JPH0121770B2 - - Google Patents
Info
- Publication number
- JPH0121770B2 JPH0121770B2 JP57122376A JP12237682A JPH0121770B2 JP H0121770 B2 JPH0121770 B2 JP H0121770B2 JP 57122376 A JP57122376 A JP 57122376A JP 12237682 A JP12237682 A JP 12237682A JP H0121770 B2 JPH0121770 B2 JP H0121770B2
- Authority
- JP
- Japan
- Prior art keywords
- base material
- resin
- resin varnish
- varnish
- 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.)
- Expired
Links
- 229920005989 resin Polymers 0.000 claims description 63
- 239000011347 resin Substances 0.000 claims description 63
- 239000002966 varnish Substances 0.000 claims description 57
- 239000000463 material Substances 0.000 claims description 44
- 238000000576 coating method Methods 0.000 claims description 12
- 238000001035 drying Methods 0.000 claims description 11
- 238000004519 manufacturing process Methods 0.000 claims description 11
- 239000011248 coating agent Substances 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 6
- 239000004744 fabric Substances 0.000 description 9
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 description 8
- 238000000034 method Methods 0.000 description 8
- 230000006835 compression Effects 0.000 description 5
- 238000007906 compression Methods 0.000 description 5
- 239000005011 phenolic resin Substances 0.000 description 5
- 235000010678 Paulownia tomentosa Nutrition 0.000 description 4
- 240000002834 Paulownia tomentosa Species 0.000 description 4
- 238000010030 laminating Methods 0.000 description 4
- 229920001568 phenolic resin Polymers 0.000 description 4
- 239000000758 substrate Substances 0.000 description 4
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 239000004745 nonwoven fabric Substances 0.000 description 2
- 230000035515 penetration Effects 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 238000007730 finishing process Methods 0.000 description 1
- 238000007759 kiss coating Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 229920001225 polyester resin Polymers 0.000 description 1
- 239000004645 polyester resin Substances 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B15/00—Pretreatment of the material to be shaped, not covered by groups B29B7/00 - B29B13/00
- B29B15/08—Pretreatment of the material to be shaped, not covered by groups B29B7/00 - B29B13/00 of reinforcements or fillers
- B29B15/10—Coating or impregnating independently of the moulding or shaping step
- B29B15/12—Coating or impregnating independently of the moulding or shaping step of reinforcements of indefinite length
- B29B15/122—Coating or impregnating independently of the moulding or shaping step of reinforcements of indefinite length with a matrix in liquid form, e.g. as melt, solution or latex
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/0058—Liquid or visquous
- B29K2105/0073—Solution
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Reinforced Plastic Materials (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Moulding By Coating Moulds (AREA)
Description
本発明は積層板の製造に使用されるプリプレグ
の製造法、詳しくは、基材に樹脂ワニスを含浸さ
せる方法に関する。
従来プリプレグは、第1図に示すように基材1
を樹脂ワニス2の中に浸漬して通過させ、スクイ
ズロール3で一定量にしぼり乾燥室4で120〜180
℃、1〜5分間乾燥させ所定の寸法に切断して製
造していた。5は製造されたプリプレグである。
しかしながらこの方法では樹脂付着量の調整は
樹脂ワニス濃度で調整しなおかつスクイズロール
で一定量に調整していた。したがつて使用樹脂ワ
ニス濃度は10〜60%(重量%以下同じ)ときわめ
て希釈された状態で含浸させており、その使用す
る溶剤はプリプレグ製品のコストアツプとなりな
おかつ乾燥室で飛散されたものの処理に費用がか
かつていた。本発明に於て、樹脂ワニスとは、フ
エノール樹脂、エポキシ樹脂、ポリエステル樹脂
等の熱硬化性樹脂を、アセトン、メチルエチルケ
トン、トルエン、アルコール等の溶媒に溶解させ
たものである。
樹脂ワニスを60〜80%の高濃度で塗布する場合
従来法例えば第1図に示すような浸漬法で塗布す
ることは可能であるがその場合プリプレグの塗布
付着量は基材である紙及び繊維の空隙量に比例し
て増大していくので、必要付着量が40〜50%の場
合はかなりの量をスクイズロール等で除去しなけ
ればならない。
スクイズロール等で適正樹脂量にしぼると紙の
場合の紙切れ及び右左のバランスのズレにより蛇
行等が発生し実作業が出来ない状態になる。
又濃度60〜80%の高濃度樹脂ワニスを第2図に
示すようなキス塗工法で塗布すると樹脂タンク6
容量が大きく樹脂ワニス温度、濃度変化による塗
布量バラツキが大で適さない。第2図に於て、7
はガイドロール、8はキスロールである。
本発明はこのような点に鑑みてなされたもの
で、基材に、樹脂濃度60〜80%の樹脂ワニスを、
基材の上方から基材の片面に塗布した後乾燥する
ことを特徴とするものである。
第3図は、基材に、樹脂濃度60〜80%の樹脂ワ
ニスを、基材の上方から基材の片面に塗布する方
法の一例を示すもので、この場合は、基材を、水
平方向に移動させると共に基材の上面に、堰板と
カツトバーとにより樹脂ワニスを溜め、カツトバ
ーにより樹脂ワニスの塗布膜厚を調整しながら樹
脂ワニスを基材に塗布するものである。第3図に
於て、1は基材、9はガイドロール、10は圧縮
ロール、11は堰板、12はカツトバー、13は
高濃度樹脂ワニスである。基材11はガイドロー
ル9により送られ圧縮ロール10で基材の厚みを
10〜50体積%圧縮させ(ガイドロール9及び圧縮
ロール10は加熱するとより効果が上がる)圧縮
された基材は堰板11、カツトバー12とにより
基材上面に溜められた高濃度樹脂ワニス13に接
し、高濃度樹脂ワニスは、カツトバー12とガイ
ドロール9のギヤツプにより付着膜厚を調節され
ながら、基材上方から基材の片面に塗布される。
樹脂ワニスの粘度は200〜5000センチポイズが最
も適しておりあまり低粘度のワニスは堰板の両端
から流れる場合がありさらに基材を通してガイド
ロール9に粘着する恐れがある。この場合堰板の
両端に直角に第2の〓板を取付け、堰板11、2
ケの第2の〓板、カツトバー12とにより一定の
スリツト巾を有する長方形の空間を形成し、この
中に樹脂ワニスを供給するようにすると良い。第
2の〓板を基材の幅より内側に取付ければ、基材
の両端部、例えば5〜20mmには樹脂ワニスが塗布
されないようにすることも出来る。その場合紙布
の両端部を5〜20mmあけて必要な部分のみ、部分
的にコーテイングが出来るこれは積層板の製造に
おいて仕上げ工程で端部を5〜20mm切断しなけれ
ばならず、そのため基材端部は樹脂ワニスをコー
テイングしなくても5〜20mmの樹脂ワニス分の歩
留向上が図れる。
又この方法では通常の基材のまゝでは浸透むら
が発生する場合、紙布の厚み(密度)を圧縮ロー
ルで薄くし紙布の空隙量を少くすることにより均
等に浸透させることが出来る。
第4図は、基材に、樹脂濃度60〜80%の樹脂ワ
ニスを、基材の上方から基材の片面に塗布する他
の方法を示すもので、第4図に於て、1は基材、
14はガイドロール、15はコーテイングロー
ル、16はメタリングロール、17は堰板で高濃
度樹脂ワニス13はメタリングロール16、堰板
17とにより、コーテイングロール15の上に溜
められる。高濃度樹脂ワニス13は、一定量の膜
厚をメタリングロールと16コーテイングロール
15のキヤツプで調整されガイドロール14に通
紙されている紙布等の基材に転写され一定量の樹
脂ワニスを紙布に塗布し乾燥することによりプリ
プレグを製造する。
プリプレグの樹脂付着量の調整は、使用する被
含浸材である紙布等基材の厚み及び密度により決
められるので第4図に示すロール転写法の場合
は、ロール間の精度と保守管理を十分に行ない樹
脂分付着量の変動とロール間の安全性さらに高速
における不均一膜厚が発生しないようにロール間
の精度をコントロールする。
第3図、第4図にそれぞれ示すように、カツト
バー12と堰板11、又は、メタリングロール1
6と堰板17とにより、基材上面又はコーテイン
グロールの上に溜められた高濃度樹脂ワニス13
に熱を与え、高濃度樹脂ワニスの粘度を下げるこ
とが好ましい。この場合、加温は35℃〜50℃が好
ましい。低粘度になることによりワニスは紙の繊
維間へ浸透しやすくなり、かつ繊維へのぬれ性も
向上する。高濃度樹脂ワニスに熱を与えるには例
えば第3図に於て、ガイドロール9、カツトバー
12又、第4図に於て、コーテイングロール1
5、メタリングロール16の一方又は双方の中に
高温の熱媒体(蒸気、温水)配管を行い、これら
を熱ロールとすることにより行うことが出来る。
第5図は、第3図のガイドロール9、カツトバー
12に、熱媒体配管18を行つたものの斜視図で
ある。第3図に於て、ガイドロール9、カツトバ
ー12が冷体では接触する高濃度樹脂は、ワニ
ス、紙等の基材から熱が奪われワニス粘度が高く
なり悪影響を及ぼす。これらのロール熱媒体を通
しワニス粘度上昇を防ぎ、かつ高濃度樹脂ワニス
が紙等の基材に浸透するのに必要とする時間を維
持する。高濃度樹脂ワニスに与える熱量を可変と
することにより、ワニス粘度は必要とする値に雰
囲気温度に関係なく調整できる。
以上説明したように、本発明は、基材に、樹脂
濃度60〜80%の樹脂ワニスを、基材の上方から基
材の片面に塗布した後乾燥することを特徴とする
プリプレグの製造法であり、本発明に於て、基材
としては、紙のみでなく、ガラス不織布、ガラス
布、合成繊維の布不織布が使用し得る。樹脂濃度
60〜80%の高濃度樹脂ワニスを基材の上方から基
材の片面に塗布する場合、基材の真上、即ち、鉛
直方向からだけでなく、45゜傾いた方向から塗布
することも出来る。又、乾燥は80〜180℃で20秒
〜5分加熱することにより行なわれる。
本発明に於ては、基材に樹脂ワニスを含浸乾燥
してプリプレグを製造する場合、60〜80%の高濃
度の樹脂ワニスが使用出来、溶剤の使用量が少な
くてすみ、プリプレグ製造の効率化が達成され
る。
実施例 1
水溶性フエノール樹脂でコツトンリンタ紙基材
を前処理した後、第3図の塗工法で桐油変性フエ
ノール樹脂のワニス濃度70%のワニスを樹脂付着
量50%になるように室温で含浸乾燥させてプリプ
レグを得た。このプリプレグを8枚加熱加圧積層
して得た1.6mmの積層板の特性を別表に示す。
実施例 2
水溶性フエノール樹脂でコツトンリンタ紙基材
を前処理した後第4図の塗工法で桐油変性フエノ
ール樹脂のワニス濃度65%のワニスを樹脂付着量
50%になるように室温で含浸乾燥させてプリプレ
グを得た。このプリプレグを8枚加熱加圧積層し
て得た1.6mmの積層板の特性を別表に示す。
実施例 3
水溶性フエノール樹脂でコツトンリンタ紙基材
を前処理した後第3図の塗工法で桐油変性フエノ
ール樹脂のワニス濃度75%のワニスを樹脂付着量
50%になるようにワニスを40℃に加温して含浸乾
燥させてプリプレグを得た。このプリプレグを8
枚加熱加圧積層して得た1.6mmの積層板の特性を
別表に示す。
比較例
水溶性フエノール樹脂でコツトンリンタ紙基材
を前処理した後に第1図の塗工法で桐油変性フエ
ノール樹脂ワニスのワニス濃度50%のワニスを樹
脂付着量50%になるように室温で含浸乾燥させて
プリプレグを得た。このプリプレグを8枚加熱加
圧積層して得た1.6mmの積層板の特性を別表に示
す。
The present invention relates to a method for manufacturing a prepreg used for manufacturing a laminate, and more particularly, to a method for impregnating a base material with a resin varnish. Conventional prepreg has a base material 1 as shown in Figure 1.
is immersed in resin varnish 2, passed through it, squeezed to a certain amount with squeeze roll 3, and heated to 120 to 180 in the drying room 4.
℃ for 1 to 5 minutes and cut into predetermined dimensions. 5 is the manufactured prepreg. However, in this method, the amount of resin deposited was adjusted by adjusting the resin varnish concentration and was also adjusted to a constant amount using a squeeze roll. Therefore, the resin varnish used is impregnated in a very diluted state with a concentration of 10 to 60% (same as below weight%), and the solvent used increases the cost of prepreg products and is difficult to dispose of the material scattered in the drying room. It was expensive. In the present invention, a resin varnish is one in which a thermosetting resin such as a phenol resin, an epoxy resin, or a polyester resin is dissolved in a solvent such as acetone, methyl ethyl ketone, toluene, or alcohol. When applying resin varnish at a high concentration of 60 to 80%, it is possible to apply it using conventional methods, such as the dipping method shown in Figure 1, but in that case, the amount of prepreg applied will be lower than the paper and fibers that are the base material. Since the amount of adhesion increases in proportion to the amount of voids, if the required amount of adhesion is 40 to 50%, a considerable amount must be removed with a squeeze roll or the like. If the amount of resin is reduced to an appropriate amount using a squeeze roll or the like, meandering will occur due to paper breakage and imbalance between the right and left sides, making it impossible to perform actual work. Also, if a high-concentration resin varnish with a concentration of 60 to 80% is applied using the kiss coating method as shown in Figure 2, the resin tank 6
It is not suitable because it has a large capacity and the amount of application varies widely due to changes in resin varnish temperature and concentration. In Figure 2, 7
is a guide roll, and 8 is a kiss roll. The present invention was made in view of these points, and includes a resin varnish with a resin concentration of 60 to 80% on the base material.
It is characterized in that it is applied to one side of the substrate from above and then dried. Figure 3 shows an example of a method in which a resin varnish with a resin concentration of 60 to 80% is applied to one side of the base material from above the base material. The resin varnish is stored on the upper surface of the base material using a weir plate and a cut bar, and the resin varnish is applied to the base material while adjusting the coating film thickness of the resin varnish using the cut bar. In FIG. 3, 1 is a base material, 9 is a guide roll, 10 is a compression roll, 11 is a weir plate, 12 is a cut bar, and 13 is a high concentration resin varnish. The base material 11 is sent by a guide roll 9 and the thickness of the base material is reduced by a compression roll 10.
The compressed base material is compressed by 10 to 50% by volume (heating the guide roll 9 and compression roll 10 will improve the effect). The high-concentration resin varnish is applied to one side of the substrate from above, with the thickness of the deposited film being adjusted by the gap between the cut bar 12 and the guide roll 9.
The most suitable viscosity of the resin varnish is 200 to 5000 centipoise, and a varnish with too low a viscosity may flow from both ends of the weir plate and may also stick to the guide roll 9 through the base material. In this case, a second weir plate is installed at right angles to both ends of the weir plate, and the weir plates 11, 2
It is preferable that a rectangular space having a constant slit width is formed by the second cutter plate and the cut bar 12, and the resin varnish is supplied into this rectangular space. If the second plate is attached inside the width of the base material, the resin varnish can be prevented from being applied to both ends of the base material, for example, 5 to 20 mm. In that case, you can leave a 5-20mm gap between both ends of the paper cloth and coat only the necessary areas.This is because the edges must be cut off by 5-20mm during the finishing process in the production of laminates, so the base material Even if the end portions are not coated with resin varnish, the yield can be improved by 5 to 20 mm of resin varnish. In addition, in this method, if uneven penetration occurs with a normal base material, even penetration can be achieved by thinning the thickness (density) of the paper cloth using a compression roll and reducing the amount of voids in the paper cloth. Figure 4 shows another method of applying a resin varnish with a resin concentration of 60 to 80% to one side of the base material from above the base material. wood,
14 is a guide roll, 15 is a coating roll, 16 is a metering roll, and 17 is a weir plate. The high concentration resin varnish 13 is accumulated on the coating roll 15 by the metering roll 16 and the weir plate 17. The high-concentration resin varnish 13 is transferred to a base material such as paper cloth, which is transferred to a base material such as paper cloth, which is passed through a guide roll 14, with a film thickness of a certain amount adjusted by a cap of a metering roll and a coating roll 15, and a certain amount of resin varnish is applied. Prepreg is manufactured by applying it to paper cloth and drying it. Adjustment of the amount of resin attached to the prepreg is determined by the thickness and density of the base material used, such as paper cloth, to be impregnated. Therefore, in the case of the roll transfer method shown in Figure 4, sufficient precision and maintenance between rolls must be maintained. In addition, the accuracy between rolls is controlled to prevent fluctuations in the amount of resin deposited, safety between rolls, and non-uniform film thickness at high speeds. As shown in FIGS. 3 and 4, the cut bar 12 and the weir plate 11 or the metering roll 1
6 and the weir plate 17, the high concentration resin varnish 13 is accumulated on the upper surface of the base material or on the coating roll.
It is preferable to apply heat to lower the viscosity of the high concentration resin varnish. In this case, heating is preferably from 35°C to 50°C. By lowering the viscosity, the varnish can more easily penetrate between the paper fibers and improve its wettability to the fibers. To apply heat to the high concentration resin varnish, for example, in FIG. 3, the guide roll 9 and the cut bar 12, and in FIG.
5. This can be carried out by providing high-temperature heat medium (steam, hot water) piping in one or both of the metering rolls 16 and using these as a heat roll.
FIG. 5 is a perspective view of the guide roll 9 and cut bar 12 shown in FIG. 3 with heat medium piping 18 installed therein. In FIG. 3, the highly concentrated resin that the guide roll 9 and cut bar 12 come into contact with in a cold state removes heat from the base material such as varnish or paper, increasing the viscosity of the varnish and having an adverse effect. These rollers pass through the heat medium to prevent the varnish from increasing in viscosity and to maintain the time required for the high concentration resin varnish to penetrate into the base material such as paper. By varying the amount of heat given to the high-concentration resin varnish, the varnish viscosity can be adjusted to a required value regardless of the ambient temperature. As explained above, the present invention is a prepreg manufacturing method characterized by applying a resin varnish with a resin concentration of 60 to 80% to one side of the base material from above the base material and then drying it. In the present invention, as the base material, not only paper but also glass nonwoven fabric, glass cloth, and synthetic fiber cloth or nonwoven fabric can be used. resin concentration
When applying a 60-80% high concentration resin varnish to one side of a substrate from above, it can be applied not only from directly above the substrate, that is, vertically, but also from a 45° angle. . Further, drying is performed by heating at 80 to 180°C for 20 seconds to 5 minutes. In the present invention, when producing prepreg by impregnating and drying a resin varnish on a base material, a resin varnish with a high concentration of 60 to 80% can be used, and the amount of solvent used is small, which improves the efficiency of prepreg production. is achieved. Example 1 After pre-treating the paper base material with a water-soluble phenolic resin, it was impregnated with a 70% varnish of tung oil-modified phenolic resin using the coating method shown in Figure 3 and dried at room temperature so that the resin coverage was 50%. Prepreg was obtained. The properties of a 1.6 mm laminate obtained by laminating 8 sheets of this prepreg under heat and pressure are shown in the attached table. Example 2 After pre-treating a Kotonlinta paper base material with a water-soluble phenolic resin, a varnish of 65% varnish concentration of tung oil-modified phenolic resin was applied using the coating method shown in Figure 4 to reduce the amount of resin attached.
A prepreg was obtained by impregnating and drying at room temperature to a concentration of 50%. The properties of a 1.6 mm laminate obtained by laminating 8 sheets of this prepreg under heat and pressure are shown in the attached table. Example 3 After pre-treating a paper base material with a water-soluble phenolic resin, a varnish of 75% varnish concentration of tung oil-modified phenolic resin was applied using the coating method shown in Figure 3 to reduce the amount of resin attached.
A prepreg was obtained by heating the varnish to 40°C and impregnating and drying it so that the concentration was 50%. This prepreg is 8
The properties of the 1.6 mm laminate obtained by laminating the sheets under heating and pressure are shown in the attached table. Comparative Example After pre-treating a Kotton Rinter paper base material with a water-soluble phenolic resin, it was impregnated with a 50% varnish concentration of tung oil-modified phenolic resin varnish using the coating method shown in Figure 1 and dried at room temperature so that the resin coverage was 50%. A prepreg was obtained. The properties of a 1.6 mm laminate obtained by laminating 8 sheets of this prepreg under heat and pressure are shown in the attached table.
【表】【table】
【表】
この表からも明らかなように、本発明に於て
は、60〜80%の高濃度樹脂ワニスを使用しても従
来の低濃度樹脂ワニスを使用して得られた積層板
と各特性に於て、何ら遜色ないものが得られる。[Table] As is clear from this table, in the present invention, even if a high concentration resin varnish of 60 to 80% is used, the laminate obtained using a conventional low concentration resin varnish and each In terms of characteristics, it is possible to obtain something comparable in no way.
第1図〜第4図はプリプレグの製造法を示す簡
略断面図で、第1,2図は従来のもの、第3,4
図は本発明のものを示す。第5図は第3図のガイ
ドロール、カツトバーを加熱した状態を示す斜視
図である。
符号説明、1……基材、2……樹脂ワニス、3
……スクイズロール、4……乾燥室、5……プリ
プレグ、6……樹脂タンク、7……ガイドロー
ル、8……キスロール、9……ガイドロール、1
0……圧縮ロール、11……堰板、12……カツ
トバー、13……高濃度樹脂ワニス、14……ガ
イドロール、15……コーテイングロール、16
……メタリングロール、17……堰板、18……
熱媒体配管。
Figures 1 to 4 are simplified sectional views showing the prepreg manufacturing method, with Figures 1 and 2 being the conventional method, and Figures 3 and 4 being the same.
The figure shows the invention. FIG. 5 is a perspective view showing the guide roll and cut bar shown in FIG. 3 in a heated state. Description of symbols, 1...Base material, 2...Resin varnish, 3
... Squeeze roll, 4 ... Drying room, 5 ... Prepreg, 6 ... Resin tank, 7 ... Guide roll, 8 ... Kiss roll, 9 ... Guide roll, 1
0... Compression roll, 11... Weir plate, 12... Cut bar, 13... High concentration resin varnish, 14... Guide roll, 15... Coating roll, 16
...Metaling roll, 17...Weir plate, 18...
Heat medium piping.
Claims (1)
基材の上方から基材の片面に塗布した後乾燥する
ことを特徴とするプリプレグの製造法。 2 基材を、水平方向に移動させると共に、基材
の上面に、堰板とカツトバーとにより樹脂ワニス
を溜め、カツトバーにより樹脂の塗布膜厚を調整
しながら樹脂ワニスを基材に塗布することを特徴
とする特許請求の範囲第1項記載のプリプレグの
製造法。 3 樹脂ワニスを加温することを特徴とする特許
請求の範囲第1項又は第2項記載のプリプレグの
製造法。 4 基材の両端部を除いて樹脂ワニスを塗布する
ことを特徴とする特許請求の範囲第1項、第2項
又は第3項記載のプリプレグの製造法。 5 基材を圧縮して空隙量を少なくした後、樹脂
濃度60〜80%の樹脂ワニスを、基材の上方から基
材の片面に塗布し、乾燥することを特徴とするプ
リプレグの製造法。[Claims] 1. A resin varnish with a resin concentration of 60 to 80% is applied to the base material,
A prepreg manufacturing method characterized by coating one side of a base material from above and then drying. 2 While moving the base material in the horizontal direction, resin varnish is collected on the upper surface of the base material using a weir plate and a cut bar, and the resin varnish is applied to the base material while adjusting the coating film thickness of the resin using the cut bar. A method for producing a prepreg according to claim 1. 3. The prepreg manufacturing method according to claim 1 or 2, which comprises heating the resin varnish. 4. The prepreg manufacturing method according to claim 1, 2, or 3, characterized in that the resin varnish is applied to the base material except for both ends thereof. 5. A prepreg manufacturing method, which comprises compressing the base material to reduce the amount of voids, then applying a resin varnish with a resin concentration of 60 to 80% to one side of the base material from above the base material, and drying.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57122376A JPS5912814A (en) | 1982-07-14 | 1982-07-14 | Preparation of prepreg |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57122376A JPS5912814A (en) | 1982-07-14 | 1982-07-14 | Preparation of prepreg |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5912814A JPS5912814A (en) | 1984-01-23 |
| JPH0121770B2 true JPH0121770B2 (en) | 1989-04-24 |
Family
ID=14834302
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57122376A Granted JPS5912814A (en) | 1982-07-14 | 1982-07-14 | Preparation of prepreg |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5912814A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2183951B (en) * | 1985-11-28 | 1990-05-23 | Duracell Int | Displacement measuring apparatus |
| JPH02121908U (en) * | 1989-03-17 | 1990-10-04 | ||
| JP2002194671A (en) * | 2000-12-21 | 2002-07-10 | Kanegafuchi Chem Ind Co Ltd | How to prevent hair loss on piloerected textile products |
| EP3599069B1 (en) | 2018-07-23 | 2023-04-12 | Crompton Technology Group Limited | Fibre coating apparatus |
-
1982
- 1982-07-14 JP JP57122376A patent/JPS5912814A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5912814A (en) | 1984-01-23 |
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