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JPH0811867B2 - Glass fiber for unsaturated polyester resin reinforcement - Google Patents
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JPH0811867B2 - Glass fiber for unsaturated polyester resin reinforcement - Google Patents

Glass fiber for unsaturated polyester resin reinforcement

Info

Publication number
JPH0811867B2
JPH0811867B2 JP3016870A JP1687091A JPH0811867B2 JP H0811867 B2 JPH0811867 B2 JP H0811867B2 JP 3016870 A JP3016870 A JP 3016870A JP 1687091 A JP1687091 A JP 1687091A JP H0811867 B2 JPH0811867 B2 JP H0811867B2
Authority
JP
Japan
Prior art keywords
resin
curing
unsaturated polyester
curing accelerator
glass 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.)
Expired - Fee Related
Application number
JP3016870A
Other languages
Japanese (ja)
Other versions
JPH04240265A (en
Inventor
大谷内達也
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.)
Asahi Fiber Glass Co Ltd
Original Assignee
Asahi Fiber Glass 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 Asahi Fiber Glass Co Ltd filed Critical Asahi Fiber Glass Co Ltd
Priority to JP3016870A priority Critical patent/JPH0811867B2/en
Publication of JPH04240265A publication Critical patent/JPH04240265A/en
Publication of JPH0811867B2 publication Critical patent/JPH0811867B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Reinforced Plastic Materials (AREA)
  • Surface Treatment Of Glass Fibres Or Filaments (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、FRPの製造に好適に
用いられる、不飽和ポリエステル樹脂補強用ガラス繊維
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a glass fiber for reinforcing an unsaturated polyester resin, which is preferably used for producing FRP.

【0002】[0002]

【従来の技術】FRPは、ガラス繊維、炭素繊維、有機
繊維のような補強用繊維に液状の熱硬化性樹脂を含浸さ
せ、該樹脂を硬化させることによって製造される。FR
Pとしては、不飽和ポリエステル樹脂をガラス繊維で補
強したもの最も一般的に用いられており、又液状の
飽和ポリエステル樹脂中には、硬化剤、硬化開始剤、触
媒等の硬化を起させる物質を混入したもの又は、これに
更に硬化を促進する物質(硬化促進剤)を混入したもの
が使用される。近年生産性を向上させる目的で、硬化時
間を短縮する要求が出て来た。この目的の為に、硬化促
剤の混入量を大とする必要が生ずる。
2. Description of the Related Art FRP is manufactured by impregnating a reinforcing fiber such as glass fiber, carbon fiber or organic fiber with a liquid thermosetting resin and curing the resin. FR
As P, unsaturated polyester resin is supplemented with glass fiber.
What was mightier are most commonly used, also non liquid
The saturated polyester resin, curing agent, curing initiator, those obtained by mixing materials caused Ru cause curing catalyst and the like, or, in this
Further, a substance mixed with a substance that accelerates curing (curing accelerator) is used. In recent years, there has been a demand for shortening the curing time for the purpose of improving productivity. For this purpose, the mixing amount of the hardening accelerator to be large occur.

【0003】[0003]

【発明が解決しようとする課題】従来技術は次のような
問題点を有する。液状の不飽和ポリエステル樹脂(以下
本樹脂という)に多量の硬化促進剤を添加、混合すると
樹脂の硬化速度が増大する。このため樹脂の粘度
が、使用中急速に増加するため、作業条件にバラツキが
生じ、また液状の樹脂のポットライフが短くなり、混
合を少量づつ行なうことが必要となり、FRP製造の手
間が増大する。
The prior art has the following problems. Liquid unsaturated polyester resin (hereinafter
When a large amount of curing accelerator is added to and mixed with this resin)
The curing speed of the resin is increased. For this reason, the viscosity of the present resin increases rapidly during use, which causes variations in working conditions, shortens the pot life of the present resin in a liquid state, and requires a small amount of mixing. Increase.

【0004】又、補強用ガラス繊維(以下本繊維とい
う)と樹脂との界面に微少な亀裂が発生し易く、このた
め得られたFRPの耐水性が劣化し、白化が生じ易い。
In addition, reinforcing glass fiber (hereinafter referred to as the present fiber)
U) and occurred minute cracks in the interface between the resin easily, Therefore resulting water resistance of the FRP is deteriorated, whitening occurs easily.

【0005】硬化促進剤の添加量を増大させることによ
り、硬化速度を大とすることができるが、生産性を向上
させるため添加量を大とするとコストが増大する。又、
硬化を加熱炉中で行なわせることにより硬化時間を短縮
することができるが、この方法は余分なエネルギーを消
費し、又設備費が増大してコストが増大したり、FRP
の品質の劣化を生じ易い。
The curing rate can be increased by increasing the amount of the curing accelerator added, but the productivity is improved.
Therefore, if the addition amount is large, the cost increases. or,
Although the curing time can be shortened by performing the curing in a heating furnace, this method consumes extra energy, increases the equipment cost, and increases the cost.
It is easy to cause deterioration of quality.

【0006】本発明は、上述の従来技術の問題点を解消
し、液状の不飽和ポリエステル樹脂のポットライフを低
下させることなく、樹脂の硬化を促進して、生産性を向
上させ、品質が均一で、耐水性の良好なFRPを得るこ
とを目的とする。
The present invention solves the above-mentioned problems of the prior art, accelerates curing of the liquid unsaturated polyester resin without lowering the pot life of the liquid unsaturated polyester resin, improves productivity, and provides uniform quality. The purpose is to obtain an FRP having good water resistance.

【0007】[0007]

【課題を解決するための手段】本発明においては、上記
目的を達成するために、不飽和ポリエステル樹脂補強用
ガラス繊維として、本樹脂の硬化を促進する硬化促進剤
を被着させたものを使用する。次に、本発明を更に具体
的に説明する。
SUMMARY OF THE INVENTION In order to achieve the above object, the present invention is for reinforcing an unsaturated polyester resin.
As the glass fiber, a glass fiber coated with a curing accelerator that accelerates the curing of the present resin is used. Next, the present invention will be described more specifically.

【0008】本発明に用いる補強用繊維としては、ガラ
ス繊維を用いる。
[0008] As the reinforcing fiber used in the present invention, Ru with glass fibers.

【0009】繊維は多数の単繊維(モノフィラメン
ト)に、望ましくは集束剤を附与、集束した繊維束の形
態、例えばストランド、チョップドストランド(C
S)、チョップドストランドマット(CM)、コンティ
ニュアスストランドマット(CSM)のような形態、或
はモノフィラメントの形態、例えばサーフェシングマッ
ト、ガラスペーパーのような形態で用いることが出来、
使用態様に特に限定はない。
The present fiber is formed by adding a sizing agent to a large number of monofilaments (monofilaments) to form a bundle of fibers, for example, strands or chopped strands (C).
S), chopped strand mat (CM), continuous strand mat (CSM), or monofilament, for example, surfacing mat, glass paper,
There is no particular limitation on the mode of use.

【0010】熱硬化性樹脂としては、液状の不飽和ポリ
エステル樹脂を用いる。液状の不飽和ポリエステル樹脂
はエチレングリコール等のグリコールと無水フタール、
無水マレイン酸等との縮合物をスチレン等のモノマーに
溶解したものであるが、それ自身では実質的硬化を生せ
ず、メチルエチルケトンパーオキサイド等のパーオキサ
イドのような硬化剤を加えることにより架橋反応(硬
化)が生ずる。硬化促進剤としてはナフテン酸コバルト
等が好適に使用できる。
A liquid unsaturated polyester resin is used as the thermosetting resin . Liquid unsaturated polyester resins are glycols such as ethylene glycol and anhydrous phthalates,
Condensate with maleic anhydride, etc. is used as a monomer such as styrene
Although it is dissolved , it does not substantially cure by itself, and a crosslinking reaction (curing) occurs when a curing agent such as peroxide such as methyl ethyl ketone peroxide is added. Cobalt naphthenate or the like can be preferably used as the curing accelerator.

【0011】繊維に硬化促進剤を被着させる方法に特
に限定はないが、硬化促進剤の溶液(或はエマルジョ
ン、サスペンジョン)を上述したような繊維にスプレ
ーし、或は繊維を上記溶液等に浸漬することにより、
硬化促進剤を繊維に均一に被着させることができる。
硬化促進剤の被着量は、樹脂及び硬化促進剤の種類、所
望の硬化速度に応じて定められるが、繊維の0.01
〜2wt%、望ましくは0.05〜1wt%とするのが
適当であり、液状の樹脂に混合する場合に比し、硬化促
進剤の使用量を大幅に減少させうる。なお、硬化促進剤
を含有させた集束剤を用いることにより、硬化促進剤を
集束と同時に被着させることもできる。
[0011] No particular limitation on the method of the curing accelerator to the fiber depositing, but the solution of the curing accelerator (or emulsion, suspension) was sprayed on the fiber as described above, or the present fibers above By immersing in a solution etc.,
The curing accelerator can be uniformly applied to the fibers.
The coating amount of the curing accelerator is determined according to the types of the resin and the curing accelerator, and the desired curing rate, but is 0.01% of the present fiber.
It is suitable to be about 2 wt%, preferably 0.05 to 1 wt%, and the amount of the curing accelerator used can be greatly reduced as compared with the case of mixing with a liquid resin. By using a sizing agent containing a curing accelerator, the curing accelerator is
It can also be applied simultaneously with focusing .

【0012】硬化促進剤の量があまり少ないと効果が充
分でなく、又この量があまり大きいと、繊維と樹脂と
の界面付近で硬化が急速に進行し、FRPの品質の劣化
を招来し易い。
[0012] insufficient effect and is much smaller amount of the curing accelerator, also when this amount is too large, curing in the vicinity of the interface between the fibers and the resin proceeds rapidly, and lead to FRP of quality degradation easy.

【0013】繊維に液状の樹脂を含浸させ、該樹脂
を要すれば加熱して樹脂を硬化させてFRPとする。F
RPの製造方法に特に限定はなく、ハンドレーアップ
法、スプレーアップ法、プレス法、レジンインジェクシ
ョンモールド法、引抜き成形法、フィラメントワインデ
ィング法等を適宜選択しうる。引抜き成形法、フィラメ
ントワインディング法においては、繊維に過剰の樹脂
が附与され、過剰の樹脂はダイス等によってスクイズさ
れるが、スクイズによって除去された樹脂中への繊維
からの硬化促進剤の移行は僅かであり、スクイズされた
樹脂を原料として再使用することができる。
The present fiber is impregnated with the present liquid resin, and the resin is heated if necessary to cure the resin to obtain FRP. F
The method for producing RP is not particularly limited, and a hand layup method, a spray up method, a pressing method, a resin injection molding method, a pultrusion molding method, a filament winding method or the like can be appropriately selected. Pultrusion method, in the filament winding method, is given whenever an excess of resin in the fibers, an excess of the resin is squeezed by the dies or the like, the curing accelerator from the fibers into the resin removed by the squeeze The transfer is slight and the squeezed resin can be reused as a raw material.

【0014】繊維に含浸せしめられた樹脂(この樹
脂中に硬化剤が含まれていることは前述の通りであ
る。)は、硬化促進剤の作用を受けて速やかに硬化す
る。本発明においては、硬化促進剤は繊維表面に被着
されているので、樹脂の硬化は繊維と樹脂の界面から開
始され、次第に外側の樹脂が硬化し収縮するので、硬化
した樹脂が繊維の表面に密着し易くなり、繊維表面にお
ける微少な亀裂の発生が防止され、FRPの耐水性が向
上する。
[0014] The fiber impregnation brought was present resin (this tree
As described above, the curing agent is contained in the fat.
It ) Is quickly hardening under the action of curing accelerator. In the present invention, since the curing accelerator is applied to the fiber surface, curing of the resin is initiated from the interface of the fiber and the resin gradually because the outer resin is cured to shrink, the cured resin of the fiber It becomes easy to adhere to the surface, the generation of minute cracks on the fiber surface is prevented, and the water resistance of FRP is improved.

【0015】又、硬化促進剤による硬化促進作用は、硬
化促進剤を樹脂中に混入した場合に比し遜色なく、且
つ、少量で充分であって、ポットライフを低下させるこ
となく、生産性を向上させ、均質なFRPをうることが
できる。なお、樹脂として樹脂に顔料、充填材、内
部離型剤等を配合した樹脂組成物を用いることもでき
る。又、樹脂中に少量の(ポットライフがあまり減少し
ない程度の)硬化促進剤を含有せしめるのが適当であ
る。
Further, the curing accelerating action of the curing accelerator is comparable to the case where the curing accelerator is mixed in the present resin, and a small amount is sufficient, without lowering pot life and productivity. Can be improved and a homogeneous FRP can be obtained. Incidentally, the present resin as the resin pigment, it is also possible to use a filler, a resin composition containing an internal mold release agent. In addition, it is suitable that the resin contains a small amount of a curing accelerator (so that the pot life is not significantly reduced).

【0016】[0016]

【作用】樹脂の硬化促進剤を繊維に被着させること
により、樹脂のポットライフを低下させることなく、
樹脂の硬化を促進し、FRPの生産性を高め、均質なF
RPをうる。又、樹脂の硬化を樹脂と本繊維の界面か
ら開始させ、界面付近の微少な亀裂の発生を防止し、F
RPの耐水性を向上させる。
[Function] By applying the curing accelerator of the present resin to the present fiber, the pot life of the present resin is not reduced,
Promotes resin curing, increases FRP productivity, and ensures uniform F
Get RP. Further, curing of the resin is started from an interface of the resin and the fibers, to prevent the occurrence of fine cracks in the vicinity of the interface, F
Improves the water resistance of RP.

【0017】[0017]

【実施例】直径11μのE−硝子繊維にポリ酢酸ピニル
系バインダを固形分として1wt%附与集束してなる
1,000m当りの重量2,300gのガラス繊維束製
ロービングの表面に、ナフテン酸コバルト(硬化促進
剤)のエマルジョンをスプレーし、ナフテン酸コバルト
を固形分として0.1wt%被着させた。このロービン
グに不飽和ポリエステル樹脂配合物〔配合物中の樹脂1
00重量部、顔料3重量部、メチルエチルケトンパーオ
キサイド(硬化剤)1重量部、ナフテン酸コバルト(硬
化促進剤)1重量部)を用いスプレーアップ法によりG
C30wt%のFRPを製造した。硬化促進剤を被着さ
せないロービングを用いた場合に比し、硬化時間を約5
0%短縮することができた。ポットライフも約0.5時
間と変わりなく、均質な、耐水性の良好なFRPをうる
ことができた。
EXAMPLE A naphthenic acid was applied on the surface of a roving made of a glass fiber bundle having a weight of 2,300 g per 1,000 m, which was obtained by concentrating 1 wt% of polypinyl acetate binder as a solid content on E-glass fiber having a diameter of 11 μm. Cobalt (acceleration of hardening
Agent) emulsion was sprayed to deposit 0.1 wt% cobalt naphthenate as a solid content. An unsaturated polyester resin blend [resin 1 in the blend was added to this roving.
00 parts by weight , pigment 3 parts by weight , methyl ethyl ketone peroxide (curing agent) 1 part by weight , cobalt naphthenate (curing accelerator) 1 part by weight ) by a spray-up method
C30 wt% FRP was manufactured. The curing time is about 5 times as compared with the case of using roving which does not apply the curing accelerator.
It was possible to shorten by 0%. The pot life was the same as that of about 0.5 hours, and it was possible to obtain a homogeneous FRP having good water resistance.

【0018】[0018]

【比較例】樹脂中に硬化促進剤を添加することによって
硬化時間を実施例と同一にするためには、樹脂中のメチ
ルエチルケトンパーオキサイド、ナフテン酸コバルトの
量を夫々3重量部、3重量部とする必要があり、硬化促
進剤の総使用量は実施例に比し約3倍となり、又ポット
ライフも15分に低下した。又硬化剤の使用量も3倍と
なった。又比較例の耐水性は不良であった。
To the same manner as in Example a curing time by adding a curing accelerator to the Comparative Examples] in the resin, methyl ethyl ketone peroxide, amount respectively 3 parts by weight of cobalt naphthenate in the resin, and 3 parts by weight The total amount of the curing accelerator used was about 3 times that of the example, and the pot life was also reduced to 15 minutes. Also, the amount of hardener used is tripled.
became. Further, the water resistance of the comparative example was poor.

【0019】[0019]

【発明の効果】ポットライフを低下させることなく、F
RPの生産性を高め、均質な耐水性の良好なFRPをう
ることができる。
EFFECT OF THE INVENTION F without reducing pot life.
It is possible to improve the productivity of RP and obtain a uniform FRP having good water resistance.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 不飽和ポリエステル樹脂の硬化を促進
する硬化促進剤を被着させたことを特徴とする不飽和ポ
リエステル樹脂補強用ガラス繊維
1. A unsaturated port, characterized in that the curing accelerator to accelerate were deposited the curing of unsaturated polyester resins
Glass fiber for polyester resin reinforcement
JP3016870A 1991-01-18 1991-01-18 Glass fiber for unsaturated polyester resin reinforcement Expired - Fee Related JPH0811867B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3016870A JPH0811867B2 (en) 1991-01-18 1991-01-18 Glass fiber for unsaturated polyester resin reinforcement

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3016870A JPH0811867B2 (en) 1991-01-18 1991-01-18 Glass fiber for unsaturated polyester resin reinforcement

Publications (2)

Publication Number Publication Date
JPH04240265A JPH04240265A (en) 1992-08-27
JPH0811867B2 true JPH0811867B2 (en) 1996-02-07

Family

ID=11928240

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3016870A Expired - Fee Related JPH0811867B2 (en) 1991-01-18 1991-01-18 Glass fiber for unsaturated polyester resin reinforcement

Country Status (1)

Country Link
JP (1) JPH0811867B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4748879B2 (en) * 2001-05-25 2011-08-17 旭化成イーマテリアルズ株式会社 Glass cloth and prepreg

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5245672A (en) * 1975-10-08 1977-04-11 Asahi Chemical Ind Treated material for reinforcement and its treating method

Also Published As

Publication number Publication date
JPH04240265A (en) 1992-08-27

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