JPS5935766B2 - Molding method of fiber reinforced plastic pipe - Google Patents
Molding method of fiber reinforced plastic pipeInfo
- Publication number
- JPS5935766B2 JPS5935766B2 JP50056861A JP5686175A JPS5935766B2 JP S5935766 B2 JPS5935766 B2 JP S5935766B2 JP 50056861 A JP50056861 A JP 50056861A JP 5686175 A JP5686175 A JP 5686175A JP S5935766 B2 JPS5935766 B2 JP S5935766B2
- Authority
- JP
- Japan
- Prior art keywords
- tape
- resin
- fibers
- reinforced plastic
- plastic pipe
- 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
- 238000000034 method Methods 0.000 title claims description 13
- 229920002430 Fibre-reinforced plastic Polymers 0.000 title claims description 4
- 239000011151 fibre-reinforced plastic Substances 0.000 title claims description 4
- 238000000465 moulding Methods 0.000 title description 10
- 229920005989 resin Polymers 0.000 claims description 49
- 239000011347 resin Substances 0.000 claims description 49
- 239000000835 fiber Substances 0.000 claims description 20
- 239000004744 fabric Substances 0.000 claims description 11
- 229910052751 metal Inorganic materials 0.000 claims description 11
- 239000002184 metal Substances 0.000 claims description 11
- 238000010438 heat treatment Methods 0.000 claims description 10
- 229920001187 thermosetting polymer Polymers 0.000 claims description 9
- 229920005992 thermoplastic resin Polymers 0.000 claims description 4
- 229920002678 cellulose Polymers 0.000 description 15
- 239000001913 cellulose Substances 0.000 description 15
- -1 polyethylene terephthalate Polymers 0.000 description 9
- 238000009826 distribution Methods 0.000 description 8
- 229920000139 polyethylene terephthalate Polymers 0.000 description 7
- 239000005020 polyethylene terephthalate Substances 0.000 description 7
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 6
- 238000004804 winding Methods 0.000 description 6
- 238000001879 gelation Methods 0.000 description 5
- 239000003365 glass fiber Substances 0.000 description 5
- 239000003822 epoxy resin Substances 0.000 description 4
- 229920000647 polyepoxide Polymers 0.000 description 4
- 229920000049 Carbon (fiber) Polymers 0.000 description 3
- 239000004760 aramid Substances 0.000 description 3
- 229920003235 aromatic polyamide Polymers 0.000 description 3
- 239000004917 carbon fiber Substances 0.000 description 3
- 239000002759 woven fabric Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000005011 phenolic resin Substances 0.000 description 2
- 229920006267 polyester film Polymers 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- PAOHAQSLJSMLAT-UHFFFAOYSA-N 1-butylperoxybutane Chemical compound CCCCOOCCCC PAOHAQSLJSMLAT-UHFFFAOYSA-N 0.000 description 1
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 description 1
- 229920002292 Nylon 6 Polymers 0.000 description 1
- 229920002302 Nylon 6,6 Polymers 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- 229920001568 phenolic resin Polymers 0.000 description 1
- 239000011295 pitch Substances 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920001225 polyester resin Polymers 0.000 description 1
- 239000004645 polyester resin Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 150000005846 sugar alcohols Polymers 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 229920006337 unsaturated polyester resin Polymers 0.000 description 1
- 230000037303 wrinkles Effects 0.000 description 1
Landscapes
- Moulding By Coating Moulds (AREA)
Description
【発明の詳細な説明】
本発明は繊維強化プラスチック(以下FRPという)パ
イプの成形法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for forming fiber reinforced plastic (hereinafter referred to as FRP) pipes.
従来、FRPパイプの一成形法として、ガラス繊維、カ
ーボン繊維、あるいは芳香族ポリアミド繊維等にエポキ
シ樹脂、不飽和ポリエステル樹脂あるいはフェノール樹
脂等の熱硬化性樹脂を含浸させ半硬化状態としたプリプ
レグシート又はクロス(交織も含む)を、芯金に巻付け
て積層し、この積層物の表面に更にセルロース系テープ
をヘリカルに巻きつけて加熱硬化し、冷却後芯金を抜き
取り、テープをはぎとる方法が知られている。Conventionally, one method for forming FRP pipes is to impregnate glass fibers, carbon fibers, or aromatic polyamide fibers with thermosetting resins such as epoxy resins, unsaturated polyester resins, or phenol resins to create a semi-cured prepreg sheet or There is a method in which cloth (including mixed weaves) is wrapped around a core metal and laminated, a cellulose tape is further wrapped helically around the surface of this laminate, heated and hardened, and after cooling, the core metal is removed and the tape is peeled off. It is being
しかしながらセルロース系テープを使用するこの成形法
においては、細心の取扱いと硬化条件等の設定下におい
ても、加熱による熱硬化性樹脂の粘度低下による外表面
への多量の樹脂フロー、又積層の芯金からの移動又は脱
落等が起こり易く、更には成形物の長手方向に部分的に
繊維の蛇行が発生する。かかる現象は成形物中に樹脂の
偏在およびボードを発生させ、繊維の蛇行が成形物に外
力が加わつた場合、その部分で破損に至らしめる危険性
を有する。更に、セルロース系テープは、その硬化温度
条件下では完全に劣化し、その上硬化樹脂との剥離性が
悪いためにそのはぎ取りには回転金属プラン等を用いね
ばならず、成形物表面を粗雑にし、塗装等の仕上加工を
必要とする。本発明者らは従来のセルロース系テープを
使用する成形法におけるこれら諸問題の原因を追求の’
結果、その最大の原因はセルロース系テープが樹脂の
加熱硬化時にテープの横方向の収縮を生じ、又比較的低
温度からテープの縦方向の収縮に伴う収縮応力を発生さ
せることに基づくことを見出した。However, in this molding method that uses cellulose tape, even under careful handling and setting of curing conditions, a large amount of resin flows to the outer surface due to a decrease in the viscosity of the thermosetting resin due to heating, and a large amount of resin flows to the outer surface of the laminated core metal. The fibers are likely to move or fall off, and furthermore, the fibers may meander partially in the longitudinal direction of the molded product. This phenomenon causes uneven distribution of resin and boards in the molded product, and when the meandering of the fibers applies external force to the molded product, there is a risk that the molded product will be damaged at that portion. Furthermore, cellulose tape completely deteriorates under the curing temperature conditions and has poor peelability from the cured resin, so a rotating metal plan or the like must be used to remove it, resulting in a rough surface of the molded product. , requires finishing processing such as painting. The present inventors have investigated the causes of these problems in the conventional molding method using cellulose tape.
As a result, we found that the main reason for this is that the cellulose tape shrinks in the transverse direction when the resin heats and hardens, and also generates shrinkage stress as the tape shrinks in the longitudinal direction at relatively low temperatures. Ta.
すなわち、一般にセルロース系テープは水分; を吸収
し易いセルロース以外にこれも又吸水し易いポリアルコ
ールである柔軟剤が比較的多量に含有されているため、
このようなセルロース系テープを加熱すると、縦横方向
に共に収縮し、実験結果によると横方向に110〜14
0℃附近迄にク 3.5%前後収縮し、170〜180
℃附近迄に4.0〜4.5%収縮し、更に縦方向に各々
、2〜2.5%、3.0〜3.5%収縮することが判明
、加えて縦方向の収縮応力は20mm巾テープで40〜
50℃から発生し初めることを知見した。5 更に熱硬
化性樹脂を含浸させた繊維のプリプレグ或はクロスの加
圧成形条件についても種々検討した結果、成形物中に樹
脂の偏在、ボードの発生を防止するためには、これら加
圧成形法において、加圧開始時と樹脂のゲル化点との関
係が極めて重要であることを見出し、樹脂のゲル化点附
近まで加熱した後加圧を開始すると、樹脂フローも適当
で樹脂の偏在、ボードのない成形物が得られることが判
った。That is, in general, cellulose tapes contain a relatively large amount of softener, which is polyalcohol, which also easily absorbs water, in addition to cellulose, which easily absorbs water.
When such a cellulose tape is heated, it shrinks both in the vertical and horizontal directions, and according to experimental results, it shrinks in the horizontal direction by 110 to 14
It shrinks by around 3.5% until it reaches around 0℃, and it shrinks to 170~180℃.
It was found that the shrinkage occurred by 4.0 to 4.5% in the vicinity of ℃, and further contraction in the longitudinal direction by 2 to 2.5% and 3.0 to 3.5%, respectively.In addition, the shrinkage stress in the longitudinal direction was 40~ with 20mm width tape
It was found that the occurrence started at 50°C. 5 Furthermore, as a result of various studies on the pressure molding conditions of fiber prepreg or cloth impregnated with thermosetting resin, we found that these pressure molding conditions are necessary to prevent uneven distribution of resin and board formation in the molded product. In this method, we discovered that the relationship between the start of pressurization and the gelation point of the resin is extremely important, and if we start pressurization after heating the resin to near the gelation point, the resin flow will be appropriate and the uneven distribution of the resin will be reduced. It has been found that moldings without boards can be obtained.
一方ゲル化点の前において加圧を開始して得られた成形
物は樹脂フローも多く、連続又は独立のボードが発生し
、逆にゲル化点をすぎた点で加圧を開始して得られた成
形物は樹脂フローはほとんどなくボードは比較的少ない
が、樹脂の偏在が生ずる。成形物の機械的性質は、内部
組織、特にボードと樹脂の偏在に敏感で、ゲル化点附近
での加圧では、他の点での加圧に較べ最大の機械的性質
を与えることを見出しL本発明においては、熱硬化性樹
脂を含浸した繊維のプリプレグ又はクロスを芯金に巻付
けて積層し、この表面にテープを巻付けて硬化させる成
形法において、熱硬化性樹脂の加熱硬化条件下、テープ
の横方向に収縮せず、樹脂のゲル化点附近で縦方向に収
縮し、積層物を加圧し且つ積層物に密着して容易に巻か
れ硬化後劣化せず硬化樹脂と容易に剥離し、表面に光沢
を与える性質を有するテープを鋭意探索し、このような
性質を有するテープの製造条件下その性質を任意に制御
可能な材料として結晶性熱可塑性樹脂テープを見出し本
発明に至つたものである。On the other hand, molded products obtained by starting pressurization before the gelling point have a large amount of resin flow, resulting in continuous or independent boards; The resulting molded product has almost no resin flow and relatively little board, but the resin is unevenly distributed. We found that the mechanical properties of molded products are sensitive to the internal structure, especially the uneven distribution of the board and resin, and that applying pressure near the gelation point gives the greatest mechanical properties compared to applying pressure at other points. L In the present invention, in a molding method in which prepreg or cloth of fibers impregnated with a thermosetting resin is wrapped around a core bar and laminated, and a tape is wrapped around the surface of the fabric and cured, the heating curing conditions of the thermosetting resin are At the bottom, the tape does not shrink in the horizontal direction, but contracts in the vertical direction near the gel point of the resin, pressurizes the laminate, adheres tightly to the laminate, is easily rolled, does not deteriorate after curing, and easily connects to the cured resin. The present invention was achieved by searching for tapes that can be peeled off and giving gloss to the surface, and finding a crystalline thermoplastic resin tape as a material whose properties can be controlled arbitrarily under the manufacturing conditions of tapes having such properties. It is ivy.
すなわち、本発明は熱硬化性樹脂を含浸させた繊維のプ
リプレグシート又はクロスを芯金に巻付けて積層物の表
面に、硬化時の熱によるテープの横方向の収縮がなく、
樹脂のゲル化点附近で縦方向に収縮が入るように予め加
熱処理により制御した結晶性熱可塑性樹脂テープを圧着
して、積層物の長手方向にヘリカルに巻付け、加熱硬化
し冷却後芯金を抜き取り、テープをはぎ取ることにより
、外表面に樹脂フローが少く、繊維の長手方向に沿つた
蛇行もなく、成形物中に樹脂の偏在、ボードの発生がな
く機械的性質が良好でそして、テープは連続的に硬化樹
脂表面から容易に剥離し得、成形物の表面に光沢を有し
、表面の後加工を必要としないFRPパイプの成形法に
ある。That is, in the present invention, a fiber prepreg sheet or cloth impregnated with a thermosetting resin is wound around a core bar, and the surface of the laminate is free from shrinkage in the lateral direction due to heat during curing.
A crystalline thermoplastic resin tape that has been previously controlled by heat treatment so that it shrinks in the longitudinal direction near the gelation point of the resin is crimped, wrapped helically in the longitudinal direction of the laminate, heated to harden, and cooled to form a core metal. By removing the tape and peeling off the tape, there is little resin flow on the outer surface, there is no meandering along the longitudinal direction of the fibers, there is no uneven distribution of resin in the molded product, there is no board formation, and the mechanical properties are good. The present invention provides a method for molding an FRP pipe that can be easily peeled off continuously from the surface of a cured resin, has a glossy surface, and does not require post-processing of the surface.
本発明に使用される結晶性熱可塑性樹脂のテープとして
はポリエチレンテレフタレート又はその共重合体、ナイ
ロン6、ナイロン66、或はポリプロピレンからなるも
のであるが、特にポリエチレンテレフタレート又はその
共重合体は耐熱性、熱収縮温度の制御、樹脂との剥離性
等から有効に使用しうる。The crystalline thermoplastic resin tape used in the present invention is made of polyethylene terephthalate or its copolymer, nylon 6, nylon 66, or polypropylene, and polyethylene terephthalate or its copolymer is particularly heat resistant. It can be effectively used because of its control of heat shrinkage temperature, releasability from resin, etc.
これらのテープの巾は積層物の長さ、太さ、又はテーパ
ーによつて選択できるが、通常5〜20nで、巻付け作
業のし易さ等から10〜15n巾のものが好ましく、テ
ープの厚みについても任意に選択できるが通常20〜1
00μで巻き作業のし易さ等から20〜50μが好まし
い。これらテープの熱収縮応力発生開始の制御は、使用
する樹脂の種類、硬化条件等に合わせたゲル化点との関
係で設定されるが、通常のエポキシ樹脂を使用し、ポリ
エチレンテレフタレートテープを使用する場合、市販の
ポリエステルフイルムを100〜160℃でローラー又
はオーブン中を通して加熱処理し、90〜140℃附近
で熱収縮応力が発生するよう設定するが、好ましくは1
40℃附近の熱処理で120℃前後で熱収縮応力が発生
するものが好ましい。この熱処理によつてテープの横方
向の収縮はほとんどなく、芯金に巻かれた積層物の表面
で硬化時移動することは全くない。なお、ポリエステル
フイルムをその2次転移点温度より若干高い温度で大巾
に延伸することで、縦方向の収縮応力を大きくすること
が可能であるがこのようなテープの場合は、樹脂の硬化
温度の比較的低温領域から急激な収縮応力が発生し外表
への樹脂フローが多くなり好ましくない。テープの積層
物の巻付け方法としては従来セルロース系テープ使用に
おけると同様に行われ、ヘリカル巻きが特に好ましく用
いられる。本発明で用いられる繊維のプリプレグ又はク
ロスは、ガラス繊維、カーボン繊維、芳香族ポリアミド
繊維等の繊維を一方向に平行に配列させた状態又は織物
或はこれらの交織織物を、エポキシ樹脂、不飽和ポリエ
ステル樹脂、フエノール樹脂等の未硬化の熱硬化性樹脂
とBF3/MEA、ブチルパーオキサイド等の硬化剤を
配合し、有機溶媒により粘度を低下させた浸透性高い樹
脂液に、含浸し乾燥して半硬化状態とすることにより製
造されるものが使用される。The width of these tapes can be selected depending on the length, thickness, or taper of the laminate, but is usually 5 to 20 nm, preferably 10 to 15 nm in width for ease of winding. The thickness can be selected arbitrarily, but it is usually 20 to 1
00μ and 20 to 50μ is preferable from the viewpoint of ease of winding work. Control of the start of heat shrinkage stress generation in these tapes is set in relation to the gel point according to the type of resin used, curing conditions, etc., but when using ordinary epoxy resin and polyethylene terephthalate tape, In this case, a commercially available polyester film is heated at 100 to 160°C through a roller or in an oven, and the temperature is set to generate heat shrinkage stress at around 90 to 140°C.
It is preferable that heat treatment at around 40°C causes heat shrinkage stress at around 120°C. Due to this heat treatment, there is almost no lateral shrinkage of the tape, and there is no movement at all during curing on the surface of the laminate wound around the core metal. Note that it is possible to increase the shrinkage stress in the longitudinal direction by stretching the polyester film to a wide width at a temperature slightly higher than its secondary transition temperature, but in the case of such a tape, the curing temperature of the resin Rapid shrinkage stress occurs from the relatively low temperature region of the resin, which increases resin flow to the outer surface, which is undesirable. The method for winding the tape laminate is the same as in conventional cellulose tapes, with helical winding being particularly preferred. The fiber prepreg or cloth used in the present invention is a state in which fibers such as glass fibers, carbon fibers, and aromatic polyamide fibers are arranged in parallel in one direction, or woven fabrics or mixed woven fabrics of these fibers, and epoxy resin, unsaturated It is made by blending uncured thermosetting resin such as polyester resin or phenolic resin with a curing agent such as BF3/MEA or butyl peroxide, and then impregnating it with a highly permeable resin liquid whose viscosity has been lowered with an organic solvent and drying it. Those manufactured by semi-curing are used.
本発明の成形法はパイプのみならず従来セルロース系テ
ープを巻付ける方法を用いるロツド等の成形品の製造法
にも応用しうることは勿論であり、本発明の意義は極め
て大きいものである。以下実施例により本発明を説明す
る。It goes without saying that the molding method of the present invention can be applied not only to pipes but also to methods for manufacturing molded products such as rods using the conventional method of winding cellulose tape, and the significance of the present invention is extremely large. The present invention will be explained below with reference to Examples.
実施例 1
熱硬化性樹脂としてシエルエピコートDX一210(シ
エル化学製エポキシ樹脂)125重量部、BF3/ME
A3重量部およびメチルエチルケトン65重量部から成
る樹脂溶液を用い、厚み0.15mm)樹脂分42.5
%の一方向配列のカーボン繊維のプリプレグシートをつ
くつた。Example 1 125 parts by weight of Ciel Epicote DX-210 (epoxy resin manufactured by Ciel Chemical Co., Ltd.) as a thermosetting resin, BF3/ME
Using a resin solution consisting of 3 parts by weight of A and 65 parts by weight of methyl ethyl ketone, the thickness was 0.15 mm) resin content was 42.5 mm.
% of unidirectionally aligned carbon fiber prepreg sheets were made.
このプリプレグシートを100×100mmの正方形を
10枚切り出し、これを一方向に10フライ積層して、
熱電対をさし込み、ポリエチレンテレフタレートフイル
ムで絶縁したアルミ電極の間にこの積層物をはさみ、1
70℃に加熱した加圧成形機の平板上におく。Cut out 10 square pieces of 100 x 100 mm from this prepreg sheet, stack them 10 times in one direction,
Insert a thermocouple and sandwich this laminate between aluminum electrodes insulated with polyethylene terephthalate film.
Place on a flat plate of a pressure molding machine heated to 70°C.
両電極間の誘電率の変化と積層物の温度変化を記録する
誘電率から得た、この積層物のゲル化点は18分後の1
58℃であつた。この結果に基づき、市販の38μのポ
リエステルテープを140℃のロール上で加熱処理して
おく。The gel point of this laminate, obtained from the dielectric constant that records the change in dielectric constant between both electrodes and the temperature change of the laminate, is 1 after 18 minutes.
It was 58°C. Based on this result, a commercially available 38μ polyester tape was heat-treated on a roll at 140°C.
この熱処理テープは、縦方向に130℃附近から収縮し
始め、同時に熱収縮応力が発生しはじめる。しかも17
0℃での横方向の収縮は全くなかつた。他方、市販のセ
ルロース系テープを用意した。This heat-treated tape begins to shrink in the longitudinal direction at around 130° C., and at the same time, heat shrinkage stress begins to occur. And 17
There was no lateral shrinkage at 0°C. On the other hand, a commercially available cellulose tape was prepared.
このテープは厚み45μ、巾18mmで熱収縮応力は4
0℃附近から発生し、170℃における横方向への収縮
は4%で縦方向のそれは3.3%であつた。上記プリプ
レグシートから梯形片を切り出しテーパー率1/500
の中心部直径29.5m7nのクロムモリブデン鋼の芯
金に、ローリングマシンにて3フライ巻付けた。This tape has a thickness of 45μ, a width of 18mm, and a heat shrinkage stress of 4
The shrinkage occurred at around 0°C, and at 170°C, the shrinkage in the transverse direction was 4% and the shrinkage in the longitudinal direction was 3.3%. Cut out a trapezoidal piece from the above prepreg sheet and taper rate 1/500
The core of chrome-molybdenum steel with a center diameter of 29.5m7n was wound three times using a rolling machine.
この表面に上記ポリエチレンテレフタレートテープおよ
びセルロース系テープを各々テープ巻機で積層物の表面
にテーブにしわの入らぬ程度に密着させ、長手方向に2
nピツチにへリカル構造に巻き上げた。この2本の巻物
を予め170℃に加熱した炉中に吊り下げ120分間樹
脂を完全硬化させた後、冷却した。ポリエチレンテレフ
タレートテープの場合、外表面への樹脂フローはほとん
どなく、又テープの移動も全くなかつた。The above-mentioned polyethylene terephthalate tape and cellulose tape were each attached to the surface of the laminate using a tape winding machine to the extent that no wrinkles were formed in the tape, and
It was rolled up into a helical structure with n pitches. These two scrolls were suspended in a furnace preheated to 170° C. for 120 minutes to completely cure the resin, and then cooled. In the case of the polyethylene terephthalate tape, there was almost no resin flow to the outer surface and no tape movement at all.
テープの巻き終りの先端をもち上げ、パイプ状物を回転
させながらテープの端を引つぱると、連続的にテープは
剥離し、つやのある表面が得られた。繊維の蛇行も全く
みられず、パイプの一部を切断し、電子顕微鏡で断面を
観察したところ、樹脂の偏在、ボードは発見できず均一
な成形物が得られた。一方セルロース系テープの場合、
外表面への樹脂フローが幾すじも流れており、テープは
完全に劣化し、部分的にすでに切断していた。When the end of the tape was lifted up and the end of the tape was pulled while rotating the pipe, the tape was continuously peeled off and a glossy surface was obtained. No meandering of the fibers was observed, and when a part of the pipe was cut and the cross section was observed under an electron microscope, no uneven distribution of resin or board was found, and a uniform molded product was obtained. On the other hand, in the case of cellulose tape,
There were several streaks of resin flow to the outer surface, and the tape was completely degraded and had already broken in parts.
テープはパイプの中心に向つて両端から、初めの位置か
ら最大2%程度移動していた。パイプの一部を切断し電
子顕微鏡で観察したところ、連続したボードがみつかり
、一部樹脂の偏在が認められた。又テープは上表層は、
容易に取り除けるが、樹脂と接した最下層は接着し、こ
れを取除くのに金属回転ブラシが必要であつた。そのた
め表面はつやのないものとなつた。繊維は各所で、パイ
プの円周上に沿つて蛇行していた。実施例 2
厚さ0.10mmのガラス繊維朱子織布に実施例1と同
様にしてシエルエピコートDX−210125重量部、
BF3/MEA3重量部およびメチルエチルケトン29
0重量部の樹脂液を含浸付着、乾燥して樹脂付着量40
.5%のガラス繊維布のプリプレグを得た。The tape had moved from both ends toward the center of the pipe by a maximum of about 2% from its initial position. When a part of the pipe was cut and observed under an electron microscope, a continuous board was found, with uneven distribution of resin in some parts. Also, the upper surface layer of the tape is
Although easy to remove, the bottom layer in contact with the resin adhered and required a rotating metal brush to remove it. As a result, the surface became dull. The fibers meandered along the circumference of the pipe at various points. Example 2 Ciel Epicoat DX-210125 parts by weight was applied to a glass fiber satin woven fabric having a thickness of 0.10 mm in the same manner as in Example 1.
BF3/MEA 3 parts by weight and methyl ethyl ketone 29
Impregnated with 0 parts by weight of resin liquid and dried to obtain a resin adhesion amount of 40 parts by weight.
.. A 5% glass fiber cloth prepreg was obtained.
このゲル化点は実施例1と同様に測定した所、15分後
の145℃であつた。The gelation point was measured in the same manner as in Example 1 and was found to be 145°C after 15 minutes.
このガラス繊維布プリプレグを用いて、実施例1と同様
にして同じ芯金に5フライ巻きつけて、その表面に実施
例1と同じポリエチレンチレフタレートテープを密着す
るよう巻付けた。Using this glass fiber cloth prepreg, it was wrapped five times around the same metal core in the same manner as in Example 1, and the same polyethylene tyrephthalate tape as in Example 1 was wrapped tightly around the surface thereof.
次いで170℃で120分硬化処理した。テープは容易
に連続的に剥離でき、繊維の蛇行、I 樹脂の偏在そし
てボードもないパイプ状成形物を得た。Then, it was cured at 170°C for 120 minutes. The tape could be easily and continuously peeled off, yielding a pipe-shaped molded product free of meandering fibers, uneven distribution of resin, and boards.
これに対しセルロース系テープを用い、同様にして成形
したパイプ状物はテープがずれ、繊維も若干蛇行してお
りボードがみられた。On the other hand, in a pipe-shaped product formed in the same manner using cellulose tape, the tape was shifted, the fibers were slightly meandering, and boards were observed.
実施例 3
厚さ0.11mmのケプラー(デユポン社製芳香族ポリ
アミド繊維)平織物布に実施例1と同様にして、シエル
エピコートDX− 210樹脂を38%付着したケプラ
ー布のプリプレグを得た。Example 3 In the same manner as in Example 1, a prepreg of Kepler cloth was obtained by adhering 38% of Ciel Epicoat DX-210 resin to a 0.11 mm thick Kepler (aromatic polyamide fiber manufactured by Dupont) plain woven cloth.
このゲノ ル化点は実施例1と同様に測定した所12分
後の131℃であつた。市販のポリエチレンテレフタレ
ートテープを120℃で熱処理した。The genolization point was measured in the same manner as in Example 1 and was found to be 131°C after 12 minutes. A commercially available polyethylene terephthalate tape was heat treated at 120°C.
このプリプレグを梯形片に切り出しテーパー率2.1/
1000、中心直径10.93nのステンレススチール
製の芯金に3フライ巻付けた。この表面に上記テープを
巻きつけ170℃で120分間加熱硬化し冷却後芯金を
抜き取つた。テープの移動、積層物の脱落、それに外表
面への樹脂フローも全くなかつた。Cut this prepreg into trapezoidal pieces with a taper ratio of 2.1/
1000, and three flies were wound around a stainless steel core metal having a center diameter of 10.93n. The above-mentioned tape was wrapped around this surface and cured by heating at 170° C. for 120 minutes, and after cooling, the core metal was removed. There was no tape movement, no laminate shedding, and no resin flow to the outside surface.
テープを連続的に剥離しつやのある表面が得られ、繊維
の蛇行もなく、ボードのないパイプ状成形物を得た。こ
れに対し、実施例1で用いたセルロース系テープを使用
したところ、テープは初めの位置からずれ、繊維は部分
的にパイプ円周上に大きく蛇行し、最内層までその蛇行
は達していた。The tape was continuously peeled off to obtain a shiny surface, no meandering of fibers, and a pipe-shaped molded product without a board. On the other hand, when the cellulose tape used in Example 1 was used, the tape deviated from its initial position, and the fibers meandered partially around the circumference of the pipe, and the meandering reached the innermost layer.
Claims (1)
はクロスを芯金に巻付けて積層し加熱硬化して繊維強化
プラスチックパイプを成形するに際し、硬化前の積層物
の表面に、加熱による横方向の収縮がなく樹脂のゲル化
点附近で縦方向に収縮する結晶性熱可塑性樹脂のテープ
を巻付けて加熱硬化後該テープをはぎ取ることを特徴と
する繊維強化プラスチックパイプの成形法。1. When forming a fiber-reinforced plastic pipe by wrapping prepreg sheets or cloth of fibers impregnated with a thermosetting resin around a core metal and curing them by heating, the surface of the laminate before curing is coated with a lateral direction caused by heating. A method for forming a fiber-reinforced plastic pipe, characterized by wrapping a tape of a crystalline thermoplastic resin that does not shrink and shrinks in the longitudinal direction near the gelling point of the resin, and then peeling off the tape after curing by heating.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP50056861A JPS5935766B2 (en) | 1975-05-12 | 1975-05-12 | Molding method of fiber reinforced plastic pipe |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP50056861A JPS5935766B2 (en) | 1975-05-12 | 1975-05-12 | Molding method of fiber reinforced plastic pipe |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS51131575A JPS51131575A (en) | 1976-11-16 |
| JPS5935766B2 true JPS5935766B2 (en) | 1984-08-30 |
Family
ID=13039185
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP50056861A Expired JPS5935766B2 (en) | 1975-05-12 | 1975-05-12 | Molding method of fiber reinforced plastic pipe |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5935766B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63215329A (en) * | 1987-03-05 | 1988-09-07 | Mitsubishi Metal Corp | Webbed bevel gear |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5075442B2 (en) * | 2006-03-27 | 2012-11-21 | 三菱レイヨン株式会社 | Protective member and manufacturing method thereof |
-
1975
- 1975-05-12 JP JP50056861A patent/JPS5935766B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63215329A (en) * | 1987-03-05 | 1988-09-07 | Mitsubishi Metal Corp | Webbed bevel gear |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS51131575A (en) | 1976-11-16 |
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