JPH09225938A - Method and device for manufacturing prepreg - Google Patents

Method and device for manufacturing prepreg

Info

Publication number
JPH09225938A
JPH09225938A JP3690196A JP3690196A JPH09225938A JP H09225938 A JPH09225938 A JP H09225938A JP 3690196 A JP3690196 A JP 3690196A JP 3690196 A JP3690196 A JP 3690196A JP H09225938 A JPH09225938 A JP H09225938A
Authority
JP
Japan
Prior art keywords
resin liquid
sheet
resin
heating
prepreg
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.)
Pending
Application number
JP3690196A
Other languages
Japanese (ja)
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 JP3690196A priority Critical patent/JPH09225938A/en
Publication of JPH09225938A publication Critical patent/JPH09225938A/en
Pending legal-status Critical Current

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  • Application Of Or Painting With Fluid Materials (AREA)
  • Reinforced Plastic Materials (AREA)

Abstract

PROBLEM TO BE SOLVED: To impregnate a fiber material with a resin liquid in a good manner and manufacture a material with extremely small number of foams by applying the resin liquid on one face side of a sheet-shaped base, heating the base from the opposite face side at the temperature lower than the boiling point of a solvent used for the resin liquid and then heat drying the resin impregnated sheet-shaped base. SOLUTION: A sheet-shaped base, for example, a glass cloth 1 is unwound, passed through a guide roll 8a and transferred to a coating device 4 formed of a supporting stand 4b and a coater 4a such as a coater roll or a doctor knife. Then a resin liquid feed device 2 such as a nozzle is used on the upper face side of the coater 4a, and a resin liquid, for example, an epoxy resin liquid 3a is applied. The glass cloth 1 with one face side coated with the resin liquid 3a is transferred immediately to a heating device 5, and heated by hot air of atmospheric temperature lower than the boiling point of a solvent used for the resin liquid 3a from the lower side face, and then both faces of the glass cloth are heat dried by the given atmospheric temperature by a heat drying device 6 to manufacture a 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間
にある気泡が抜けず、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 common that the air bubbles between the fibers 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分間以上)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) so that the resin liquid is impregnated into the fiber material of the sheet-shaped base material. But,
It is impractical because the production efficiency is extremely poor and the equipment becomes long. 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(例えば、55重量%
以上)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 The present invention provides a high-concentration resin liquid (for example, 55% by weight) in the conventional prepreg manufacturing method.
When the above-mentioned) is impregnated into a sheet-like base material made of a fibrous material, various examinations have been made in order to solve the problem that a large amount of air bubbles remain in the fibrous material, resulting in a prepreg. By improving the impregnation of the resin material into the fibrous material of the sheet-shaped base material and performing it uniformly, a prepreg with very few bubbles in the sheet-shaped base material made of the fibrous material even when a high-concentration resin liquid is used. It is to provide a resin liquid impregnation method to be obtained 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おいて、
前記シート状基材の片面側に樹脂液を塗布した後、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
るために、樹脂液に使用している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温し、しかる
後樹脂液中に含まれる溶剤を気化させるとともに、必要
により樹脂を半硬化の状態にするために樹脂含浸シート
状基材を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
加温する加温工程、及び加熱乾燥工程を必須工程とする
ものである。
According to the present invention, a sheet-like base material made of a fibrous material is impregnated with a resin liquid and then dried to produce a prepreg.
After coating the resin liquid on one side of the sheet-shaped substrate, in order to lower the viscosity of the resin liquid and to impregnate the inside of the fibrous material of the sheet-shaped substrate, at a temperature lower than the boiling point of the solvent used for the resin liquid. The resin-impregnated sheet-shaped substrate is heated and dried by heating from the side opposite to the surface coated with the resin liquid and then evaporating the solvent contained in the resin liquid and, if necessary, semi-curing the resin. The present invention relates to a method for manufacturing a prepreg, which comprises: That is, the prepreg manufacturing method of the present invention comprises a coating step of applying a resin liquid on one side of a sheet-shaped base material made of a fibrous material, a heating step of heating the sheet-shaped base material that has gone through the step, and a heating / drying step. This is an essential step.

【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。この場合は加温工程後
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、通常始めに塗布した樹脂液と付着量調整
のために塗布した樹脂液を加熱乾燥する加熱乾燥工程を
設ける。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は反対側の面だけでも、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 step, a coating amount adjustment step for continuously adjusting the resin coating amount is added, and then the resin liquid applied first and the resin liquid applied for adjusting the coating amount are heated and dried. Provide a drying process. The resin-adhesion-amount adjusting step may be performed only on the surface opposite to the surface applied to impregnate the resin liquid first, or from both surfaces. The prepreg can be selected according to the required quality, but the former is preferable in consideration of the cost of the apparatus and the balance of the amount of adhesion on both sides. In addition,
The resin adhesion amount adjusting step does not need to be continuous with the preceding step, and may be carried out after winding once, but it is preferable because a winding device and man-hours are required. There is no.

【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温
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、加熱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. The sheet-shaped substrate to be used and the resin liquid to be impregnated, which are configured so as 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 of the prepreg, a resin amount adjusting device is further installed in front of the heating and 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、加熱乾燥
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 better impregnation property as the case of using a conventional low-concentration resin liquid even when a resin liquid having a solid content of 55% or more is used, and has few voids even after a heating and drying step. It is a thing.

【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、含浸槽に貯溜しこ
れにシート状基材を浸漬するのではなく、必要量の樹脂
液をシート状基材に供給し、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。樹脂液の濃
度は、前述のように従来法では50重量%程度である
が、本発明においては、従来法と同じ程度でもよいが、
好ましくは55〜70%程度とする。このように高濃度
とすることにより溶剤の量を減少させることができる。
The steps of the present invention will be sequentially described below. (Resin liquid coating process) High-concentration resin liquid is not stored in the impregnation tank and the sheet-shaped substrate is immersed in it, but the required amount of resin liquid is supplied to the sheet-shaped substrate and applied from one side. By this, volatilization of the solvent from the resin liquid can be suppressed, and the high-concentration resin liquid can be maintained at a constant concentration and viscosity. The concentration of the resin liquid is about 50% by weight in the conventional method as described above, but in the present invention, it may be the same as in the conventional method,
It is preferably about 55 to 70%. With such a high concentration, the amount of solvent can be reduced.

【0011】(加温工程)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せる工程であ
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。好ましくは溶剤の沸
点より20℃以上低い温度である。また、温度が低すぎ
ても低粘度化の効果が小さいので、最低50℃以上であ
ることが好ましい。さらには樹脂液を塗布した面より加
温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
面側より加温する方が、含浸性をより向上させることと
なる。両面より加温してもよいが、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温する方法よりも少
ないことは明らかである。
(Warming step) In the step of heating the sheet-shaped base material coated with the high-concentration resin liquid to lower the viscosity of the resin liquid and to easily replace the air in the fiber material. is there. 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. The temperature is preferably 20 ° C. or more lower than the boiling point of the solvent. Further, since the effect of lowering the viscosity is small even if the temperature is too low, it is preferably at least 50 ° C or higher. Furthermore, if the temperature of the resin liquid rises before the sheet-shaped substrate when heated from the surface coated with the resin liquid, the sheet-shaped substrate will still be at a lower temperature even if the resin liquid has a lower viscosity. This lowers the temperature and prevents the viscosity from decreasing and impairs the impregnating property, which is not preferable. Therefore, heating the sheet-shaped substrate from the side opposite to the surface coated with the resin liquid improves the impregnation property. It is possible to heat from both sides, but it is clear that the effect is less than in 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、さらに
は必要により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温す
る温度を50℃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、通常は沸点
が70〜160℃、好ましくは100〜160℃の溶剤
の単独あるいは2種以上混合したものを使用する。好ま
しい溶剤の具体例としては、ジメチルホルムアミド(沸
点153℃)、メチルイソブチルケトン(沸点116
℃)、キシレン(沸点140℃)、酢酸ブチル(沸点1
26℃)、プロピレングリコールモノメチルエーテル
(沸点120℃)等がある。
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 in the subsequent heating and drying step, and if necessary, the resin is semi-dried. High energy is required to bring the resin into a cured state, which is not preferable. For a solvent with a boiling point of 70 ° C or lower, after being applied to a sheet-shaped substrate, it must be gradually vaporized even at room temperature, and the heating temperature must be 50 ° C or lower to avoid bumping. When it becomes low, the viscosity of the resin liquid is not lowered so much and the impregnation property into the fiber material becomes insufficient, which is not preferable. Therefore, a solvent having a boiling point of 70 to 160 ° C., preferably 100 to 160 ° C. is usually used alone or as a mixture of two or more thereof. Specific examples of preferable solvents include dimethylformamide (boiling point: 153 ° C.) and methyl isobutyl ketone (boiling point: 116).
℃), xylene (boiling point 140 ℃), butyl acetate (boiling point 1
26 ° C.) and propylene glycol monomethyl ether (boiling point 120 ° C.).

【0013】(加熱乾燥工程)この工程は通常樹脂液に
使用している溶剤の沸点より高い温度で加熱乾燥するこ
とにより樹脂液中の溶剤を気化させ、さらには必要によ
り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。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) In this step, the solvent in the resin liquid is vaporized by heating and drying at a temperature higher than the boiling point of the solvent usually used for the resin liquid, and if necessary, the resin is in a semi-cured state. It is possible to obtain a prepreg made of 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及び図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。
An embodiment 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に移送した。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
約124g/m2 の量で下記のエポキシ樹脂液3aを塗
布した。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0.2mm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. Transferred to. The following epoxy resin liquid 3a was applied on the upper surface of the coater using a resin liquid supply device 2 such as a nozzle in an amount of about 124 g / m 2 . The gap between the support base 4b and the coater 4a such as a coater roll or a doctor knife is adjusted to 0.2 mm in advance.

【0016】片面側に樹脂液を塗布されたガラスクロス
1は直ちに加温装置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%
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 heated by the heating / drying device 6. Both surfaces were 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 approx. 61.5%

【0017】《実施例2》この実施例では、210g/
2 のガラスクロスの場合を示す。実施例1と同じく3
m/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を約214g/m
2 の量で塗布した。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, 210 g /
The case of a glass cloth of m 2 is shown. 3 as in Example 1
The epoxy resin liquid 3a shown in the above table is transferred to the coating device 4 at a speed of m / min and the amount of the epoxy resin liquid 3a shown in the above table is about 214 g / m.
It was applied in an amount of 2 . 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
は直ちに加温装置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で下面側に約38g/m2 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
3bは最初に塗布するエポキシ樹脂液3aと同一のもの
を使用したが、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 in an amount of about 38 g / m 2. To do. The epoxy resin liquid 3b in the resin liquid tank 7d is the same as the epoxy resin liquid 3a to be applied first, but may be different 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。この結果は以下の通りであり、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。 〈プリプレグ中のボイド数〉 5.2mm2 の面積内 実施例1 0 実施例2 約20〜50 従来例 500〜1000以上
The prepregs of Examples 1 and 2 were observed with a 50 × microscope to examine the presence or absence of bubbles in the prepreg. The results are as follows, and the number of voids was extremely small in each case, and the number of voids was significantly smaller than that of the prepreg obtained by the usual impregnation method using the epoxy resin solution having the same composition. <Number of voids in prepreg> Within area of 5.2 mm 2 Example 10 Example 2 Approximately 20 to 50 Conventional example 500 to 1000 or more

【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温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 reducing the viscosity of the resin liquid while suppressing the evaporation of the solvent in the resin liquid, It is possible to obtain an extremely 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 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 加温装置 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

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、しかる後これを加熱乾燥させることによって
プリプレグを製造する方法において、前記シート状基材
の片面側に樹脂液を塗布する工程、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
より加温する工程、しかる後樹脂含浸シート状基材を加
熱乾燥する工程を有することを特徴とするプリプレグの
製造方法。
1. A method for producing a prepreg by impregnating a sheet-like base material made of a fibrous material with a resin liquid and then heating and drying the resin liquid, wherein the resin liquid is applied to one side of the sheet-like base material. Characterized by having a step of heating from the side opposite to 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 heating and drying the resin-impregnated sheet-shaped substrate Manufacturing method of prepreg.
【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、しかる後これを加熱乾燥させることによって
プリプレグを製造する方法において、前記シート状基材
の片面側に樹脂液を塗布する工程、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
より加温する工程、しかる後前記樹脂液を塗布した面の
反対面に樹脂液を塗布する工程、さらに樹脂含浸シート
状基材を加熱乾燥する工程を有することを特徴とするプ
リプレグの製造方法。
2. A method for producing a prepreg by impregnating a sheet-like base material made of a fibrous material with a resin liquid and then heating and drying the resin liquid, wherein the resin liquid is applied to one side of the sheet-like base material. Step, heating the resin liquid at a temperature lower than the boiling point of the solvent used for the resin liquid from the opposite surface side, then applying the resin liquid to the opposite surface of the resin liquid applied surface, A method for producing a prepreg, which further comprises a step of heating and drying the resin-impregnated sheet-shaped substrate.
【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
温する加温装置と、樹脂含浸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 manufacturing a prepreg, comprising: a heating device for further heating and a heating / drying device through which a resin-impregnated sheet-shaped substrate 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
温する加温装置と、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
脂含浸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 surface opposite to 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 a heating / drying device through which the resin-impregnated sheet-shaped substrate passes, the prepreg manufacturing device.
JP3690196A 1996-02-23 1996-02-23 Method and device for manufacturing prepreg Pending JPH09225938A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3690196A JPH09225938A (en) 1996-02-23 1996-02-23 Method and device for manufacturing prepreg

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3690196A JPH09225938A (en) 1996-02-23 1996-02-23 Method and device for manufacturing prepreg

Publications (1)

Publication Number Publication Date
JPH09225938A true JPH09225938A (en) 1997-09-02

Family

ID=12482692

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3690196A Pending JPH09225938A (en) 1996-02-23 1996-02-23 Method and device for manufacturing prepreg

Country Status (1)

Country Link
JP (1) JPH09225938A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001261862A (en) * 2000-03-17 2001-09-26 Hitachi Chem Co Ltd Preparation process of prepreg, prepreg, metal-laminated laminate and printed circuit board
JP2002353581A (en) * 2001-05-30 2002-12-06 Hitachi Chem Co Ltd Manufacturing method of prepreg for printed wiring board
JP2010248520A (en) * 2010-06-01 2010-11-04 Hitachi Chem Co Ltd Method for producing prepreg, prepreg, metal-clad laminate, and printed wiring board
WO2018173618A1 (en) * 2017-03-22 2018-09-27 東レ株式会社 Method for producing prepreg and method for producing fiber-reinforced composite material

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001261862A (en) * 2000-03-17 2001-09-26 Hitachi Chem Co Ltd Preparation process of prepreg, prepreg, metal-laminated laminate and printed circuit board
JP2002353581A (en) * 2001-05-30 2002-12-06 Hitachi Chem Co Ltd Manufacturing method of prepreg for printed wiring board
JP4696399B2 (en) * 2001-05-30 2011-06-08 日立化成工業株式会社 Method for producing prepreg for printed wiring board
JP2010248520A (en) * 2010-06-01 2010-11-04 Hitachi Chem Co Ltd Method for producing prepreg, prepreg, metal-clad laminate, and printed wiring board
WO2018173618A1 (en) * 2017-03-22 2018-09-27 東レ株式会社 Method for producing prepreg and method for producing fiber-reinforced composite material
JPWO2018173618A1 (en) * 2017-03-22 2020-02-20 東レ株式会社 Method for producing prepreg and method for producing fiber-reinforced composite material
US11806899B2 (en) 2017-03-22 2023-11-07 Toray Industries, Inc. Method for producing prepreg and method for producing fiber-reinforced composite material

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