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JPH0579485B2 - - Google Patents
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JPH0579485B2 - - Google Patents

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Publication number
JPH0579485B2
JPH0579485B2 JP21223885A JP21223885A JPH0579485B2 JP H0579485 B2 JPH0579485 B2 JP H0579485B2 JP 21223885 A JP21223885 A JP 21223885A JP 21223885 A JP21223885 A JP 21223885A JP H0579485 B2 JPH0579485 B2 JP H0579485B2
Authority
JP
Japan
Prior art keywords
sheet
roll
resin
laminate
fiber base
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
JP21223885A
Other languages
Japanese (ja)
Other versions
JPS6273916A (en
Inventor
Toshihiko Kadota
Kunyoshi Yamada
Tatsuya Ito
Toshiaki Hanyuda
Kaneya Yamaguchi
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.)
Resonac Holdings Corp
Original Assignee
Showa Highpolymer 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 Showa Highpolymer Co Ltd filed Critical Showa Highpolymer Co Ltd
Priority to JP21223885A priority Critical patent/JPS6273916A/en
Publication of JPS6273916A publication Critical patent/JPS6273916A/en
Publication of JPH0579485B2 publication Critical patent/JPH0579485B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、樹脂と繊維基材からなる成形用シー
ト状樹脂複合材を製造する方法に関する。さらに
詳しくは、チヨツプドストランド、マツトおよび
クロス等のガラス繊維基材、あるいは炭素系の繊
維基材、あるいは木綿、麻等の天前然繊維やポリ
エステル、ポリアミド、ポリビニルアルコール等
の合成繊維を含む有機質繊維基材等の各種繊維基
材から選ばれた1種または多種に、液状樹脂ある
いは樹脂混合液を含浸させて、成形用シート状樹
脂複合材を製造する方法に関し、特に、これら繊
維基材と樹脂の混合物を剥離シートの片面に積層
した後に、例えば該積層物を内側にしてロール状
に巻き取る過程における樹脂の繊維基材への含浸
および脱泡を促進する技術に関するものであつ
て、その目的は、繊維基材の含有率が高く、かつ
気泡がない、あるいは気泡が少ない高品質、高性
能の樹脂/繊維複合製品(以下FRPという)用
の成形材料すなわちプリプレグを提供するにあ
る。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing a sheet-shaped resin composite material for molding consisting of a resin and a fiber base material. More specifically, glass fiber base materials such as chopped strand, pine and cloth, carbon fiber base materials, natural fibers such as cotton and linen, and synthetic fibers such as polyester, polyamide, and polyvinyl alcohol are used. Regarding the method of producing a sheet-like resin composite material for molding by impregnating one or more selected types of fiber base materials such as organic fiber base materials with a liquid resin or a resin mixture, in particular, The invention relates to a technique for promoting impregnation of resin into a fiber base material and defoaming in the process of laminating a mixture of material and resin on one side of a release sheet and then winding it up into a roll with the laminate inside, for example. The purpose is to provide a high quality, high performance molding material for resin/fiber composite products (hereinafter referred to as FRP), that is, prepreg, which has a high content of fiber base material and has no or few bubbles. .

〔従来の技術〕[Conventional technology]

従来、シート状FRP成形材料としてSMC
(sheet molding compound)が知られている。
この製造機として、たとえば、ゴムベルト式やメ
ツシユベルト式があり、前者は2枚の離型フイル
ムに挾んだ液状樹脂と繊維基材の積層物を平らな
ゴムベルトに載せ、その上からベルトの進行方向
に沿つて複数本の平ロールや筋ロールで押さえつ
けることにより、該積層物に圧縮、剪断および延
伸等の力を及ぼして、含浸を促進するものであ
り、また後者は、メツシユベルトの凹凸形状の効
果が加わつて、含浸をさらに促進しようとするも
のである。ところで、SMCは一般に液状樹脂と
繊維の他に、粉・粒状フイラーが高濃度に含有さ
れているため、含浸時の液状樹脂と該フイラーの
混合物の粘度は、たとえば100ポアズ以上でかな
り高い。この高粘度の系が繊維基材に含浸する力
を得るためにはロールの押圧を高くする必要があ
る。しかし押圧に伴い、一般に樹脂の流動が起
り、シートの横方向へ流出し易い。SMCでは積
層物を挾む上下2枚の離型フイルムが、この樹脂
の流れ出しを防いでいるのである。
Conventionally, SMC was used as a sheet-shaped FRP molding material.
(sheet molding compound) is known.
For example, there are rubber belt type and mesh belt type machines for this production.The former places a laminate of liquid resin and fiber base material sandwiched between two release films on a flat rubber belt, and then By pressing the laminate with a plurality of flat rolls or striped rolls along the mesh belt, forces such as compression, shearing, and stretching are applied to the laminate to promote impregnation. is added to further promote impregnation. Incidentally, since SMC generally contains powder/granular filler at a high concentration in addition to liquid resin and fibers, the viscosity of the mixture of liquid resin and filler during impregnation is quite high, for example, 100 poise or more. In order to obtain enough force to impregnate the fiber base material with this highly viscous system, it is necessary to increase the pressure of the rolls. However, as the resin is pressed, it generally flows and tends to flow in the lateral direction of the sheet. In SMC, the upper and lower release films that sandwich the laminate prevent this resin from flowing out.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

本発明が対象とする技術課題は、0.8〜50ポア
ズという比較的低い範囲の粘度をもつ液状樹脂を
チヨツプドストランド、マツトあるいはクロス等
の形状の繊維基材に、短時間に含浸を完了させる
方法についてである。すなわち上記のSMCの製
造に見られる含浸法は、本発明の系のように、粘
度が低いこと、および上側に離型フイルムをかぶ
せないことから、もし含浸のための押圧が高い
と、液状樹脂が流出してしまう。これを防止する
ために、押圧を低くしたり、あるいは溝が深く、
幅が広いような特殊な筋ロールを使えば、それだ
け含浸のための力が相殺されてしまう。
The technical problem addressed by the present invention is to complete impregnation of a fiber base material in the form of chopped strands, mats, or cloth in a short time with a liquid resin having a relatively low viscosity of 0.8 to 50 poise. It's about how to do it. In other words, the impregnation method seen in the production of SMC mentioned above has a low viscosity and does not cover the upper side with a release film like the system of the present invention, so if the pressure for impregnation is high, the liquid resin will leak out. To prevent this, the pressure may be lowered or the grooves may be deep.
If you use a special muscle roll with a wide width, the force for impregnation will be offset accordingly.

したがつて、この種の含浸ロールによる含浸法
に代る別種の方法を探すか、あるいはこの含浸ロ
ール法を補填する方法を見出し、含浸効果を高め
る必要がある。
Therefore, it is necessary to find another method to replace this type of impregnation method using an impregnation roll, or to find a method to supplement this impregnation roll method to enhance the impregnation effect.

〔問題を解決するための手段〕[Means to solve the problem]

本発明者らは、上記のごとき従来技術の適用の
限界、乃至問題点につき、鋭意検討した結果、連
続的なシート状樹脂複合材の含浸法としては、ま
つたく新規であり、かつ比較的機構の簡単な装置
を従来の機械に付設することにより、所期の目的
に達することができることを見出し、本発明に到
つた。
As a result of intensive investigation into the limitations and problems of the application of the prior art as described above, the present inventors found that a continuous impregnation method for sheet-shaped resin composites is both novel and relatively mechanical. The inventors have discovered that the desired objective can be achieved by attaching a simple device to a conventional machine, and have arrived at the present invention.

すなわち、本発明は従来の含浸ロールを用いる
装置において、液状樹脂と繊維基材の積層物を運
搬する剥離シートの下側に、剥離シートに接して
可動板を設け、バイブレーターに接続された可動
板の上下の振動によつて、積層物特に液状樹脂
に、任意の振動数と振幅の脈動を与えるものであ
る。その効果は、いいかえれば上部の含浸ロール
の積層物への押圧に脈動を与え、これによつて生
じる局所的な液体の流動、すなわち、積層物の厚
さ方向の振動による含浸の促進にある。
That is, the present invention provides a device using a conventional impregnating roll, in which a movable plate is provided below the release sheet and in contact with the release sheet for conveying a laminate of liquid resin and fiber base material, and the movable plate is connected to a vibrator. By vertically vibrating the laminate, especially liquid resin, pulsation of arbitrary frequency and amplitude is applied. In other words, the effect is that the pressure of the upper impregnating roll on the laminate is pulsated, and the resulting local liquid flow, that is, the vibration in the thickness direction of the laminate, promotes impregnation.

〔作用〕[Effect]

この方法で問題となるのはどの程度の振動を与
えるかである。一般に粘性液体を振動する(揺り
動かす)場合、振動数の増加につれ、損失率が大
きくなることが知られている。一方、液体の振動
数が高いほど、目的とする液体の局所的流動の頻
度は高くなり、したがつて、外部の振動応力の振
動数には好適な限られた範囲が存在することにな
る。本発明の積層物の厚さを勘案して、振幅を
0.1〜1.0mmとすると好適な振動数は1〜20Hzであ
る。
The problem with this method is how much vibration to apply. It is generally known that when vibrating (shaking) a viscous liquid, the loss rate increases as the vibration frequency increases. On the other hand, the higher the frequency of the liquid, the higher the frequency of local flow of the target liquid, and therefore there is a suitable limited range of the frequency of the external vibrational stress. The amplitude should be adjusted in consideration of the thickness of the laminate of the present invention.
When it is 0.1 to 1.0 mm, a suitable vibration frequency is 1 to 20 Hz.

この振動は、市販の発振器(バイブレータ)
で、あるいは、振動数の調節のためインバーター
(周波数変換装置)を付設して実現できる。
This vibration is generated by a commercially available oscillator (vibrator)
Alternatively, it can be realized by adding an inverter (frequency converter) to adjust the vibration frequency.

本発明による上下振動は剥離紙を介して積層物
に伝えられ、上部の固定された複数本の含浸ロー
ルの接層物の押圧に脈動を与える。これによつ
て、含浸ロールが本来もつている圧縮、剪断等に
よる混練、含浸および脱泡の効果が飛躍的に促進
される。
The vertical vibration according to the present invention is transmitted to the laminate through the release paper, and gives pulsations to the pressing of the laminate by the plurality of impregnating rolls fixed at the top. As a result, the effects of kneading, impregnation, and defoaming by compression, shearing, etc. that the impregnating roll originally has are dramatically promoted.

以下、本発明を図を用いて説明する。 Hereinafter, the present invention will be explained using figures.

本発明の液状樹脂/繊維基材複合材製造装置の
一例を図に示す。この図では、振動部が2ケ所示
されているが、この振動部の個数は特定するもの
ではない。バイブレータ4が可動板5に接続さ
れ、バイブレータ4の振動が直接に可動板5に伝
わる。剥離シート2は平らなステンレス製の固定
板と可動板の上を定速で移動するが、可動板の上
で上下動をうける。液状樹脂/繊維基材複合積層
物(チヨツプドストランドマツト)1も同様に移
動し、可動板5の上部に設置された含浸ロール6
により脈動状の押圧をうける。この含浸ロール6
の型や大きさおよび本数は特定されず、また、可
動板上のみでなく、さらに固定板上にあつても差
しつかえない。バイブレータ4による発振の振動
数は1〜20Hzであり、3〜10Hzが好適である。こ
の範囲より低周波数では効果が少なく、一方高周
波側は振動の損失が大きく効率が低くなる。振幅
は積層物の厚さと含浸ロールの押圧効果を勘案し
て、0.1〜1.0mmであり、0.2〜0.5mmが好適である。
An example of the liquid resin/fiber base material composite manufacturing apparatus of the present invention is shown in the figure. In this figure, two vibrating parts are shown, but the number of vibrating parts is not specified. A vibrator 4 is connected to a movable plate 5, and the vibrations of the vibrator 4 are directly transmitted to the movable plate 5. The release sheet 2 moves at a constant speed on a flat stainless steel fixed plate and a movable plate, but is subjected to vertical movement on the movable plate. The liquid resin/fiber base material composite laminate (chipped strand mate) 1 also moves in the same way, and the impregnation roll 6 installed on the upper part of the movable plate 5
It is subjected to pulsating pressure. This impregnation roll 6
The type, size, and number of the plates are not specified, and they may be placed not only on the movable plate but also on the fixed plate. The frequency of oscillation by the vibrator 4 is 1 to 20 Hz, preferably 3 to 10 Hz. At frequencies lower than this range, there is little effect, while at higher frequencies vibration loss is large and efficiency is low. The amplitude is 0.1 to 1.0 mm, preferably 0.2 to 0.5 mm, taking into account the thickness of the laminate and the pressing effect of the impregnated roll.

含浸工程とレベリングが終了したシート状成形
材料は、剥離シートを外側にして巻き取りロール
7で連続して巻きとられるか、定尺にカツトされ
る。
The sheet-shaped molding material that has undergone the impregnation process and leveling is continuously wound up with a take-up roll 7 with the release sheet facing outside, or is cut into a regular length.

ここで使用される剥離シートに両面が剥離処理
されたシートを使うとそのまま巻き取つたり、ま
た積み重ねても、使用時に容易に成形材料が剥が
れるので好都合である。
It is advantageous to use a release sheet that has been subjected to release treatment on both sides as the release sheet used here, since the molding material can be easily peeled off during use even when the sheets are rolled up or stacked.

本発明の対象とするFRP成形材料の主成分た
る樹脂とは、熱硬化性のオリゴマー、またはその
反応性希釈剤溶液であつて、後述の繊維基材を除
く添加剤とこれらの混合物の粘度が高くとも50ポ
アズ、好ましくは20ポアズ以下の液体である。好
適な例としては、不飽和ポリエステル樹脂、ビニ
ルエステル樹脂、エポキシ樹脂、ジアリルフタレ
ート樹脂あるいはフエノール樹脂に類別される熱
硬化性オリゴマー、およびこれらを反応性低分子
有機化合物に希釈した溶液であつて、さらに硬化
反応触媒、硬化反応促進剤および必要に応じて粘
度調節剤、湿潤剤等を添加する。より具体的に、
不飽和ポリエステル樹脂系あるいはビニルエステ
ル樹脂系を例にして述べれば、それぞれの基本オ
リゴマー、あるいはこれをスチレン、フタル酸ジ
アリルやアクリル酸エステルなどの反応性不飽和
化合物で希釈した溶液に、加熱硬化を目的とする
ならば有機過酸物触媒を、また紫外線硬化を目的
とするならば光増感剤を適量添加し、さらに必要
に応じて酸化マグネシウムやポリイソシアネート
系等の増粘剤、等を添加し混合する。混合物の粘
度は作業条件下で50ポアズ以下、好ましくは1〜
20ポアズが本発明の製造に適する。
The resin that is the main component of the FRP molding material that is the object of the present invention is a thermosetting oligomer or its reactive diluent solution, and the viscosity of the additives and mixtures thereof, excluding the fiber base material described below, is The liquid is at most 50 poise, preferably 20 poise or less. Suitable examples include thermosetting oligomers classified as unsaturated polyester resins, vinyl ester resins, epoxy resins, diallyl phthalate resins, or phenol resins, and solutions obtained by diluting these with reactive low-molecular organic compounds, Furthermore, a curing reaction catalyst, a curing reaction accelerator, and if necessary, a viscosity modifier, a wetting agent, etc. are added. More specifically,
Taking an unsaturated polyester resin system or a vinyl ester resin system as an example, each basic oligomer or a solution of this diluted with a reactive unsaturated compound such as styrene, diallyl phthalate, or acrylate ester is heated and cured. If you are aiming for UV curing, add an appropriate amount of an organic peroxide catalyst, or if you are aiming for ultraviolet curing, add an appropriate amount of photosensitizer, and if necessary, add a thickener such as magnesium oxide or polyisocyanate. and mix. The viscosity of the mixture is below 50 poise under working conditions, preferably between 1 and
20 poise is suitable for production according to the invention.

繊維基材として材質および形態のいずれも特定
するものでなく、広くFRPに用いられているガ
ラス繊維、炭素繊維、およびポリエステル、ポリ
アミド、ポリビニルアルコール、セルロース系等
の有機繊維のチヨツプドストランドあるいは短繊
維、これからつくられたマツト、長繊維のマツ
ト、および各種のクロスが用いられる。
Neither the material nor the form is specified as the fiber base material, but chopped strands or organic fibers such as glass fiber, carbon fiber, and organic fibers such as polyester, polyamide, polyvinyl alcohol, and cellulose, which are widely used in FRP, are used as fiber base materials. Short fibers, mats made from them, long fiber mats, and various cloths are used.

液状樹脂と繊維基材の積層方法は、特に制限す
るものでなく、各種のコーテイング技術が応用で
きる。このうち、繊維基材がクロスあるいは長繊
維のマツトならば、液状樹脂槽を通過させる含浸
コーテイング方式が、あるいはより一般には剥離
紙上にナイフコーター等で一定厚みの液状樹脂を
塗布して、その上に繊維基材を積層する方式がと
られる。
The method of laminating the liquid resin and the fiber base material is not particularly limited, and various coating techniques can be applied. Among these methods, if the fiber base material is cloth or long-fiber pine, an impregnating coating method is used in which the fiber is passed through a liquid resin bath, or more generally, a liquid resin is applied to a certain thickness on a release paper using a knife coater, etc. A method is used in which fiber base materials are laminated on top of each other.

〔実施例〕〔Example〕

以下、実施例によつて本発明を詳述する。 Hereinafter, the present invention will be explained in detail with reference to Examples.

実施例 1 不飽和ポリエステル樹脂(リゴラツク M411、
昭和高分子製)100部に対して低収縮剤としてポ
リスチレン(エスブライト #8、昭和電工製)
を4部、硬化触媒としてt−ブチルパーベンゾエ
ート(パーブチル Z、日本油脂製)を1.2部、
増粘剤として酸化マグネシウム(マグミツク 、
協和化学工業製)を2部、離型剤としてステアリ
ン酸亜鉛を2部、さらに炭酸カルシウム(ソフト
ン 1200、備北化学製)を10部、および適量のス
チレンモノマーを配合し、この配合物をヘンシエ
ルミキサーで撹拌混合した後に減圧槽に移して予
備脱泡して、常温で粘度(B−型粘度計)が18ポ
アズの液状樹脂混合物を調製した。
Example 1 Unsaturated polyester resin (Rigorac M411,
Polystyrene (S-Bright #8, manufactured by Showa Denko) as a low shrinkage agent for 100 parts of Showa Kobunshi (manufactured by Showa Kobunshi)
4 parts, 1.2 parts of t-butyl perbenzoate (Perbutyl Z, manufactured by NOF Corporation) as a curing catalyst,
Magnesium oxide (Magumitsuku,
2 parts of Kyowa Chemical Industry Co., Ltd.), 2 parts of zinc stearate as a mold release agent, 10 parts of calcium carbonate (Softon 1200, Bihoku Chemical Co., Ltd.), and an appropriate amount of styrene monomer. After stirring and mixing in a mixer, the mixture was transferred to a vacuum tank and preliminarily defoamed to prepare a liquid resin mixture having a viscosity (B-type viscometer) of 18 poise at room temperature.

有効幅600mm、原料供給部からシートの巻き取
り部までの間で、含浸用のロール等を設置しうる
有効長2500mmの平面部を有し、この上に、原料供
給部の前方から巻き取り部まで剥離シートが等速
に移動できる駆動機構を有する機械を製作した。
有効平面を構成する平板は厚さ3mmのステンレス
製であり、上流部から約200mm、および約1300mm
の場所に、それぞれ幅500mm、長さ700mmの2枚の
長方形の可動板があり、残部は固定板である。可
動板はバイブレータの振動板に一体接続されてい
る。バイブレータは小型ジヤツキに載せてある。
It has a flat section with an effective width of 600 mm and an effective length of 2,500 mm between the raw material supply section and the sheet winding section on which a roll for impregnation can be installed. We have created a machine with a drive mechanism that allows the release sheet to move at a constant speed.
The flat plate that constitutes the effective plane is made of stainless steel with a thickness of 3 mm, and extends approximately 200 mm and 1300 mm from the upstream part.
There are two rectangular movable plates each 500mm wide and 700mm long, and the rest are fixed plates. The movable plate is integrally connected to the diaphragm of the vibrator. The vibrator is mounted on a small jack.

バイブレーターは振動力150Kgf、出力65Wの
市販機で、前方にインバーターを接続して周波数
の調整をした。用いた振動は周波数5Hz、振幅
0.3mmであつた。
The vibrator was a commercially available machine with a vibration force of 150 kgf and an output of 65 W, and an inverter was connected to the front to adjust the frequency. The vibration used had a frequency of 5Hz and an amplitude
It was 0.3mm.

可動板の上方に、外径35mmの筋ロールをそれぞ
れ3本ずつ計6本取りつけた。また、下流の固定
板状に同種の筋ロールを2本取りつけた。これら
のロールはいずれも上部のスプリングにより押圧
が調整された。押圧の度合はロールの前方に形成
される樹脂液のバンクを目安とした。
Above the movable plate, a total of six muscle rolls, three each having an outer diameter of 35 mm, were attached. In addition, two strip rolls of the same type were attached to the downstream stationary plate. The pressure of each of these rolls was adjusted by a spring at the top. The degree of pressure was determined based on the bank of resin liquid formed in front of the roll.

本実施例の装置の概要を図に示す。両面剥離シ
ート(藤森工業製バイナシート 80XT、幅500
mm)が定速(約2m/分)で移動し、ナイフコー
ター(クリアランス約1mm)で上記の液状樹脂混
合物が剥離シート上に幅350mmに積層され、この
上にチヨツプドストランドマツト(旭フアイバー
グラス製、CM305、幅500mm)が積層された後、
含浸ロールと可動板のゾーンを通過し最後に巻き
取り部で剥離シートを外側にして紙管に巻きとら
れた。紙管1本に約10mずつシートを巻きとり、
これを内側にアルミニウム箔をラミネートしたク
ラフト紙で包み、両端を離ゴムで締めて、材料中
のスチレンモノマーの飛散を防いだ。この製品を
温度40℃に保つた空気槽中に2日間保存して熟
成、増粘した。これを取り出して室温まで冷却し
た後、市販のスリツター(ロール面を離型性処理
した機械)で幅100mmおよび150mmのテープとし、
同幅の紙管芯に長さ約10m巻いて、ブリキ製の円
筒缶に収納密封した。
The outline of the apparatus of this example is shown in the figure. Double-sided release sheet (Fujimori Industries Binasheet 80XT, width 500
mm) moves at a constant speed (approximately 2 m/min), the above liquid resin mixture is laminated to a width of 350 mm on the release sheet using a knife coater (clearance approximately 1 mm), and chopped strand pine (Asahi After the fiberglass (CM305, width 500mm) is laminated,
It passed through a zone of impregnated rolls and a movable plate, and was finally wound up onto a paper tube at a winding section with the release sheet facing outside. Roll the sheet around 10m each into a paper tube,
This was wrapped in kraft paper laminated with aluminum foil on the inside, and both ends were tightened with release rubber to prevent the styrene monomer in the material from scattering. This product was stored for 2 days in an air bath maintained at a temperature of 40°C to age and thicken. After taking it out and cooling it to room temperature, it was made into tapes with widths of 100 mm and 150 mm using a commercially available slitter (a machine whose roll surface has been treated with release properties).
It was wrapped around a paper tube core of the same width to a length of about 10 meters, and then stored and sealed in a cylindrical tin can.

このテープとして得られたシート状複合材製品
は厚さ約0.8mmで柔軟でかなりの粘着性を有する
ものであつた。材料に残留気泡はほとんど見られ
なかつた。
The sheet-like composite material product obtained as this tape had a thickness of about 0.8 mm, was flexible, and had considerable adhesiveness. Almost no residual air bubbles were observed in the material.

比較列 1 実施例1の複合積層物製造機の運転条件のう
ち、バイブレータを停止した以外すべて実施例1
と同一にして製造試験をした。
Comparison row 1 Among the operating conditions of the composite laminate manufacturing machine of Example 1, all conditions were as in Example 1 except that the vibrator was stopped.
A manufacturing test was carried out using the same method.

製造されたシート状材料を増粘した後、スリツ
トされる前に離型シートに重ねたまま約100mm平
方切りとり、残留気泡の状態の観察したところ、
かなりの気泡が認められた。
After thickening the produced sheet-like material, before slitting it, a square cut of approximately 100 mm was cut out while still stacked on a release sheet, and the state of the remaining air bubbles was observed.
Considerable air bubbles were observed.

応用例 1 実施例1で得られた幅150mmのシート状製品か
ら、150×150mm2のシートを5枚切りとつて、剥離
シートを取り去り、これを重ね合わせて、50トン
の圧縮成形機により温度160℃で2分間加工して、
200mm平方で厚さ約2mmの板を成形した。この板
に残留気泡および白化はまつたく見られなかつ
た。
Application example 1 Five sheets of 150 x 150 mm 2 were cut from the sheet-like product with a width of 150 mm obtained in Example 1, the release sheet was removed, the sheets were overlapped, and the sheets were heated at a temperature using a 50-ton compression molding machine. Processed at 160℃ for 2 minutes,
A plate of 200 mm square and approximately 2 mm thick was molded. No residual bubbles or whitening were observed on this board.

応用例 2 長さ1000mm、外径70mmの鉄製パイプの外表面を
ケレンがけした後、清浄にして、この上から実施
例1で得られた幅100mmのシート材料を、剥離シ
ートをはぎながら、1端を20mm重ね合わせて斜め
に巻きつけ、この上から剥離シートを介して手の
ひらで押えつけて、パイプ面とシート状材料とを
密着させて、この間に空気が残らないようにし
た。このものを温度160〜165℃に保つた空気恒温
槽中に3分入れた後、外に取り出した。
Application example 2 After the outer surface of a steel pipe with a length of 1000 mm and an outer diameter of 70 mm was scuffed and cleaned, the sheet material with a width of 100 mm obtained in Example 1 was placed on top of the pipe while peeling off the release sheet. The ends were overlapped by 20 mm and wrapped diagonally, and a release sheet was placed over this and pressed down with the palm of the hand to bring the pipe surface and the sheet-like material into close contact, so that no air remained between them. This product was placed in an air constant temperature bath maintained at a temperature of 160 to 165°C for 3 minutes, and then taken out.

パイプの外側に巻かれたFRP層はバーコール
硬度(934−1型以下同じ)が58で硬く、さらに
残留気泡や白化は認められなかつた。
The FRP layer wrapped around the outside of the pipe was hard with a Barcol hardness of 58 (same for 934-1 types and below), and no residual bubbles or whitening were observed.

実施例 2 ビニルエステル樹脂(エピビス型エポキシアク
リレート樹脂:リポキシ R802、昭和高分子製)
100部に対して無水フタル酸7.2部を混合し、100
〜110℃で90分反応させた。この変性ビニルエス
テル樹脂(約45%のスチレンとの混合液体)100
部に、光増感剤、2−ヒドロキシ−2−メチル−
1−フエニルプロパノン(ダロキユア 11173、
メルク製)を1部、増粘剤として酸化マグネシウ
ム(マグミツク 、協和化学工業製)1部を添加
し、この配合物をインテンシブミキサーで減圧撹
拌混合した。この液状樹脂混合物の粘度は15ポア
ズであつた。
Example 2 Vinyl ester resin (Epivis type epoxy acrylate resin: Lipoxy R802, manufactured by Showa Kobunshi)
Mix 7.2 parts of phthalic anhydride to 100 parts,
The reaction was carried out at ~110°C for 90 minutes. This modified vinyl ester resin (liquid mixed with about 45% styrene) 100
In part, photosensitizer, 2-hydroxy-2-methyl-
1-phenylpropanone (Darokyua 11173,
1 part of Magnesium oxide (Magmik, manufactured by Kyowa Kagaku Kogyo) was added as a thickener, and the mixture was stirred and mixed under reduced pressure using an intensive mixer. The viscosity of this liquid resin mixture was 15 poise.

実施例1と同様の機械と方法でシート状複合材
を製造し、2日間の増粘時間を経たのち、スリツ
ターで幅100mmのテープ状の製品を得た。製品は
約0.7mmの厚さの柔軟なシートで粘着性が高いも
のであつた。この製品中に残留する気泡はほとん
ど見られなかつた。
A sheet-like composite material was produced using the same machine and method as in Example 1, and after 2 days of thickening, a tape-like product with a width of 100 mm was obtained using a slitter. The product was a flexible sheet approximately 0.7 mm thick and highly adhesive. Almost no air bubbles remained in this product.

応用例 3 一部に赤錆びの見える厚さ3mmの平らな鉄板の
上面(約100×100mm2)がケレンがけして洗浄し、
この上に実施例2のビニルエステル樹脂(リポキ
シ R802)に2−ヒドロキシ−2−メチル−1
−フエニルプロパノンを1%添加した液をプライ
マーとしてはけ塗りし、さらにその上に実施例2
で製造したシート状材料を1枚100mm角に切り取
つて張り合わせて、圧着した。
Application example 3 The top surface of a 3 mm thick flat iron plate (approximately 100 x 100 mm 2 ) with some red rust visible was cleaned by scrubbing.
On top of this, 2-hydroxy-2-methyl-1 was added to the vinyl ester resin (Lipoxy R802) of Example 2.
- Brush a solution containing 1% phenylpropanone as a primer, and then apply Example 2 on top of that as a primer.
The sheet-like material manufactured by was cut into 100 mm square pieces, pasted together, and crimped.

市販の光照射装置(日照灯、SSL−250A、
100V、スタンレー電気製)を点灯して、シート
状材料面の上部10cmから垂直に照射した。照射時
間と共に硬化が進み、10分後のFRP層はバーコ
ール硬度が51、アドヒージヨンテスター(エルコ
メーター社)による剥離試験で接着強度が50Kg/
cm2で凝集破壊した。FRP層中に気泡はほとんど
見られなかつた。
Commercially available light irradiation equipment (sunlight, SSL-250A,
A 100 V (manufactured by Stanley Electric) was turned on and irradiated vertically from 10 cm above the surface of the sheet material. Curing progresses with the irradiation time, and after 10 minutes, the FRP layer has a Barcol hardness of 51 and an adhesion strength of 50 kg/kg in a peel test using an adhesion tester (Elcometer).
Cohesive failure occurred in cm2 . Almost no air bubbles were observed in the FRP layer.

比較例 2 原材料を実施例2と同一とし、製造装置および
条件を比較例1と同様にして、シート状のビニル
エステル樹脂複合材料を製造した。この材料を増
粘した後、幅100mmにスリツトし、これから100mm
平方のシートを切り取つて、応用例3と同様に光
照射して硬化させた。10分後のFRP硬化物中に
白化部が点在して認められた。
Comparative Example 2 A sheet-shaped vinyl ester resin composite material was manufactured using the same raw materials as in Example 2 and using the same manufacturing equipment and conditions as in Comparative Example 1. After thickening this material, slit it to a width of 100mm, and then
A square sheet was cut out and cured by irradiation with light in the same manner as in Application Example 3. After 10 minutes, scattered white areas were observed in the cured FRP product.

応用例 4 実施例4で得られたビニルエステル樹脂複合テ
ープ(幅100mm)を応用例2と同様にして鉄パイ
プに巻きつけた。このものを架台上約500mmの高
さに水平に保持して太陽光にあてた(場所−群馬
県伊勢崎市、日時−5月、午後2時)。架台の下
にアルミ板を置き太陽光が反射してパイプの裏面
にもあたるようにした。20分後裏面のFRP層も
ほぼ硬化した。FRP層の全面の目視した結果、
白下あるいは残留気泡は見当らなかつた。
Application Example 4 The vinyl ester resin composite tape (width 100 mm) obtained in Example 4 was wrapped around an iron pipe in the same manner as Application Example 2. This object was held horizontally on a pedestal at a height of about 500 mm and exposed to sunlight (location: Isesaki City, Gunma Prefecture, date and time: May, 2:00 p.m.). An aluminum plate was placed under the pedestal so that sunlight reflected and hit the back side of the pipe. After 20 minutes, the FRP layer on the back side was almost cured. As a result of visual inspection of the entire surface of the FRP layer,
No white spots or residual bubbles were found.

〔発明の効果〕〔Effect of the invention〕

本発明方法による成形用シート状樹脂複合材
は、これを金属、コンクリートまたはプラスチツ
ク製の構造物を成形物の外側あるいは内側に巻い
たり、張りつけたりした後、硬化することによつ
て、FRP表面層あるいはFRPライニング層を容
易に形成せしめることができるので、複合管の製
造や建築物、構造物の補強・防食性FRPライニ
ング施工の分野に、新規かつ有用な手法を提供で
きる一方、広くFRPのプリプレグとして各種の
中高圧成形法により、種々のFRP成形品を容易
かつ高品質に製造する有用なプロセスをも提供す
る。
The sheet-shaped resin composite material for molding according to the method of the present invention is produced by wrapping or pasting a structure made of metal, concrete, or plastic around the outside or inside of the molded product, and then hardening it to form an FRP surface layer. Alternatively, since the FRP lining layer can be easily formed, it can provide a new and useful method in the fields of composite pipe manufacturing and reinforcement/corrosion-proof FRP lining construction for buildings and structures. We also provide useful processes for easily and high-quality manufacturing of various FRP molded products using various medium-high pressure molding methods.

特に、巻きつけや貼りつけを含む無圧あるいは
低圧下の成形でも気泡を極少におさえ、これによ
り力学的・電気的強度の他、耐水性、耐食性、耐
候性が優れた成形物を与えることに本発明の成形
材料の実用的価値がある。
In particular, air bubbles can be kept to a minimum even during no-pressure or low-pressure molding, including wrapping and pasting, thereby providing molded products with excellent mechanical and electrical strength, as well as water resistance, corrosion resistance, and weather resistance. There is practical value of the molding material of the present invention.

【図面の簡単な説明】[Brief explanation of the drawing]

図は本発明のシート状樹脂複合材製造機の概略
図である。 1……チヨツプドストランドマツト、2……剥
離シート、3……ナイフコータ、4……バイブレ
ータ、5……可動板、6……含浸(筋)ロール、
7……巻き取りロール、8……液状樹脂。
The figure is a schematic diagram of a sheet-shaped resin composite manufacturing machine of the present invention. 1... Chopped strand mat, 2... Peeling sheet, 3... Knife coater, 4... Vibrator, 5... Movable plate, 6... Impregnated (stripe) roll,
7... Winding roll, 8... Liquid resin.

Claims (1)

【特許請求の範囲】[Claims] 1 定速で移動する剥離シートの上に、繊維基材
と液状樹脂を積層し、この積層物を複数本の含浸
用ロールで押圧することによつて含浸を行なつて
成形用シート状樹脂複合材を製造する方法におい
て、剥離シートの下側に接して、剥離シートの幅
以内の幅と、先端のロールから終端のロールまで
の長さ以内の長さをもつ方形で表面が平滑な板を
1枚、あるいは複数枚並べて、設け、この板に上
下の振動を与えることにより、上部の含浸用ロー
ルの積層物への押圧に脈動を与えることを特徴と
する成形用シート状樹脂複合材を製造する方法。
1. A fiber base material and a liquid resin are laminated on a release sheet that moves at a constant speed, and this laminate is impregnated by pressing with multiple impregnation rolls to form a sheet-shaped resin composite for molding. In the method of manufacturing the material, a rectangular smooth-surfaced plate with a width within the width of the release sheet and a length within the length from the tip roll to the end roll is placed in contact with the underside of the release sheet. Manufactures a sheet-like resin composite material for molding characterized by providing one sheet or a plurality of sheets side by side and applying vertical vibration to this sheet to give pulsations to the pressure of the upper impregnating roll on the laminate. how to.
JP21223885A 1985-09-27 1985-09-27 Manufacture of molding sheet-shaped resin composite material Granted JPS6273916A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21223885A JPS6273916A (en) 1985-09-27 1985-09-27 Manufacture of molding sheet-shaped resin composite material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21223885A JPS6273916A (en) 1985-09-27 1985-09-27 Manufacture of molding sheet-shaped resin composite material

Publications (2)

Publication Number Publication Date
JPS6273916A JPS6273916A (en) 1987-04-04
JPH0579485B2 true JPH0579485B2 (en) 1993-11-02

Family

ID=16619253

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21223885A Granted JPS6273916A (en) 1985-09-27 1985-09-27 Manufacture of molding sheet-shaped resin composite material

Country Status (1)

Country Link
JP (1) JPS6273916A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102011005462B8 (en) 2011-03-11 2012-10-11 Thermoplast Composite Gmbh Method and device for producing a fiber composite material in the form of a fiber-impregnated with a polymer sliver

Also Published As

Publication number Publication date
JPS6273916A (en) 1987-04-04

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