sufficiently removed, and a large amount of air bubbles remain. Usually, even if the solid content becomes high, the resin liquid is heated to reduce the viscosity.However, if the resin liquid contains a low melting point solvent, the solvent gradually evaporates and impregnates. It becomes difficult to control the application conditions in the bath. Therefore, a method of heating at a temperature below the boiling point using a high-boiling solvent is used, but if the temperature is raised more than necessary, the solvent will easily evaporate. It Even under these conditions, the solvent gradually evaporates, increasing the concentration,
In order to increase the viscosity, a resin liquid concentration control device and a viscosity control device are attached and a solvent is appropriately added. This is contrary to the purpose of reducing the cost of raw materials by using a high concentration resin liquid. INDUSTRIAL APPLICABILITY The present invention provides a prepreg which has the same or higher impregnation property as when a resin liquid having a solid content of 55% or more is used and which has the same or better impregnation as when a resin liquid having a conventional low concentration is used. Is.

【0010】以下、本発明の工程を順次説明する。 (樹脂液塗布工程)高濃度樹脂液を含浸槽に貯溜するの
ではなく、シート状基材に必要量を供給し、片面側より
塗布することにより、樹脂液からの溶剤の揮発を抑え、
高濃度樹脂液を一定の濃度・粘度に保持することが出来
る。
The steps of the present invention will be sequentially described below. (Resin liquid coating step) Instead of storing the high-concentration resin liquid in the impregnation tank, by supplying a necessary amount to the sheet-shaped substrate and applying from one side, the volatilization of the solvent from the resin liquid is suppressed,
High-concentration resin liquid can be maintained at a constant concentration and viscosity.

【0011】(加熱工程)高濃度樹脂液を塗布されたシ
ート状基材を加温することにより、樹脂液を低粘度化さ
せ、繊維材中の空気との置換を容易に行わしめる工程で
ある。樹脂液に使用している溶剤の沸点より高い温度で
加熱すると溶剤の突沸により、急激な高濃度化が起り樹
脂液の含浸性が極端に低下するとともに脱泡ができずに
樹脂中に多量の発泡が生ずることとなる。この問題を解
決するためには樹脂液に使用している溶剤の沸点より低
い温度で加温することが必要である。さらには樹脂液を
塗布した面より加熱するとシート状基材より先に樹脂液
の温度が上昇するため、樹脂液が低粘度化してもシート
状基材の方が低温のために、樹脂液の温度を下げ、低粘
度化を妨げることとなり、含浸性を低下させることとな
るので好ましくない。この為、シート状基材の樹脂液を
塗布した面の反対面側より加熱する方が、含浸性をより
向上させることとなる。両面より加熱してもよいが、そ
の効果は前述の樹脂液を塗布した面の反対面側より加熱
する方法よりも少ない事は明らかである。
(Heating step) This is a step of heating the sheet-shaped base material coated with the high-concentration resin liquid to reduce the viscosity of the resin liquid and easily replace the air in the fiber material. . When heated at a temperature higher than the boiling point of the solvent used for the resin liquid, sudden concentration increase occurs due to the sudden boiling of the solvent, impregnating property of the resin liquid is extremely lowered, and defoaming is not possible and a large amount of the resin liquid is not formed. Foaming will occur. In order to solve this problem, it is necessary to heat at a temperature lower than the boiling point of the solvent used in the resin liquid. Furthermore, when heating from the surface coated with the resin liquid, the temperature of the resin liquid rises before that of the sheet-shaped substrate, so even if the resin liquid has a low viscosity, the sheet-shaped substrate has a lower temperature. This is not preferable because it lowers the temperature, hinders lowering of the viscosity, and lowers the impregnating property. Therefore, heating the sheet-shaped base material from the side opposite to the surface coated with the resin liquid improves the impregnation property. It may be heated from both sides, but it is clear that the effect is less than that of the method of heating from the side opposite to the side coated with the resin liquid.

【0012】樹脂液に使用する溶剤は高沸点のものが好
ましいが、160℃を越えるものについては後の加熱乾
燥工程で、樹脂液中に含まれる溶剤を気化させるととも
に樹脂を半硬化の状態にさせる為に高エネルギーが必要
となるので好ましくない。沸点が70℃以下の溶剤につ
いてはシート状基材に塗布した後、常温下でも徐々に気
化するとともに、突沸をさけるために加熱する温度を5
0%以下にしなければならないが、加温温度が低くなる
と樹脂液の低粘度化も小さく、繊維材への含浸性も不十
分となり好ましくない。従って、好ましくは沸点が70
℃〜160℃の単独、或は2種以上混合したものを使用
する。
The solvent used for the resin liquid preferably has a high boiling point, but for those having a temperature of higher than 160 ° C., the solvent contained in the resin liquid is vaporized and the resin is semi-cured in the subsequent heat drying step. High energy is required for this purpose, which is not preferable. For solvents with a boiling point of 70 ° C or less, after being applied to a sheet-shaped substrate, the solvent is gradually vaporized even at room temperature, and the heating temperature is 5 to avoid bumping.
Although it must be 0% or less, when the heating temperature is low, the viscosity of the resin liquid is not lowered so much and the impregnation property into the fiber material is insufficient, which is not preferable. Therefore, the boiling point is preferably 70
C. to 160.degree. C. are used alone or as a mixture of two or more.

【0013】(加熱乾燥工程)樹脂液に使用している溶
剤の沸点より高い温度で加熱乾燥させることにより、樹
脂液中の溶剤を気化させるとともに、樹脂を半硬化の状
態にしたプリプレグを得ることができるる。加熱乾燥方
式は従来より実施されている方式を用いればよく、特に
限定されるものではない。
(Heating and drying step) By heating and drying at a temperature higher than the boiling point of the solvent used in the resin liquid, the solvent in the resin liquid is vaporized and a prepreg in which the resin is semi-cured is obtained. You can The heating and drying method may be a conventionally used method and is not particularly limited.

【0014】[0014]

【実施例】以下、図1〜2に基づいて実施例を説明す
る。しかしながら、本発明はこれらの実施例によって限
定されるものではない。
EXAMPLES Examples will be described below with reference to FIGS. However, the present invention is not limited by these examples.

【0015】《実施例1》46g/m2 のガラスクロス
1を3m/分の速度で巻出し、ガイドロール8aを経
て、支持台4bとコーターロール或いはドクターナイフ
等のコーター4aよりなる塗布装置4に移送する。コー
ターの上面側にノズル等の樹脂液供給装置2を使用して
毎分約124gの量で下記のエポキシ樹脂液3aを塗布
する。支持台4bとコーターロール或いはドクターナイ
フ等のコーター4aのギャップは予め10.2mmに調
整してある。
Example 1 A glass cloth 1 of 46 g / m 2 was unwound at a speed of 3 m / min, passed through a guide roll 8 a, a support 4 b and a coater roll or a coater 4 a such as a doctor knife. Transfer to. The following epoxy resin liquid 3a is applied to the upper surface side of the coater using a resin liquid supply device 2 such as a nozzle at an amount of about 124 g per minute. The gap between the support 4b and the coater 4a such as a coater roll or a doctor knife is adjusted to 10.2 mm in advance.

【0016】片面側に樹脂液を塗布されたガラスクロス
1は直ちに加熱装置5に移送し、下面側より雰囲気温度
120℃の熱風によって約1分間加温した後、加熱乾燥
装置6にてその両面を180℃の雰囲気温度で約1分間
加熱乾燥し、樹脂量約61.5%のプリプレグを得た。 〈樹脂液組成〉 樹脂(粘稠液) エポキシ樹脂 153.6重量部 溶剤 ジメチルホルムアミド 98.6 硬化剤 ジシアンジアミド 3.5 促進剤 イミダゾール 0.15 樹脂液固形分 約61.5% (ジメチルホルムアミドの沸点:153℃)
The glass cloth 1 coated with the resin liquid on one surface side is immediately transferred to the heating device 5 and heated from the lower surface side by hot air having an ambient temperature of 120 ° C. for about 1 minute, and then both surfaces are heated and dried by the heating and drying device 6. Was heated and dried at an ambient temperature of 180 ° C. for about 1 minute to obtain a prepreg having a resin amount of about 61.5%. <Resin liquid composition> Resin (viscous liquid) Epoxy resin 153.6 parts by weight Solvent Dimethylformamide 98.6 Curing agent Dicyandiamide 3.5 Accelerator imidazole 0.15 Resin liquid solid content about 61.5% (boiling point of dimethylformamide 153 ° C)

【0017】《実施例2》この実施例では、21.0g
/m2 のガラスクロスの場合を示す。実施例1と同じく
3m/分の速度で塗布装置4に移送し、ガラスクロスの
上面側に上表に示すエポキシ樹脂液3aを毎分約214
gの量で塗布する。この時の支持台4bとコーターロー
ル或いはドクターナイフ等のコーター4aとのギャップ
は予め0.32mmに調整してある。
Example 2 In this example, 21.0 g
/ M 2 of glass cloth is shown. The epoxy resin liquid 3a shown in the above table was transferred to the coating device 4 at a speed of 3 m / min in the same manner as in Example 1, and the epoxy resin liquid 3a shown in the above table was applied at a rate of about 214 per minute on the upper surface side of the glass cloth.
It is applied in the amount of g. At this time, the gap between the support base 4b and the coater 4a such as a coater roll or a doctor knife is adjusted to 0.32 mm in advance.

【0018】片面側に樹脂液を塗布したガラスクロス1
は直ちに加熱装置5に移送し、下面側より雰囲気温度1
20℃の熱風によって約1分30秒間加温した後、押え
ロール7a,7bと回転ロール7cよりなる樹脂付着量
調整装置7で下面側に毎分約38gの量でエポキシ樹脂
液3bを塗布する。樹脂液槽7d内のエポキシ樹脂液3
bは最初に塗布するエポキシ樹脂液3aと同一のもので
もよいし、また異なるものでもよく、必要に応じて適宜
に選択される。その後加熱乾燥装置6にて両面を180
℃の雰囲気温度で約2分間乾燥して樹脂量約42.4%
のプリプレグを得た。
A glass cloth 1 coated with a resin solution on one side
Is immediately transferred to the heating device 5, and the ambient temperature 1
After heating with hot air at 20 ° C. for about 1 minute and 30 seconds, the epoxy resin liquid 3b is applied to the lower surface side with the resin adhesion amount adjusting device 7 including the pressing rolls 7a and 7b and the rotating roll 7c at an amount of about 38 g per minute. . Epoxy resin liquid 3 in resin liquid tank 7d
b may be the same as or different from the epoxy resin liquid 3a to be applied first, and may be appropriately selected as needed. After that, 180 on both sides with the heating and drying device 6.
Drying at ambient temperature of ℃ for about 2 minutes, resin amount about 42.4%
Prepreg was obtained.

【0019】上記実施例1及び2のプリプレグについて
50倍の顕微鏡で観察してプリプレグ中の気泡の有無を
調べた結果、いずれもボイドの数は極く僅かであり、同
一組成のエポキシ樹脂液を使って通常の含浸方法で得ら
れたプリプレグに比べ格段にボイドの数が少なかった。
As a result of observing the prepregs of Examples 1 and 2 under a microscope of 50 times for presence or absence of air bubbles in the prepreg, the number of voids was very small in both cases, and epoxy resin solutions of the same composition were used. The number of voids was significantly smaller than that of the prepreg obtained by the usual impregnation method.

【0020】[0020]

【発明の効果】本発明の方法に従い、繊維材からなるシ
ート状基材の片面側に樹脂液を塗布した後、樹脂液に使
用した溶剤の沸点より低い温度で樹脂液を塗布した面と
異なる他方の面より加熱することにより樹脂液中の溶剤
の気化を抑えた状態で樹脂液を低粘度化することにより
繊維材への樹脂液を良好に含浸させることができるもの
であり、気泡の極めて少ないプリプレグを得ることがで
きるものである。しかも従来のように必ずしも竪型乾燥
機を使用する必要もなく、横型乾燥機も使用でき設備投
資額を抑えることができる。
According to the method of the present invention, after the resin liquid is applied to one side of the sheet-like base material made of the fibrous material, it is different from the surface applied with the resin liquid at a temperature lower than the boiling point of the solvent used for the resin liquid. By heating from the other side, it is possible to satisfactorily impregnate the resin liquid into the fiber material by lowering the viscosity of the resin liquid while suppressing vaporization of the solvent in the resin liquid, and it is extremely It is possible to obtain a small amount of prepreg. Moreover, it is not always necessary to use a vertical dryer as in the conventional case, and a horizontal dryer can also be used, and the capital investment can be suppressed.

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

【図1】 本発明の一実施例を示す概略側面図。FIG. 1 is a schematic side view showing one embodiment of the present invention.

【図2】 本発明の他の実施例を示す概略側図。FIG. 2 is a schematic side view showing another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 シート状基材 2 樹脂液供給装置 3a,3b 樹脂液 4 塗布装置 5 加熱装置 6 加熱乾燥装置 7 樹脂付着量調整装置 8a,8b ガイドロール 7a,7b 押えロール 7c 回転ロール 7d 樹脂液槽 1 Sheet-shaped substrate 2 Resin liquid supply device 3a, 3b Resin liquid 4 Coating device 5 Heating device 6 Heating / drying device 7 Resin adhesion amount adjusting device 8a, 8b Guide roll 7a, 7b Pressing roll 7c Rotating roll 7d Resin liquid tank

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B29K 105:08 309:08 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display location B29K 105: 08 309: 08

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 繊維材よりなるシート状基材に樹脂液を
含浸させ、しかる後これを乾燥させることによってプリ
プレグを製造するにあたり、前記シート状基材の片面側
に樹脂液を塗布した後、まず樹脂液に使用した溶剤の沸
点より低い温度で樹脂液を塗布した面の反対面側より加
熱し、しかる後前記溶剤の沸点より高い温度で加熱乾燥
することを特徴とするプリプレグの製造方法。
1. When a prepreg is manufactured by impregnating a sheet-shaped base material made of a fibrous material with a resin liquid and then drying the prepreg, a resin liquid is applied to one surface side of the sheet-shaped base material, First, a method for producing a prepreg, which comprises heating at a temperature lower than the boiling point of the solvent used for the resin liquid from the side opposite to the surface coated with the resin liquid, and then heating and drying at a temperature higher than the boiling point of the solvent.
【請求項2】 繊維材よりなるシート状基材に樹脂液を
含浸させ、しかる後これを乾燥させることによってプリ
プレグを製造するにあたり、前記シート状基材の片面側
に樹脂液を塗布した後、まず樹脂液に使用した溶剤の沸
点より低い温度で樹脂液を塗布した面の反対面側より加
熱し、しかる後、樹脂液を塗布した面の反対面に樹脂液
を塗布し、さらに樹脂液に使用された溶剤の沸点より高
い温度で加熱乾燥することを特徴とするプリプレグの製
造方法。
2. When a prepreg is manufactured by impregnating a sheet-like base material made of a fibrous material with a resin liquid and then drying the prepreg, a resin liquid is applied to one side of the sheet-like base material, First, heat at a temperature lower than the boiling point of the solvent used for the resin liquid from the opposite side of the surface coated with the resin liquid, and then apply the resin liquid to the opposite surface of the surface coated with the resin liquid, and further to the resin liquid. A method for producing a prepreg, which comprises heating and drying at a temperature higher than the boiling point of the solvent used.
【請求項3】 繊維材よりなるシート状基材の片面側に
樹脂液を塗布する装置と、片面側に樹脂液が塗布された
シート状基材を樹脂液が塗布された面の反対面側より加
熱する加熱装置と、樹脂液が塗布されたシート状基材が
通過する加熱乾燥装置とを具備したことを特徴とするプ
リプレグの製造装置。
3. An apparatus for applying a resin liquid to one surface side of a sheet-shaped base material made of a fibrous material, and a sheet-shaped base material having the resin liquid applied to one surface side opposite to the surface coated with the resin liquid. An apparatus for producing a prepreg, comprising: a heating device for further heating; and a heating / drying device through which a sheet-shaped substrate coated with a resin liquid passes.
【請求項4】 繊維材よりなるシート状基材の片面側に
樹脂液を塗布する装置と、片面側に樹脂液が塗布された
シート状基材を樹脂液が塗布された面の反対面側より加
熱する加熱装置と、樹脂液が含浸したシート状基材の樹
脂付着量を調整するため、最初に樹脂液を塗布した面の
反対面に樹脂液を付着させる樹脂付着量調整装置と、樹
脂液が塗布されたシート状基材が通過する加熱乾燥装置
とを具備したことを特徴とするプリプレグの製造装置。
4. An apparatus for applying a resin liquid to one side of a sheet-shaped base material made of a fibrous material, and a sheet-shaped base material having a resin liquid applied to one surface side opposite to the surface coated with the resin liquid. A heating device for further heating, and a resin adhesion amount adjusting device for adhering the resin liquid to the opposite surface of the surface first coated with the resin liquid in order to adjust the resin adhesion amount of the sheet-shaped substrate impregnated with the resin liquid, and the resin An apparatus for producing a prepreg, comprising: a heating / drying apparatus through which a sheet-shaped substrate coated with the liquid passes.
JP31697995A 1995-12-05 1995-12-05 Prepreg manufacturing method and manufacturing apparatus Expired - Fee Related JP3150591B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31697995A JP3150591B2 (en) 1995-12-05 1995-12-05 Prepreg manufacturing method and manufacturing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31697995A JP3150591B2 (en) 1995-12-05 1995-12-05 Prepreg manufacturing method and manufacturing apparatus

Publications (2)

Publication Number Publication Date
JPH09157415A true JPH09157415A (en) 1997-06-17
JP3150591B2 JP3150591B2 (en) 2001-03-26

Family

ID=18083074

Family Applications (1)

Application Number Title Priority Date Filing Date
JP31697995A Expired - Fee Related JP3150591B2 (en) 1995-12-05 1995-12-05 Prepreg manufacturing method and manufacturing apparatus

Country Status (1)

Country Link
JP (1) JP3150591B2 (en)

Also Published As

Publication number Publication date
JP3150591B2 (en) 2001-03-26

Similar Documents

Publication Publication Date Title
EP0476752B2 (en) Process and apparatus for resin impregnation of a fibrous substrate
JPH09225938A (en) Method and device for manufacturing prepreg
JP3150591B2 (en) Prepreg manufacturing method and manufacturing apparatus
JPS5857446B2 (en) Resin-impregnated base material and its manufacturing method
JPH0160404B2 (en)
JPH09235395A (en) Impregnation of resin liquid and apparatus for impregnation resin liquid
JP2611584B2 (en) Manufacturing method of prepreg
JP3685125B2 (en) Manufacturing method of prepreg
JPH09176341A (en) Impregnation of resin liquid and device for impregnating resin liquid
JPH11156851A (en) Production of prepreg
JPH07214554A (en) Method and apparatus for preparing preparing
JPH10139898A (en) Production of prepreg and production apparatus
JPH08174549A (en) Production of prepreg
JPS6339404B2 (en)
JP5113964B2 (en) Resin impregnation method and apparatus
JPS6083814A (en) Preparation of prepreg
JPS62108009A (en) Preparation of prepreg
JPH05318483A (en) Manufacture of prepreg for laminate and its device
JP3582770B2 (en) Manufacturing method of laminated board
JP2003001630A (en) Method for impregnation with resin
JPH05318476A (en) Manufacture of prepreg for laminate and its device
JPH07290453A (en) Resin impregnation method and apparatus
JP2001213979A (en) Manufacturing method of prepreg
JP2002037901A (en) Method for producing prepreg
JPH10324755A (en) Resin impregnated substrate, its production, laminated sheet and its production

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees