JPS6142614B2 - - Google Patents
Info
- Publication number
- JPS6142614B2 JPS6142614B2 JP56014237A JP1423781A JPS6142614B2 JP S6142614 B2 JPS6142614 B2 JP S6142614B2 JP 56014237 A JP56014237 A JP 56014237A JP 1423781 A JP1423781 A JP 1423781A JP S6142614 B2 JPS6142614 B2 JP S6142614B2
- Authority
- JP
- Japan
- Prior art keywords
- resin
- glass fiber
- diameter
- fibers
- fiber bundle
- 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
Landscapes
- Reinforced Plastic Materials (AREA)
- Moulding By Coating Moulds (AREA)
Description
【発明の詳細な説明】
本発明はスプレーアツプ法によるFRPの製造
方法に関するものである。
硝子繊維束の切断物(CSと略称)を、液状熱
硬化性樹脂とともに型面に吹付け、未硬化の繊維
補強樹脂層を形成せしめ、樹脂を硬化せしめるス
プレーアツプ法は、船舶、バスタブ、浄化槽等の
製造に広く用いられている。
スプレーアツプ法に用いられるCSは次のよう
な諸性質を兼備することが強く要望される。
(1) 得られたFRPの衝撃、引張り等の各種強度
が所定の水準値以上となること。
(2) 樹脂の保持能力が充分大きいこと。
保持能力が小さいと、FRPの中の樹脂含有
量を充分大きくすることができず、又樹脂が硬
化する迄の間に型の下方に樹脂が流下し、均一
なFRPが得られなくなる。
(3) 型附きが良好であること。
型附きとは型面に吹き付けられたCSが樹脂
中に埋没した状態で型面に沿つて馴染むことを
云い、型附きが不良の場合、CSの先端が樹脂
層から突出した状態となる。このためFRPの
表面が粗くなつたり、又繰返しスプレーアツプ
を行なうとき、最初に形成された層中のCSが
吹き飛んだりし易い。
硝子繊維束に液状樹脂を含浸させると、樹脂は
硝子繊維束を構成する個々の繊維の間に入り込
み、個々の繊維表面に所定厚みの薄層をなして附
着し、繊維によつて保持される。
この厚みは樹脂、硝子繊維の性質(粘度、界面
張力等)によつて定まる。
このため、硝子繊維束による樹脂の保持量は、
硝子繊維の表面積に比例するものと考えられる。
従つて硝子繊維束の単位長さ当りの重量が一定の
場合、径の小さい硝子繊維を多数集束してなる硝
子繊維束の方が樹脂の保持量(保持能力)が大き
い理である。
又硝子繊維束の太さ(単位長さ当りの重量)が
一定の場合、繊維束を構成する個々の硝子繊維の
太さ(径)小さい程、繊維束の可撓性は大きくな
る。従つて硝子繊維の径が小さい程型附きも良好
となるやに考えられる。
このため従来スプレーアツプ用の硝子繊維束と
しては、直径10μ程度の比較的細いものが専ら使
用されて来たが、スプレーアツプで製造される
FRPが大型化されるにつれ、上記性能の一層の
向上が強く要望されるに至つた。
本発明者はスプレーアツプ用の硝子繊維束の性
能を一層向上させ上記要望に答えるべく種々研究
を重ねる過程において、フイルム形成剤として酢
ビ系樹脂エマルジヨンを主成分として含む水性集
束剤を用いた場合には、硝子繊維として12〜14μ
の径のものを用いた方が、10μの硝子繊維を用い
れ場合に比し、従来の常識に反し、不飽和ポリエ
ステル樹脂の保持量、型附きにおいて優れている
ことを見出した。
何故このような結果が得られたのか詳らかでは
ないが、およそ次のように考えられる。
酢ビ系集束剤で集束された硝子繊維束に、液状
の不飽和ポリエステル樹脂(以下単に樹脂とい
う)を含浸させると、樹脂は硝子繊維間に侵入す
る。酢ビ系集束剤は樹脂中に含まれるスチレンに
よつて溶解し、繊維同志の間隔は次第に広くな
り、樹脂の侵入が繊維束内部迄進行する。このよ
うして樹脂の侵入が繊維束の中心部迄進行し、平
衝状態となつた場合を考えると、10μの繊維を用
いた場合の方が12〜14μの繊維を用いた場合に比
し大きい。
しかしながら、太い繊維を用いた場合の方が、
繊維間の隙間も大きく、従つて単位時間当りの樹
脂の侵入速度も大きい。このため工業的スプレー
アツプの作業条件においては、12〜14μの硝子繊
維を使用した場合の方が、樹脂の保持量も大き
く、又集束剤の溶解が速やかに行なわれて繊維束
が開繊する為可撓性が大となり、型附きも良好と
なるものと思われる。なお硝子繊維の太さを15μ
以上とした場合は上述のような良好な結果をうる
ことはできなかつた。硝子繊維の径が15μ以上の
場合は、径の増大による表面積減少効果、可撓性
の減少効果が、樹脂の侵入速度増大の効果を上廻
るものと考えられる。
次に本発明を更に具体的に説明する。
ブツシングに設けられた多数の小孔から流出し
た溶融硝子を引伸すことによつて硝子繊維は製造
される。硝子繊維の径は小孔の大きさ、引伸し速
度等によつて定まる。本発明においてはこれ等の
条件を実験的に定め、直径12〜14μとなし、この
硝子繊維にフイルム形成剤として酢ビ系樹脂エマ
ルジヨンを含む集束剤を附与して集束する。集束
本数は100〜150本とし且つ直径(μ)2×集束本
数が14.400〜24.000の範囲となるよう定める。こ
の範囲以下では繊維束の剛性が小となつて作業性
が悪く、この範囲以上では樹脂保持量が不充分と
なる。
酢ビ系樹脂としては酢ビホモポリマー、酢ビ・
エポキシコポリマー、酢ビ・アクリルコポリマ
ー、酢ビ・エチレンコポリマー等が好適に使用で
きる。酢ビ系樹脂としては重合度400〜2.000好ま
しくは500〜1000、粒子径が0.1〜2.0μ好ましく
は0.2〜0.5μのものが好適に使用できる。又集束
剤としては酢ビ系樹脂を固型分として7〜10%程
度エマルジヨンとして含むものを用いるのが適当
であり、通常この他に潤滑剤、カツプリング剤を
加えたものが使用される。
なお上述した硝子繊維に附与すべき集束剤の量
は固型分として0.7〜2.0wt%程度とするのが適当
であり、公知の集束剤附与装置を用いて附与する
ことができる。
上述の硝子繊維束を20〜60mmの長さに切断し
て、不飽和ポリエステル樹脂とともに型面に吹付
ける。硝子繊維束切断物100重量部に対する樹脂
量は200〜300重量部とするのが適当であり、以下
の実施例からも明らかなように本発明の方法によ
るときは従来のものに比し、型附きが良好であ
り、又従来のものに比した程重要でない引張り、
曲げ強度は若干低下するが、所定の基準値は充分
満足し且つ浴槽等の大型スプレーアツプ品として
最も重要な衝撃強度は増加し、総合的な比較にお
いて強度においても優れた製品をうることができ
る。
次に本発明の実施例を示す。
実施例
直径13μの硝子繊維100本に、酢ビホモポリマ
ーエマルジヨン(重合度800)を固形分として7
重量%、ステアリン酸・テトラエチレンベンタミ
ン縮合物(潤滑剤)0.4重量%、シラン系カツプ
リング剤0.1重量%含む集束剤を固型分として硝
子繊維に対し1.0重量%附与して集束した硝子繊
維束を2.5cmの長さに切断し、この繊維束切断物
と不飽和ポリエステル樹脂を型面に5回繰返し吹
付けm2当り繊維束900gr、樹脂2000grを含む
樹脂層を形成せしめ、樹脂を硬化せしめて浄化槽
を製造した。
直径10μの硝子繊維200本を用いて同様にして
製造した硝子繊維束の場合との同条件における比
較は次の通りである。
【表】DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing FRP by a spray-up method. The spray-up method, in which cut glass fiber bundles (abbreviated as CS) are sprayed onto the mold surface together with liquid thermosetting resin to form an uncured fiber-reinforced resin layer and harden the resin, is used for ships, bathtubs, and septic tanks. It is widely used in the production of etc. It is strongly desired that the CS used in the spray-up method have the following properties. (1) The various strengths of the resulting FRP, such as impact and tensile strength, must exceed specified standard values. (2) The resin retention capacity is sufficiently large. If the holding capacity is small, the resin content in the FRP cannot be sufficiently increased, and the resin will flow down the mold until it hardens, making it impossible to obtain a uniform FRP. (3) Shapeability is good. Mold attachment refers to the fact that the CS sprayed onto the mold surface is embedded in the resin and blends along the mold surface. If the mold attachment is poor, the tip of the CS will protrude from the resin layer. For this reason, the surface of FRP becomes rough, and CS in the initially formed layer tends to be blown away when spraying is repeated. When a glass fiber bundle is impregnated with liquid resin, the resin gets between the individual fibers that make up the glass fiber bundle, forms a thin layer of a predetermined thickness on the surface of each fiber, and is held by the fibers. . This thickness is determined by the properties (viscosity, interfacial tension, etc.) of the resin and glass fiber. Therefore, the amount of resin held by the glass fiber bundle is
It is thought that it is proportional to the surface area of the glass fiber.
Therefore, when the weight per unit length of the glass fiber bundle is constant, a glass fiber bundle made by bundling a large number of glass fibers with a small diameter has a larger resin retention amount (holding capacity). Further, when the thickness (weight per unit length) of the glass fiber bundle is constant, the smaller the thickness (diameter) of the individual glass fibers constituting the fiber bundle, the greater the flexibility of the fiber bundle. Therefore, it is thought that the smaller the diameter of the glass fiber, the better the shapeability. For this reason, comparatively thin glass fiber bundles with a diameter of about 10 μm have traditionally been used exclusively for spray-up;
As FRPs have become larger, there has been a strong demand for further improvements in the above performance. In the process of conducting various studies to further improve the performance of glass fiber bundles for spray-up use and to meet the above requirements, the present inventor discovered that an aqueous sizing agent containing a vinyl acetate resin emulsion as a main component was used as a film forming agent. 12~14μ as glass fiber
It has been found that, contrary to conventional wisdom, using glass fibers with a diameter of 10 μm is superior in terms of the amount of unsaturated polyester resin retained and moldability. Although it is not clear why such a result was obtained, it is thought to be approximately as follows. When a glass fiber bundle bundled with a vinyl acetate-based sizing agent is impregnated with liquid unsaturated polyester resin (hereinafter simply referred to as resin), the resin penetrates between the glass fibers. The vinyl acetate-based sizing agent is dissolved by the styrene contained in the resin, and the distance between the fibers gradually widens, allowing the resin to penetrate into the fiber bundle. Considering the case where the resin penetrates to the center of the fiber bundle and reaches a state of equilibrium, using 10μ fibers is better than using 12-14μ fibers. big. However, when using thicker fibers,
The gaps between the fibers are also large, and therefore the resin penetration rate per unit time is also large. Therefore, under the working conditions of industrial spray-up, when glass fibers with a diameter of 12 to 14 μm are used, the amount of resin retained is greater, and the sizing agent is quickly dissolved and the fiber bundle is opened. Therefore, it is thought that flexibility will be greater and moldability will be better. The thickness of the glass fiber is 15μ.
In the above case, it was not possible to obtain the above-mentioned good results. When the diameter of the glass fiber is 15μ or more, it is thought that the effect of decreasing the surface area and decreasing flexibility due to the increase in the diameter outweighs the effect of increasing the penetration speed of the resin. Next, the present invention will be explained in more detail. Glass fibers are produced by drawing molten glass flowing out from a number of small holes provided in the bushing. The diameter of the glass fiber is determined by the size of the pores, the drawing speed, etc. In the present invention, these conditions are determined experimentally to set the diameter to 12 to 14 microns, and the glass fibers are bundled by adding a binding agent containing a vinyl acetate resin emulsion as a film forming agent. The number of focused lines is set to 100 to 150, and the diameter (μ) 2 × number of focused lines is determined to be in the range of 14.400 to 24.000. Below this range, the stiffness of the fiber bundle will be low and workability will be poor; above this range, the amount of resin retained will be insufficient. Vinyl acetate-based resins include vinyl acetate homopolymer, vinyl acetate,
Epoxy copolymers, vinyl acetate/acrylic copolymers, vinyl acetate/ethylene copolymers, etc. can be suitably used. As the vinyl acetate resin, those having a degree of polymerization of 400 to 2.000, preferably 500 to 1000, and a particle size of 0.1 to 2.0μ, preferably 0.2 to 0.5μ can be suitably used. As the sizing agent, it is appropriate to use an emulsion containing about 7 to 10% vinyl acetate resin as a solid content, and usually a lubricant and a coupling agent are used in addition to this. The amount of sizing agent to be added to the above-mentioned glass fibers is suitably about 0.7 to 2.0 wt% in terms of solid content, and can be added using a known sizing agent adding device. The above-mentioned glass fiber bundle is cut into lengths of 20 to 60 mm and sprayed onto the mold surface together with unsaturated polyester resin. It is appropriate that the amount of resin is 200 to 300 parts by weight per 100 parts by weight of the cut glass fiber bundle, and as is clear from the following examples, when the method of the present invention is used, the molding is better than that of the conventional method. Good adhesion and less significant tension than conventional ones,
Although the bending strength slightly decreases, the specified standard value is fully satisfied, and the impact strength, which is the most important for large spray-up products such as bathtubs, increases, making it possible to obtain a product that is superior in strength in a comprehensive comparison. . Next, examples of the present invention will be shown. Example: 100 glass fibers with a diameter of 13 μm were mixed with vinyl acetate homopolymer emulsion (degree of polymerization: 800) as a solid content of 7.
Glass fibers bundled by adding 1.0% by weight of a sizing agent as a solid content to the glass fibers, including 0.4% by weight of stearic acid/tetraethylenebentamine condensate (lubricant) and 0.1% by weight of a silane coupling agent. The bundle was cut to a length of 2.5 cm, and the cut fiber bundle and unsaturated polyester resin were repeatedly sprayed on the mold surface 5 times to form a resin layer containing 900 gr of fiber bundle and 2000 gr of resin per m 2 and harden the resin. At least I manufactured a septic tank. A comparison under the same conditions with a glass fiber bundle produced in the same manner using 200 glass fibers with a diameter of 10 μm is as follows. 【table】
Claims (1)
して酢ビ系樹脂エマルジヨンを含む集束剤を附与
し100〜150本集束してなり、且つ直径(μ)2×
集束本数が14.400〜24.000の範囲にある硝子繊維
束の切断物を液状の不飽和ポリエステル樹脂とと
もに型面に吹付け樹脂を硬化させることを特徴と
するFRPの製造方法。1 Glass fibers with a diameter of 12 to 14μ are added with a sizing agent containing a vinyl acetate resin emulsion as a film forming agent, and 100 to 150 fibers are bundled, and the diameter (μ) is 2 ×
A method for producing FRP, which comprises spraying cut glass fiber bundles having a bundle number in the range of 14,400 to 24,000 together with a liquid unsaturated polyester resin onto a mold surface and curing the resin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56014237A JPS57128513A (en) | 1981-02-04 | 1981-02-04 | Production of frp |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56014237A JPS57128513A (en) | 1981-02-04 | 1981-02-04 | Production of frp |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57128513A JPS57128513A (en) | 1982-08-10 |
| JPS6142614B2 true JPS6142614B2 (en) | 1986-09-22 |
Family
ID=11855467
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56014237A Granted JPS57128513A (en) | 1981-02-04 | 1981-02-04 | Production of frp |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57128513A (en) |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5141769A (en) * | 1974-10-07 | 1976-04-08 | Nippon Musical Instruments Mfg | |
| JPS51119765A (en) * | 1975-04-15 | 1976-10-20 | Kuraray Co | Resin mould for reinforced plastic moulding |
| JPS5527856A (en) * | 1978-08-18 | 1980-02-28 | Asahi Fiber Glass Co Ltd | Cutting method for glass fiber roving |
| JPS55122066A (en) * | 1979-03-12 | 1980-09-19 | Asahi Fibreglass Co | Production of chopped strand mat |
-
1981
- 1981-02-04 JP JP56014237A patent/JPS57128513A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57128513A (en) | 1982-08-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2877501A (en) | Glass-reinforced thermoplastic injection molding compound and injection-molding process employing it | |
| DE69222771T2 (en) | COMPOSITION TO CHEMICAL TREATMENT OF GLASS FIBERS CONSISTING OF EPOXY EMULSIONS WITH GOOD STABILITY AND TREATED GLASS FIBERS | |
| US5665470A (en) | Glass fibers and fiber-reinforced plastics | |
| US3312569A (en) | Compatible fibrous glass reinforcements of superior bonding and wetting characteristics | |
| JP2004526070A5 (en) | ||
| DE69502699T2 (en) | GLASS FIBER SIZING COMPOSITIONS, LAYERED GLASS FIBERS AND METHOD FOR REINFORCING POLYMER MATERIALS | |
| DE2659370A1 (en) | COATED FIBERGLASS | |
| KR950018225A (en) | Mixture for melt molding of glass filament polypropylene and polypropylene | |
| CA2035270A1 (en) | Coating composition for fibers | |
| US3817898A (en) | Sizing composition and glass fibers treated therewith | |
| JP3255414B2 (en) | Glass sizing composition and glass fiber coated therewith | |
| US3249411A (en) | Method of forming a glass fiber reinforced resinous body | |
| JP2655700B2 (en) | Glass fiber reinforced poly (vinyl chloride) blend and method for producing the same | |
| WO2019195069A1 (en) | Carbon fibers with tuned stiffness | |
| EP0027942B1 (en) | Sizing composition for glass fibres, glass fibres sized therewith and process for their preparation, as well as glass fibre composites | |
| US3063883A (en) | Reinforced resin laminates | |
| US4473618A (en) | Chrome-free sizing composition containing titanium acetyl acetonate for glass fiber gun roving | |
| EP0134445B1 (en) | Abs moulding masses reinforced with glass fibres | |
| JP4062140B2 (en) | Flat glass fiber bundle, thermoplastic composition and thermoplastic molding | |
| DE3885972T2 (en) | Chemically treated fibers and processes for making and reinforcing polymers. | |
| US4656084A (en) | Aqueous size composition with pH regulator | |
| GB1593315A (en) | Coated glass fibres | |
| DE1154243B (en) | Process for finishing glass threads | |
| JPH0272908A (en) | Chemically treated molded body, filler and reinforcing material for polymer matrix | |
| JPS6142614B2 (en) |