JPS59167230A - Preparation of molded material - Google Patents
Preparation of molded materialInfo
- Publication number
- JPS59167230A JPS59167230A JP58042044A JP4204483A JPS59167230A JP S59167230 A JPS59167230 A JP S59167230A JP 58042044 A JP58042044 A JP 58042044A JP 4204483 A JP4204483 A JP 4204483A JP S59167230 A JPS59167230 A JP S59167230A
- Authority
- JP
- Japan
- Prior art keywords
- mold
- resin
- roller
- molding
- fiber
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Moulding By Coating Moulds (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は繊維強化熱硬化性樹脂(以下FRP)筒状成形
物の製造法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for manufacturing a fiber-reinforced thermosetting resin (hereinafter referred to as FRP) cylindrical molded article.
FRP筒状成形物の低速回転成形は、特開昭54−11
1577により提案されている。即ち円筒の型が回転軸
方向に動くことなく、しかもFRP成形用材料供胎部が
相対釣に移動できるように片持式梁体に摺動部を設けた
装置を用い、該型を1〜4 rpm (周速5〜10r
rL/分)で回転サセ、型ノ回転軸方向と平行に抑圧ロ
ーラーを設置し、型の回転と抑圧ローラー回転を駆動部
よりチェーン、ホイールを用いて同調回転させ、かつ抑
圧ローラーをエアーシリンダーにより上下動させ、すな
わち押圧したり抑圧を解除したりして調節しながら強化
材に樹脂を含浸させ、脱泡させる成形方法が提案されて
いる。Low-speed rotary molding of FRP cylindrical moldings is described in Japanese Patent Application Laid-open No. 54-11.
1577. That is, using a device in which a sliding part is provided on a cantilever beam body so that the cylindrical mold does not move in the direction of the rotation axis and the FRP molding material delivery part can move relative to each other, the mold is 4 rpm (peripheral speed 5~10r
rL/min), a suppression roller is installed parallel to the rotation axis direction of the mold, the rotation of the mold and the rotation of the suppression roller are synchronously rotated from the drive unit using a chain and a wheel, and the suppression roller is rotated by an air cylinder. A molding method has been proposed in which the reinforcing material is impregnated with resin and defoamed while adjusting the reinforcing material by moving it up and down, that is, by pressing or releasing pressure.
しかし、この成形方法は成形材料の供給装置及び抑圧ロ
ーラーが片持式梁体の側面のガイドレールに沼って移動
するため該梁体に働く曲げモーメントが変化し、それに
よって梁体にたわみが生じる。このす知みは片持式梁体
に設置されたガイドレールに連結された抑圧ローラーの
水平を保つことかできなくなり、成形の際に厚みむら、
抑圧ローラーへの成形材料のからみつきを生じる。However, in this forming method, the molding material supply device and the suppression roller move along the guide rails on the side of the cantilevered beam, which changes the bending moment acting on the beam, which causes the beam to deflect. arise. This knowledge makes it impossible to keep the suppression roller connected to the guide rail installed on the cantilever beam body horizontally, resulting in uneven thickness and
This causes the molding material to become entangled with the suppression roller.
又、この方法では材料供給装置を材料の供給を停止した
状態で最先端より最後尾に移動する場合繊維強化材が該
装置上でカッターで切断される前は長繊維であるためた
るんでしまい作り0部にからみついたり型面に接触した
りする問題が発生する。又、液状熱硬化性樹脂の移送導
管を伸縮自在の構造とする必要から導管内の洗浄が不完
全となる。しかも、構造が複雑となるため導管の本数に
制限がでてくる。In addition, in this method, when the material supply device is moved from the leading end to the rear end with the material supply stopped, the fiber reinforcement material is long fibers before being cut with a cutter on the device, so it becomes sagging. Problems such as getting entangled with the part 0 or coming into contact with the mold surface occur. Furthermore, since the conduit for transporting the liquid thermosetting resin needs to have a telescopic structure, the inside of the conduit cannot be completely cleaned. Moreover, since the structure is complicated, the number of conduits is limited.
更に、この方法は抑圧ローラーがチンヴi動により円筒
型の回転と同調回転させるため型を真円形状としなけれ
ばならす、楕円、欠円、多角等の真円以外の形状の成形
物の製造には適さない。しかも抑圧ローラーを型と同調
回転させるため成形材料がローラーにからみついた場合
に成形を困難にする欠点がある。Furthermore, this method requires the mold to be perfectly circular because the suppression roller rotates in synchronization with the rotation of the cylindrical mold by means of a chimney motion, and is suitable for manufacturing molded products with shapes other than perfect circles, such as ellipses, missing circles, and polygons. is not suitable. Moreover, since the suppression roller is rotated in synchronization with the mold, there is a drawback that molding becomes difficult if the molding material becomes entangled with the roller.
本発明者らは、かかる欠点な改善するために鋭意研究し
た結果、本発明に至った。The present inventors conducted extensive research to improve these drawbacks, and as a result, they arrived at the present invention.
即ち、本発明は重力の2倍より小さい遠心力で回転し、
かつ軸方向に往復移動する筒状型の内壁面に繊維強化材
及び液状熱硬化性樹脂を該型内空間に位置する片付式梁
体に固定された繊維強化材供給装置及び液状熱硬化性樹
脂供給装置により供給し、次いで上記片持式梁体に固定
され自在に回転する少なくとも1個の抑圧ローラーで上
dシ強化材及び樹脂を押圧して含浸、脱厄させることを
特徴とづ−る成形物の製造方法を提供する。That is, the present invention rotates with a centrifugal force less than twice the gravity,
A fiber reinforcing material supply device and a liquid thermosetting resin are fixed to a detachable beam body located in the mold interior space, and a fiber reinforcing material supplying device and a liquid thermosetting resin are applied to the inner wall surface of a cylindrical mold that reciprocates in the axial direction. The resin is supplied by a resin supply device, and then the upper reinforcing material and the resin are pressed by at least one press roller fixed to the cantilever beam body and freely rotated to impregnate and remove dirt. A method for manufacturing a molded article is provided.
本発明では片持式梁体に繊維強化材供給装置、液状熱硬
化性樹脂供給装置及び抑圧ローラー装置4を固定するこ
とにより片持式梁体の構造を簡略化することができ、し
かもかかる梁体の長さを大きくすることができる。これ
により長尺物のFRP筒状成形物を製造することが可能
となる。又各供給装置に繊維強化材、液状熱硬化性樹脂
を移送する各導管が固定化でき、その伸縮自在の機構が
不要になり、加えて太幅な軽量化を図ることができる。In the present invention, the structure of the cantilever beam can be simplified by fixing the fiber reinforcement supply device, the liquid thermosetting resin supply device, and the suppression roller device 4 to the cantilever beam. Can increase body length. This makes it possible to manufacture a long FRP cylindrical molded product. In addition, each conduit for transferring the fiber reinforcement material and liquid thermosetting resin to each supply device can be fixed, eliminating the need for an expandable mechanism, and in addition, it is possible to significantly reduce the weight.
尚、液状熱硬化性樹脂供給装置は吐出口直前又は直後で
混合する機構とすることができるため触媒、促進剤等の
混合が完全に行ないうろことができる。Incidentally, since the liquid thermosetting resin supply device can have a mechanism for mixing just before or after the discharge port, the catalyst, accelerator, etc. can be completely mixed.
本発明に用いられる筒状型は図−1に示すごとく少なく
とも2個以上に開閉できるようにし締め付はボルトにて
一体筒状となるものが好ましい。型の回転は例えばモー
ターで駆動された複敬個の伝動ローラーにより芙施され
る。筒状型の回転速度は重力の2倍より小さい遠心力と
なるような速度である。例えば直径2rrLの筒状型で
あれば30 rp、m。The cylindrical mold used in the present invention is preferably one that can be opened and closed in at least two parts, as shown in FIG. 1, and is tightened into an integral cylindrical shape using bolts. The mold is rotated, for example, by multiple transmission rollers driven by a motor. The rotational speed of the cylindrical mold is such that the centrifugal force is less than twice the force of gravity. For example, if it is a cylindrical type with a diameter of 2rrL, it is 30 rp, m.
以下の回転速度となる。又、筒状型は例えはガイドレー
ルに泪って筒状型移動装置によって型の軸方向に0〜2
0m/分の範囲の速度で定速度又は可速度で往復移動で
き、しかも型自体を例えばガイドレールにより前後に反
転でき、文型の回転も左右両方の回転ができる6M4に
のものが用いられる。The rotation speed is as follows. In addition, the cylindrical mold is moved in the axial direction of the mold from 0 to 2 by the cylindrical mold moving device, for example, while lying on the guide rail.
A 6M4 type is used, which can reciprocate at a constant speed or at a variable speed in the range of 0 m/min, and also allows the mold itself to be reversed back and forth using, for example, a guide rail, and the sentence pattern can be rotated both left and right.
尚、型の軸方向の移動は車輪の駆動でも良くチt、ワイ
ヤー、歯車等の駆動であっても良い。Incidentally, the axial movement of the mold may be driven by wheels, or may be driven by wheels, wires, gears, or the like.
繊維強化材供給装置は例えは図−2に示すごとくゴムロ
ーラーにより繊維強化材、例えはひも状のものを導き移
送しゴムローラーと放射線状に剪断刃を有する剪断刃ロ
ーラーにより構成され剪断刃ローラーの作動、解除によ
り繊維強化材を切断して供給したり、又は図−2に於い
て剪断刃ローラーを剪断刃を有していないローラーに代
えて繊維強化材をひも状の状態で供給できろ機構乞有す
るものが用いられる。供給量を自由に選択し、ひも状で
供給する場合は周速と同調させて周方向に平行スルスパ
イラル状に供給するか、或いはそれ以上の速度でランダ
ムループ状で供給することかできる。As shown in Figure 2, the fiber reinforcement supply device guides and transports the fiber reinforcement material, for example a string-like material, using a rubber roller, and is composed of a rubber roller and a shearing blade roller having radial shearing blades. The fiber reinforced material can be cut and supplied by activation and release, or the fiber reinforced material can be supplied in the form of a string by replacing the shearing blade roller with a roller without shearing blades in Figure 2. What the organization has is used. The amount of supply can be freely selected, and when it is supplied in the form of a string, it can be supplied in parallel spirally in the circumferential direction in synchronization with the circumferential speed, or it can be supplied in a random loop at a higher speed.
又これらを組合せて供給しても艮い。It is also permissible to supply a combination of these.
液状熱硬化性樹脂供給装置は例えは図−4に示すごとく
液状熱硬化性樹脂、硬化触媒等を筒状型の内壁面に供給
するまでに混合するものであり、好ましくは液状熱硬化
性樹脂吐出口直前または直後で混合することができるも
のである。The liquid thermosetting resin supply device mixes the liquid thermosetting resin, curing catalyst, etc. before supplying it to the inner wall surface of the cylindrical mold, as shown in Figure 4, and preferably the liquid thermosetting resin It can be mixed immediately before or after the discharge port.
この装置について液状熱硬化性樹脂として不飽和ポリエ
ステル樹脂を用いた場合の供給方法を述べる。不飽和ポ
リエステル樹脂と促進剤、例えば6%ナフテン酸コノ4
ル)f添加混合したものなポンプでラインミキサーに移
送する。A method of supplying this device when unsaturated polyester resin is used as the liquid thermosetting resin will be described. Unsaturated polyester resin and accelerator, e.g. 6% naphthenic acid
1) Transfer the mixture to a line mixer using a pump.
又、別ラインで触媒例えば55%メチルエチルケトンノ
(−オキサイド(MEKPO)Qポンプでラインミキサ
ーに移送する。両者をラインミキサーにより混合し吐出
口より吐出供給する。その吐出口は両端の閉じたノくイ
ブ下面に細孔な持ちシャワー状に吐出されるものか望ま
しいか、スリット状、霧状に吐出されるものでも良い。In addition, in another line, a catalyst such as 55% methyl ethyl ketone (-oxide (MEKPO)) is transferred to a line mixer using a Q pump. Both are mixed by a line mixer and discharged from a discharge port. It is preferable to have pores on the bottom surface of the tube so that it is discharged in the form of a shower, or it may be discharged in the form of slits or mist.
不飽和ポリエステル樹脂及び55%MEKPOを移送す
るポンプは通常足敏ポンプが用いられ、その際の移送比
ば100:0.2ないし100:5のものでギヤ一式、
エアーポンプ式、圧送式のいずれでも艮い。The pump to transfer unsaturated polyester resin and 55% MEKPO is usually a foot pump, with a transfer ratio of 100:0.2 to 100:5, a set of gears,
Either air pump type or pressure feeding type is available.
又、不飽和ポリエステル樹脂、促進剤、触媒の6者をそ
れぞれ別のラインで移送して2個のラインミキサー(C
より混合、供給しても艮い。In addition, the unsaturated polyester resin, accelerator, and catalyst are transferred through separate lines, and two line mixers (C
It's okay to mix and supply more.
抑圧ローラーは例えは図−4(IC示すごとく回転型に
強制的に同調することなく自在に回転し、自重による押
圧力により樹脂を強化材に含浸せしめ、成形材料中の泡
を脱泡せしめることができるものであり、自白に運り山
できる様にクランクな少なくとも1個設けたもρが好ま
しい。For example, as shown in Figure 4 (IC), the suppression roller rotates freely without being forced to synchronize with the rotating mold, impregnates the reinforcing material with resin by the pressing force of its own weight, and defoams the bubbles in the molding material. It is preferable to provide at least one crank so that it can be carried forward.
このような抑圧ローラーとしては2Kftがローラーの
長さ1cIrL当950〜400Iで、その長さが成形
物の長さに対応して自由に選択でき、通常10〜1[1
0αの範囲のものが好適である。又、その直径は回転に
支障のない寸法であれば良く、5〜40IIImの範囲
が好ましい。尚、抑圧ローラーはエアーシリンダーにて
上下できる機構を持ったものが好ましく、通常3本以上
、各ロール間隔1〜50cIIL、好ましくは5〜20
cWL程度で用いられる。For such a suppression roller, 2 Kft is 950 to 400 I per 1 cIrL of roller length, and the length can be freely selected according to the length of the molded product, and usually 10 to 1 [1
A range of 0α is preferable. Further, its diameter may be any size that does not hinder rotation, and is preferably in the range of 5 to 40 m. It should be noted that the suppression rollers preferably have a mechanism that can be moved up and down using an air cylinder, and there are usually three or more rollers, with an interval of 1 to 50 cIIL between each roll, preferably 5 to 20 cIIL.
It is used at about cWL.
本発明に用いられる葎維強化材とはガラス繊維、カーボ
ン繊維、アラミド繊維(ケブラー繊維、テユボン社製)
等の一般公知の繊維強化材を用いることができ、好まし
くはガラス繊維である。又、この繊維の形態はマット状
、テープ状、ロービング状(糸状)或いはロービング状
のものを適当な長さ、好ましくは12〜75mmに切断
したチョップストランド状が適当であり、笑にこれらの
組合せで構成することも可能である。尚、繊維強化材の
成形物中含有量は10〜80重量%、好ましくは20〜
60重量%の範囲が適する。The seedling fiber reinforcement used in the present invention is glass fiber, carbon fiber, aramid fiber (Kevlar fiber, manufactured by Teyubon)
Generally known fiber reinforcing materials such as the like can be used, and glass fiber is preferable. The suitable form of this fiber is mat, tape, roving (thread), or chopped strands obtained by cutting the roving into appropriate lengths, preferably 12 to 75 mm, and combinations thereof. It is also possible to configure The content of the fiber reinforcing material in the molded product is 10 to 80% by weight, preferably 20 to 80% by weight.
A range of 60% by weight is suitable.
本発明に用いられる液状熱硬化性樹脂とは不飽和ポリエ
ステル樹脂、ビニルエステル樹脂、エポキシ樹脂、フェ
ノール樹脂等一般公知の液状熱硬化性樹脂を用いること
ができ、好ましくは不飽和ポリエステル樹脂あるいはビ
ニルエステル樹脂が用いられる。液状熱硬化性樹脂の粘
度は通常0.5〜20ポイズ(ブルックフィールド粘度
)、好ましくは2〜20ポイズの範囲である。The liquid thermosetting resin used in the present invention can be a generally known liquid thermosetting resin such as unsaturated polyester resin, vinyl ester resin, epoxy resin, or phenol resin, and preferably unsaturated polyester resin or vinyl ester resin. Resin is used. The viscosity of the liquid thermosetting resin is usually in the range of 0.5 to 20 poise (Brookfield viscosity), preferably 2 to 20 poise.
尚、液状熱硬化性樹脂として不飽和ポリエステル樹脂又
はビニルエステル樹脂を用いる場合、構成成分として不
飽和ポリエステル又はビニルエステルにスチレン、メチ
ルメタクリレート等のビニル単量体カー混合されて用い
られる。When an unsaturated polyester resin or a vinyl ester resin is used as the liquid thermosetting resin, a vinyl monomer such as styrene or methyl methacrylate is mixed with the unsaturated polyester or vinyl ester as a constituent component.
又、これらの樹脂にナフテンはコバルト、オクデン鹸コ
バルト、ナフテン酸鉛、オクテノ醒鉛等の硬化助剤な予
め癌加しても良い。勿論、回転型に樹脂を供給する際に
添加しても艮い。Further, naphthene may be added to these resins in advance with a curing aid such as cobalt, octene cobalt, lead naphthenate, or octenolead. Of course, it may also be added when supplying the resin to the rotary mold.
次いで、本発明の製造方法を装置によって説明する。Next, the manufacturing method of the present invention will be explained using an apparatus.
図−1は、成形材料供給部、抑圧ロール等が型体の回転
軸方向に移動しないように設置され、型体が該回転軸方
向に移動し得る成形装置り一例である。この装置では、
円筒状の成形用型体Aがモーター2の駆動を伝えるロー
ラー5によって回転される。片持式梁体Bに設けられた
成形材料供給装置及び抑圧ロールの取付は部Cから樹脂
及び繊維強化材が回転する型内面に供給され、供給直後
押圧ローラーDで押圧される。その際、成形用型体Aは
、成形材料供給装置及び押圧ロールの取付は部Cカ・ら
成形材料が供給されるに従って前又は後に可動して成形
を進める。又、成形型体Aの回転及び前後の移動は各変
速機3及び6で速度が適宜選択される。FIG. 1 shows an example of a molding apparatus in which a molding material supply section, a pressing roll, etc. are installed so as not to move in the direction of the rotation axis of the mold, and the mold can move in the direction of the rotation axis. With this device,
A cylindrical molding die A is rotated by a roller 5 that transmits the drive of a motor 2. To attach the molding material supply device and the pressure roll provided on the cantilever beam B, resin and fiber reinforcing material are supplied from part C to the rotating inner surface of the mold, and immediately after being supplied, they are pressed by a pressure roller D. At this time, the molding mold body A is mounted with a molding material supply device and a press roll and is moved forward or backward as the molding material is supplied from the part C to proceed with molding. Further, the speeds of the rotation and back and forth movement of the mold body A are appropriately selected by the respective transmissions 3 and 6.
本発明によれば材料供給部、片持式梁体をコンパクトに
することかでき大口径から小口径のしかも長いFRP筒
状成形物を得ることができ、更に異形管の製造も可能と
なる。According to the present invention, it is possible to make the material supply section and the cantilever beam body compact, and it is possible to obtain a long FRP cylindrical molded product having a large diameter to a small diameter, and it is also possible to manufacture irregularly shaped pipes.
又、繊維強化材例えばガラスロービングを切断せずに供
給することもでき、高強度のFRP筒状成形物を得るこ
とができる。更に、液状熱硬化性樹脂と硬化触媒との混
合も完全であるため色むらのないFRP筒状成形物が得
られる。Furthermore, a fiber reinforced material such as glass roving can be supplied without being cut, and a high-strength FRP cylindrical molded product can be obtained. Furthermore, since the liquid thermosetting resin and the curing catalyst are completely mixed, an FRP cylindrical molded product with no uneven color can be obtained.
本発明な実施例により説明する。The present invention will be explained using an example.
実施例 1
成形用型体Aの大きさが内径1.8m、長さ6mである
図−1に示す如き製造装置にて芙施した。Example 1 Molding was carried out using a manufacturing apparatus as shown in FIG. 1, in which the mold body A had an inner diameter of 1.8 m and a length of 6 m.
長さ3.5障の片持式梁体Bのほば先端部に設置された
繊維強化材供給装置によりガラス繊維8本(ガラスロー
ビング5P−3、旭ファイバー製)¥長さ50罪のチョ
ップストランド状に切断し4給/分の吐出蓋で供給し、
次いで各ポンプで移送された不飽和ポリエステル樹脂(
ポリライトFB、−105(犬日本インキ化学工某社製
)100重量部+6%ナフテン酸コバルトo、4i量部
)及び触媒(55%MEKPO)を樹脂100重量部に
対して触媒1.0重量部の割合で混合し、液状熱硬化性
樹脂供給装置によりシャワー状にs h/分の吐出量で
ガラス繊維の上に供給した。その後、6本の抑圧ローラ
ーでその上を押圧して含浸、脱泡せしめて、連続的に成
形し、約3m成形された時点でガラス繊維及び樹脂の供
給を止めて一担成形用型体Aを片持式梁体Bと引き離し
た。その型体Aを前後に反転させ、上記梁体Bが型体A
内に入るように該型体を移動させて、上記と同様にして
先に成形したものにつづけて成形して長さ75m。Eight glass fibers (Glass Roving 5P-3, manufactured by Asahi Fiber) were chopped with a length of 50 by the fiber reinforcement supply device installed at the tip of the cantilever beam B with a length of 3.5 mm. Cut it into strands and feed it with a discharge lid at a rate of 4 feeds/minute.
The unsaturated polyester resin (
Polylite FB, -105 (manufactured by Inu Nippon Ink Kagaku Kogyo Co., Ltd.) 100 parts by weight + 6% cobalt naphthenate O, 4i parts) and a catalyst (55% MEKPO) in a proportion of 1.0 parts by weight of catalyst per 100 parts by weight of resin. The mixture was mixed in proportions and fed onto the glass fibers in a shower at a discharge rate of sh/min using a liquid thermosetting resin feeder. After that, the top is pressed with six pressure rollers to impregnate and defoam, and it is continuously molded. When about 3 m is molded, the supply of glass fiber and resin is stopped and mold A for single-layer molding is formed. was separated from cantilever beam body B. Flip the mold body A back and forth, so that the beam body B becomes the mold body A.
The mold was moved so as to fit inside the mold, and the mold was molded in the same manner as above, following the previous mold, to a length of 75 m.
厚さ9Mの筒状成形物を製造した。この成形物の物性を
表−1に示す。尚、各抑圧ローラーは直径15cWL、
長さ60儂、重さ10釉であり、各ローラー間隔は10
αである。A cylindrical molded product with a thickness of 9M was manufactured. Table 1 shows the physical properties of this molded product. In addition, each suppression roller has a diameter of 15 cWL,
The length is 60 degrees, the weight is 10 degrees, and the distance between each roller is 10 degrees.
It is α.
実施例 2
図−1に示す内巻回転成形法式製造装置を用い直径2.
8m、長さ6mの筒状型Aを2.8 r、p、m、の回
転数(周速24.6m/分)で回転させ軸方向にols
m7分の一定速度で往復移動させ実施例1と同様の供給
条件で成形し、厚み3mm、長さ7.mで成形された時
点でガラス繊維をチョツプドストランド状にしないで長
繊維、即ちロービング状でランダムに連続的に供給し、
厚さ3間に成形した。伏いて、その上に再度チョツプド
ストランド状のガラス繊#乞供給し、実施例1と同様に
して岸さ3朋に成形して長さ3m、厚さ9罪の筒状成形
物が得られた。この成形物の物性な表−1に示す。Example 2 Diameter 2.
The cylindrical mold A, which is 8 m long and 6 m long, is rotated at a rotation speed of 2.8 r, p, m (peripheral speed 24.6 m/min) and ols is rotated in the axial direction.
It was moved reciprocatingly at a constant speed of 7 m and was molded under the same supply conditions as in Example 1, with a thickness of 3 mm and a length of 7. At the time of molding, the glass fibers are not made into chopped strands, but are continuously supplied randomly in the form of long fibers, that is, in the form of rovings,
It was molded to a thickness of 3 mm. The glass fibers in the form of chopped strands were again supplied on top of the glass fibers, and the glass fibers were molded in the same manner as in Example 1 to obtain a cylindrical molded product with a length of 3 m and a thickness of 9 cm. It was done. The physical properties of this molded product are shown in Table 1.
表−1Table-1
図−1は本発明で用いられる、成形材料供給部が片持式
梁体に固定され、しかも円筒状型体が前後に移動するこ
とができる回転成形装置の部分破断正面図である。図−
2は繊維強化材の供給装置を示す部分図である。図−3
は液状熱硬化性樹脂の供給装置の概略図である。又、図
−4は片持式梁体に取り付けられた成形材料供給装置及
び抑圧ローラーの状態を示す部分図である。
A・・・・・・・・・成形用型体、 B・・・・・・
・・・片持式梁体、C・−・・−・・・・成形材料供給
装置及び抑圧ローラーの取付q部、D・・・・−・・・
・押圧ローラー
ド・・・−・・・・ガイドレール、 2・・・・−・・
・・モーター、6・−・・−・・・・変 速 機、
4・−・・・・・・・チェーン、5・・・・・・・・・
モーター、 6・−・・・・・・・変速機、7−・・
・・・・・・ベ ル ト、 8・−・・−・・・・
伝導ローラー、9・・・・・・・・・蝶 瘤 部、
1o・・・・・・・−・移動用車輪、11・・・・−・
・・・繊m強化s、 12・・・・・・・・・ゴムロ
ーラー、13・・・・・・・・・強化材ロッカー、14
・・・・・・・・・モーター、15・・・・・・・・・
ベ ル ト、 16・・・・・曲g叡#飾化口°供給
口、17・・・・・・・・−エアーシリンダー、18・
曲・液状樹脂タンク、19・・・・・・・・・触媒タン
ク、 20・・甲・トランスファーポンプ、21・
・・・・・・・・開閉バルブ、22・・・・・・・・・
ラインミキサー、26・・・・−・・・・樹脂液吐出装
置、24曲・甲・エアーシリンダー、25・・・・・・
・・・ア − ム、 26−・・・曲クランク、2
7・−・・・・・・・押圧ローラー軸受、28・−中・
抑圧ローラー軸棒図−2
+1
・11.−ノー
図−3FIG. 1 is a partially cutaway front view of a rotary molding apparatus used in the present invention, in which a molding material supply section is fixed to a cantilevered beam body and a cylindrical mold body can move back and forth. Figure-
2 is a partial view showing a fiber reinforcement supply device. Figure-3
FIG. 1 is a schematic diagram of a liquid thermosetting resin supply device. Moreover, FIG. 4 is a partial view showing the state of the molding material supply device and the suppression roller attached to the cantilever beam body. A・・・・・・Mold body for molding, B・・・・・・
・・・Cantilever beam body, C・・・・・・Moving material supply device and suppression roller mounting part q, D・・・・・・・・・・
・Press roller...--Guide rail, 2...--...
・・Motor, 6・−・・−・・・Transmission,
4・−・・・・・・・Chain, 5・・・・・・・・・
Motor, 6--...Transmission, 7--...
...Belt, 8...
Conduction roller, 9... Butterfly knob part,
1o・・・・・Moving wheels, 11・・・・・・・
...Fiber m reinforcement s, 12...Rubber roller, 13...Reinforcement locker, 14
・・・・・・・・・Motor, 15・・・・・・・・・
Belt, 16...Crack #Decoration port ° Supply port, 17...-Air cylinder, 18.
Curved/Liquid resin tank, 19... Catalyst tank, 20... Instep/Transfer pump, 21...
・・・・・・・・・Opening/closing valve, 22・・・・・・・・・
Line mixer, 26...--Resin liquid discharge device, 24 pieces/instep/air cylinder, 25...
...Arm, 26-...Crank crank, 2
7.-- Press roller bearing, 28.- Medium.
Suppression roller shaft diagram-2 +1 ・11. -No diagram-3
Claims (1)
復移動が可能な筒状型の内壁面に線維強化材及び液状熱
硬化性樹脂を、該型内空間に位置する片持式梁体に固定
された繊維強化材供給装置により供給し、次いで上記片
持式梁体に固定され自在に回転する少なくとも1個の押
圧ローラーで上記強化材及び樹脂を押圧して含浸、脱泡
せしめることからなる成形物の製造方法。A cantilevered beam positioned in the inner space of a cylindrical mold that rotates with a centrifugal force less than twice the force of gravity and is capable of reciprocating in the axial direction, with a fiber reinforced material and a liquid thermosetting resin on the inner wall surface of the mold. The reinforcing material is supplied by a fiber reinforcing material supplying device fixed to the body, and then the reinforcing material and resin are pressed by at least one press roller fixed to the cantilever beam body and freely rotated to impregnate and defoam. A method for producing a molded article consisting of:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58042044A JPS59167230A (en) | 1983-03-14 | 1983-03-14 | Preparation of molded material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58042044A JPS59167230A (en) | 1983-03-14 | 1983-03-14 | Preparation of molded material |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59167230A true JPS59167230A (en) | 1984-09-20 |
JPH0585344B2 JPH0585344B2 (en) | 1993-12-07 |
Family
ID=12625124
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58042044A Granted JPS59167230A (en) | 1983-03-14 | 1983-03-14 | Preparation of molded material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59167230A (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5186573A (en) * | 1975-01-24 | 1976-07-29 | Kubota Ltd |
-
1983
- 1983-03-14 JP JP58042044A patent/JPS59167230A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5186573A (en) * | 1975-01-24 | 1976-07-29 | Kubota Ltd |
Also Published As
Publication number | Publication date |
---|---|
JPH0585344B2 (en) | 1993-12-07 |
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