JPH0826779A - Production of glass fiber treating agent - Google Patents

Production of glass fiber treating agent

Info

Publication number
JPH0826779A
JPH0826779A JP6168440A JP16844094A JPH0826779A JP H0826779 A JPH0826779 A JP H0826779A JP 6168440 A JP6168440 A JP 6168440A JP 16844094 A JP16844094 A JP 16844094A JP H0826779 A JPH0826779 A JP H0826779A
Authority
JP
Japan
Prior art keywords
polymerizable monomer
glass fiber
treating agent
epoxy resin
resin
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
Application number
JP6168440A
Other languages
Japanese (ja)
Other versions
JP3139295B2 (en
Inventor
Yoshiyuki Yokota
善行 横田
Takahiro Aoyama
孝浩 青山
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.)
Nippon Shokubai Co Ltd
Original Assignee
Nippon Shokubai 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 Nippon Shokubai Co Ltd filed Critical Nippon Shokubai Co Ltd
Priority to JP06168440A priority Critical patent/JP3139295B2/en
Publication of JPH0826779A publication Critical patent/JPH0826779A/en
Application granted granted Critical
Publication of JP3139295B2 publication Critical patent/JP3139295B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C25/00Surface treatment of fibres or filaments made from glass, minerals or slags
    • C03C25/10Coating
    • C03C25/24Coatings containing organic materials
    • C03C25/26Macromolecular compounds or prepolymers
    • C03C25/32Macromolecular compounds or prepolymers obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
    • C03C25/36Epoxy resins

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Organic Chemistry (AREA)
  • Surface Treatment Of Glass Fibres Or Filaments (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Materials Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Polymerisation Methods In General (AREA)
  • Graft Or Block Polymers (AREA)
  • Epoxy Resins (AREA)
  • Adhesives Or Adhesive Processes (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Macromonomer-Based Addition Polymer (AREA)

Abstract

PURPOSE:To produce the treating agent with which the affinity of glass fiber for a composite material consisting of synthetic resins, etc., can be enhanced and thereby, the glass fiber is provided with an excellent improving effect on material quality by esterifying a polymerizable monomer contg. a phosphate group with an epoxy resin and then, cololymerizing the esterification reaction product with another polymerizable monomer. CONSTITUTION:In this production, a polymerizable monomer contg. a phosphate group is esterified in an amount to provide a 0.1 to 25wt.% ratio to the amount of the final copolymer with an epoxy resin which has a number average molecular weight of about >=900 and is present in an organic solvent in a ratio by weight to the amount of the polymerizable monomer contg. a phsphate group of 2:1 to 1:10. Thereafter, the esterification reaction product is copolymerized with a 9 to 91wt.% in terms of polymeric solid matter of a reactive emulsifier or polymerizable monomer contg. a carboxyl group based on the amount of the final copolymer. Preferably, then, an amono resin is mixed into the resulting polymer solution in a >=5 pts.wt. ratio to 100 pts.wt. of the raw material epoxy resin. The polymer organic solvent solution thus produced as it is or an aqueous liquid dispersion obtained by dispersing this polymer solution in water is used as the objective glass fiber treating agent.

Description

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

【0001】[0001]

【産業上の利用分野】本発明はガラス繊維処理剤の製造
法に関し、詳細には、プリント回路基盤を始めとする各
種電気絶縁用積層板、強化プラスチック、強化セメン
ト、濾過材、吸音材、断熱材などとして用いられるガラ
ス繊維に対し、合成樹脂その他の複合材料との親和性を
高め、あるいは優れた処理効率を得ることのできるガラ
ス繊維処理剤の製造法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a glass fiber treating agent, and more specifically, to various laminated boards for electrical insulation including printed circuit boards, reinforced plastics, reinforced cements, filtration materials, sound absorbing materials, and heat insulation. The present invention relates to a method for producing a glass fiber treating agent capable of increasing the affinity of a glass fiber used as a material or the like with a synthetic resin or other composite material or obtaining an excellent treatment efficiency.

【0002】[0002]

【従来の技術】ガラス繊維は従来より、ガラスヤーン、
ガラスクロス、ガラスロービング、ガラスマット、ガラ
スチョップドストランド等様々の形態で、単独あるいは
複合材料として、プリント回路基盤を始めとする電気絶
縁用、強化プラスチック用、強化セメント用、濾材用、
吸音材用、断熱材用等の用途に使用されている。しかし
ながらガラス繊維は、該繊維と複合される熱硬化性樹脂
や熱可塑性樹脂、セメント等との親和性が劣るため、こ
れらとの親和性を高め、あるいはガラス繊維を繊維シー
ト状やは紙状等に加工したときの物性を高めるため、各
々の用途に応じてポリ酢酸ビニル系樹脂、ポリアクリル
酸エステル系樹脂、水溶性高分子、フェノール系樹脂、
ポリビニルアルコール系樹脂、メラミン系樹脂、尿素系
樹脂、ポリエステル系樹脂、エポキシ系樹脂等の各種樹
脂、或はこれらのエマルジョン等からなるガラス繊維処
理剤によって処理される。また、繊維化後複合材料とし
て使用するときの複合効果を高めるため、同様の処理剤
を所謂シランカップリング剤と併用することもある。
BACKGROUND OF THE INVENTION Glass fibers have traditionally been used in glass yarns,
In various forms such as glass cloth, glass roving, glass mat, glass chopped strand, alone or as a composite material, for electrical insulation including printed circuit boards, for reinforced plastics, for reinforced cement, for filter media,
It is used for sound absorbing materials, heat insulating materials, etc. However, since glass fibers have a poor affinity with thermosetting resins, thermoplastic resins, cement, etc. that are composited with the fibers, the affinity with them is increased, or glass fibers are used in the form of fiber sheet or paper. In order to enhance the physical properties when processed into, polyvinyl acetate resin, polyacrylic ester resin, water-soluble polymer, phenolic resin,
It is treated with various resins such as polyvinyl alcohol-based resin, melamine-based resin, urea-based resin, polyester-based resin and epoxy-based resin, or a glass fiber treating agent composed of an emulsion thereof. Further, in order to enhance the composite effect when it is used as a composite material after fiberization, the same treating agent may be used in combination with a so-called silane coupling agent.

【0003】ところがこれらの樹脂系ガラス繊維処理剤
は、たとえば電気絶縁用、強化セメント用、エンジニア
リングプラスチック用、ブレーキ・クラッチフェーシン
グ用などの摩擦材等の如く厳しい条件に曝される繊維複
合材として使用した場合、必ずしも十分な改質効果を有
するものとはいえず、より優れた改質効果を与えるガラ
ス繊維処理剤の開発が望まれている。
However, these resin-based glass fiber treating agents are used as fiber composite materials exposed to severe conditions such as friction materials for electrical insulation, reinforced cement, engineering plastics, brake / clutch facings, etc. In such a case, it cannot be said that it has a sufficient modifying effect, and there is a demand for the development of a glass fiber treating agent that gives a more excellent modifying effect.

【0004】尚、カルボキシル基含有アクリル化エポキ
シ樹脂を用いることによって改質効果を高めようとする
試みもある(特開昭63−35440号、同63−35
441号、同63−50599号公報等)が、上記の様
な用途においては依然として満足のいく改質効果は得ら
れていない。しかも、従来のガラス繊維処理剤では、ガ
ラス繊維の処理後焼付硬化処理を行なうときに、揮発性
低分子物質の発生によって処理炉の汚染(ヒューム)を
生じるという問題も指摘されている。また、生産性向上
や省エネルギーの観点から、焼付時間短縮の要求も高ま
っており、短時間の焼付けで優れた改質効果を発揮し得
る様なガラス繊維処理剤の開発が求められている。
There are also attempts to enhance the modifying effect by using a carboxyl group-containing acrylated epoxy resin (Japanese Patent Laid-Open Nos. 63-35440 and 63-35).
No. 441, No. 63-50599, etc.), however, a satisfactory modifying effect has not yet been obtained in the above applications. Moreover, it has been pointed out that conventional glass fiber treating agents have a problem in that when the glass fiber is subjected to bake hardening treatment after the treatment, volatile low-molecular substances are generated to cause contamination (fumes) in the treatment furnace. Further, from the viewpoint of improving productivity and saving energy, there is an increasing demand for shortening the baking time, and there is a demand for the development of a glass fiber treatment agent capable of exhibiting an excellent modifying effect by baking for a short time.

【0005】[0005]

【発明が解決しようとする課題】本発明は上述した様な
問題点に着目してなされたものであって、その目的は、
ガラス繊維処理時における焼付硬化処理工程で低分子量
物質の揮発等による処理炉の汚染等を生じることなく、
短時間の処理でガラス繊維に対し優れた改質効果を与え
得る様なガラス繊維処理剤の製造法を確立しようとする
ものである。
The present invention has been made by paying attention to the problems as described above, and its purpose is to:
Without causing contamination of the processing furnace due to volatilization of low molecular weight substances in the bake hardening process during glass fiber processing,
It is intended to establish a method for producing a glass fiber treating agent which can give an excellent modifying effect to glass fibers by a short-time treatment.

【0006】[0006]

【課題を解決するための手段】上記課題を解決すること
のできた本発明に係るガラス繊維処理剤の製造法の構成
は、エポキシ樹脂に燐酸基含有重合性単量体をエステル
化反応させて得られる反応生成物に、その他の重合性単
量体を共重合させるところに要旨が存在する。このとき
使用するその他の重合性単量体としては、反応性乳化剤
もしくはカルボキシル基含有重合性単量体が好ましく、
また上記の共重合を有機溶剤の存在下で行ない、これを
水性媒体中に分散させたものは、改質性能(耐溶剤性、
耐熱性、電気的特性等)、取扱い性、安定性等において
非常に良好な処理剤となる。また、上記共重合によって
得られる共重合体にアミノ樹脂を混合してから水性媒体
中に分散させたものは、ガラス繊維処理剤として一段と
優れた性能を示すものとなる。
The constitution of the method for producing a glass fiber treating agent according to the present invention, which has been capable of solving the above-mentioned problems, is obtained by subjecting an epoxy resin to an esterification reaction of a phosphoric acid group-containing polymerizable monomer. The gist resides in that the reaction product obtained is copolymerized with another polymerizable monomer. As the other polymerizable monomer used at this time, a reactive emulsifier or a carboxyl group-containing polymerizable monomer is preferable,
Further, the above-mentioned copolymerization is carried out in the presence of an organic solvent, and this is dispersed in an aqueous medium to obtain a reforming property (solvent resistance,
It is a very good treatment agent in terms of heat resistance, electrical characteristics, etc.), handleability, stability, etc. In addition, a copolymer obtained by the above copolymerization and mixed with an amino resin and then dispersed in an aqueous medium show a further excellent performance as a glass fiber treating agent.

【0007】[0007]

【作用】上記の様に本発明では、エポキシ樹脂に燐酸基
含有重合性単量体をエステル化反応させて得られる反応
生成物に、その他の重合性単量体を共重合させることに
よってガラス繊維処理剤を製造するものであり、ここで
使用するエポキシ樹脂の種類は特に限定されないが、中
でも特に好ましいのはビスフェノール型エポキシ樹脂で
あり、とりわけ1分子当たり1〜2個のエポキシ基を有
し、数平均分子量が900以上のものが好ましい。この
様なエポキシ樹脂の市販品としては、、例えば油化シェ
ルエポキシ社製の「エピコート#1001」、「同10
04」、「同1007」、「同1009」、「同101
0」等が挙げられる。尚、数平均分子量が900未満の
エポキシ樹脂では、最終的に得られるガラス繊維処理剤
の耐溶剤性、耐アルカリ性、耐酸性、耐熱性、電気的特
性等が不十分になることがある。
As described above, in the present invention, the glass fiber is obtained by copolymerizing the reaction product obtained by esterifying the epoxy resin with the phosphoric acid group-containing polymerizable monomer and the other polymerizable monomer. The type of epoxy resin used for producing a treating agent is not particularly limited, but a bisphenol type epoxy resin is particularly preferable, and has 1 to 2 epoxy groups per molecule, A number average molecular weight of 900 or more is preferable. Commercially available products of such an epoxy resin include, for example, "Epicoat # 1001" and "Same 10" manufactured by Yuka Shell Epoxy Co., Ltd.
04 ”,“ 1007 ”,“ 1009 ”,“ 101 ”
0 ”and the like. When the number average molecular weight of the epoxy resin is less than 900, the solvent resistance, alkali resistance, acid resistance, heat resistance, electrical characteristics, etc. of the finally obtained glass fiber treating agent may be insufficient.

【0008】上記エポキシ樹脂の使用量は、耐溶剤性、
耐酸性、耐アルカリ性、耐水性、耐熱性等を高め且つガ
ラス繊維処理後の焼付硬化処理時における揮発性低分子
量物による処理炉の汚染を一層効果的に防止するという
観点から、後述する燐酸基含有重合性単量体に対し、固
形分換算の重量比で2:1〜1:10の範囲から選定す
ることが望ましい。
The amount of the above epoxy resin used depends on the solvent resistance,
From the viewpoint of enhancing acid resistance, alkali resistance, water resistance, heat resistance and the like, and more effectively preventing contamination of the processing furnace by volatile low molecular weight substances during baking and curing treatment after glass fiber treatment, the phosphate group described below is used. It is desirable to select from the range of 2: 1 to 1:10 in terms of solid content in terms of weight ratio with respect to the contained polymerizable monomer.

【0009】次に燐酸基含有重合性単量体としては、
(メタ)アクリロイルオキシエチルアシッドホスフェー
ト等の(メタ)アクリロイルオキシアルキルアシッドホ
スフェート類またはそのアルキレンオキシド付加物、
(メタ)アクリロイルオキシアルキルアシッドホスファ
イト類またはそのアルキレンオキシド付加物、グリシジ
ル(メタ)アクリレートやメチルグリシジル(メタ)ア
クリレート等のエポキシ基含有ビニル系モノマーと燐酸
や亜燐酸あるいはそれらの酸性エステル類とのエステル
化合物等が挙げられ、これらは単独で使用し得るほか2
種以上を適宜併用することができる。
Next, as the phosphoric acid group-containing polymerizable monomer,
(Meth) acryloyloxyethyl acid phosphate and other (meth) acryloyloxyalkyl acid phosphates or alkylene oxide adducts thereof,
Of (meth) acryloyloxyalkyl acid phosphites or their alkylene oxide adducts, epoxy group-containing vinyl monomers such as glycidyl (meth) acrylate and methylglycidyl (meth) acrylate, and phosphoric acid, phosphorous acid or their acidic esters Examples thereof include ester compounds, which may be used alone or 2
One or more species can be used in combination as appropriate.

【0010】これら燐酸基含有重合性単量体の使用量
は、得られる共重合体中に占める比率で固形分換算で
0.1〜25重量%、より好ましくは0.5〜20重量
%の範囲が好ましく、0.1重量%未満では、ガラス繊
維処理剤として使用したときの耐熱性、耐溶剤性、電気
的特性、樹脂の分散安定性などが不足気味になる他、ガ
ラス繊維の処理を行なうに当たり、焼付硬化処理時に揮
発性低分子物質の発生によって処理炉の汚染(ヒュー
ム)を起こしたり、低温硬化性の不足や硬化時間が長く
なるといった傾向が現われてくる。一方25重量%を超
える過多になると、たとえば改質ガラス繊維紙などを製
造する時の可撓性が低下したり、耐水性や電気的特性が
不良になるといった傾向が現われてくる。
The amount of the phosphoric acid group-containing polymerizable monomer used is 0.1 to 25% by weight, more preferably 0.5 to 20% by weight, based on the solid content in terms of the proportion in the obtained copolymer. The range is preferable, and if it is less than 0.1% by weight, heat resistance, solvent resistance, electrical characteristics, dispersion stability of resin, etc. when used as a glass fiber treating agent may be insufficient, and glass fiber treatment In doing so, there is a tendency that volatile low-molecular substances are generated during the bake-curing process to cause contamination (fumes) in the processing furnace, insufficient low-temperature curability, and a long curing time. On the other hand, if the amount exceeds 25% by weight, flexibility tends to decrease when producing modified glass fiber paper or the like, and water resistance and electrical characteristics tend to deteriorate.

【0011】次に、本発明で使用するその他の重合性単
量体としては、(メタ)アクリル酸、マレイン酸、フマ
ール酸、イタコン酸等のカルンボキシル基含有重合性単
量体、(メタ)アクリル酸メチル、(メタ)アクリル酸
エチル、(メタ)アクリル酸プロピル、(メタ)アクリ
ル酸n−イソブチル、(メタ)アクリル酸イソブチル、
(メタ)アクリル酸t−ブチル、(メタ)アクリル酸n
−アミル、(メタ)アクリル酸イソアミル、(メタ)ア
クリル酸n−ヘキシル、(メタ)アクリル酸シクロヘキ
シル、(メタ)アクリル酸n−オクチル、(メタ)アク
リル酸2エチルヘキシル、(メタ)アクリル酸デシル、
(メタ)アクリル酸ドデシル等の(メタ)アクリル酸エ
ステル、スチレン、ビニルトルエン、2−メチルスチレ
ン、t−ブチルスチレン、クロロスチレン等のスチレン
系重合性単量体、(メタ)アクリル酸ヒドロキシエチ
ル、(メタ)アクリル酸ヒドロキシプロピル等のヒドロ
キシル基含有(メタ)アクリル酸エステル系単量体、N
−メチロール(メタ)アクリルアミド等のN−置換(メ
タ)アクリルアミド系単量体、アクリロニトリルなど、
更には反応性乳化剤等を使用することができ、これらは
単独で使用できる他、必要に応じて2種以上を適宜併用
することができる。
Next, other polymerizable monomers used in the present invention include (meth) acrylic acid, maleic acid, fumaric acid, itaconic acid and the like, a carmboxyl group-containing polymerizable monomer, and (meth) acryl. Methyl acid, ethyl (meth) acrylate, propyl (meth) acrylate, n-isobutyl (meth) acrylate, isobutyl (meth) acrylate,
T-butyl (meth) acrylate, n (meth) acrylate
-Amyl, isoamyl (meth) acrylate, n-hexyl (meth) acrylate, cyclohexyl (meth) acrylate, n-octyl (meth) acrylate, 2-ethylhexyl (meth) acrylate, decyl (meth) acrylate,
(Meth) acrylic acid ester such as dodecyl (meth) acrylate, styrene-based polymerizable monomer such as styrene, vinyltoluene, 2-methylstyrene, t-butylstyrene, chlorostyrene, hydroxyethyl (meth) acrylate, Hydroxyl group-containing (meth) acrylic acid ester-based monomer such as hydroxypropyl (meth) acrylate, N
-N-substituted (meth) acrylamide-based monomers such as methylol (meth) acrylamide, acrylonitrile,
Furthermore, a reactive emulsifying agent or the like can be used, and these can be used alone, or two or more kinds can be appropriately used in combination as necessary.

【0012】上記その他の重合性単量体の中でも特に好
ましいのは、カルボキシル基含有重合性単量体および反
応性乳化剤であり、これらを夫々単独であるいは2種を
併用すると、耐溶剤性、耐熱性、樹脂の分散安定性等に
おいて一段と優れた処理剤を得ることができる。中でも
反応性乳化剤は、水性分散型のガラス繊維処理剤とする
ときの分散安定性を高めるのに卓効を示す。その様な反
応性乳化剤の具体例としては、下記一般式(a),
(b)で示されるスルホコハク酸エステル系反応性乳化
剤、
Of the above-mentioned other polymerizable monomers, particularly preferable are the carboxyl group-containing polymerizable monomer and the reactive emulsifier, and when these are used alone or in combination of two kinds, solvent resistance and heat resistance are improved. It is possible to obtain a treating agent which is much more excellent in the properties, the dispersion stability of the resin, and the like. Among them, the reactive emulsifier is effective in enhancing the dispersion stability when it is used as an aqueous dispersion type glass fiber treating agent. Specific examples of such a reactive emulsifier include the following general formula (a),
A sulfosuccinate-based reactive emulsifier represented by (b),

【0013】[0013]

【化1】 Embedded image

【0014】例えば花王社製の「ラムテルS−12
0」、「同S−180、「同S−180A」や三洋化成
社製の「エレミノールJS−2」等、あるいは下記一般
式(c)で示されるアルキルフェノールエーテル系反応
性乳化剤、
For example, "Ramtel S-12" manufactured by Kao Corporation
0 "," S-180, "S-180A", "Eleminol JS-2" manufactured by Sanyo Kasei Co., Ltd., or an alkylphenol ether-based reactive emulsifier represented by the following general formula (c):

【0015】[0015]

【化2】 Embedded image

【0016】例えば第一工業製薬社製の「アクアロンH
S−10」、「同RN−20」等が挙げられる。
For example, "Aqualon H" manufactured by Dai-ichi Kogyo Seiyaku Co., Ltd.
"S-10", "RN-20" and the like.

【0017】上記その他の重合性単量体の使用量は、得
られる共重合体中に占める比率で固形分換算で9〜91
重量%、より好ましくは15〜60重量%の範囲が望ま
しく、その配合量が不足する場合は、焼付硬化処理時の
炉の汚染(ヒューム)が生じ易くなる他、耐溶剤性、耐
アルカリ性、耐酸性等が不十分となり、逆に多過ぎる場
合は、電気的特性等が不十分になるといった傾向が現わ
れてくる。
The amount of the above-mentioned other polymerizable monomer used is 9 to 91 in terms of solid content in terms of the ratio in the copolymer obtained.
%, More preferably 15 to 60% by weight, and if the blending amount is insufficient, the furnace is likely to be contaminated (fumes) during bake-hardening treatment, and solvent resistance, alkali resistance, and acid resistance are also high. Insufficient properties, and conversely, if too much, electrical properties, etc. tend to be insufficient.

【0018】本発明を実施するに当たっては、まず前記
エポキシ樹脂に燐酸基含有重合性単量体をエステル化反
応させ、得られる反応生成物(エポキシ燐酸エステル基
含有重合性単量体)をその他の重合性単量体と共重合さ
せることによって行なわれる。
In carrying out the present invention, first, the above epoxy resin is subjected to an esterification reaction with a phosphoric acid group-containing polymerizable monomer, and the resulting reaction product (epoxy phosphoric acid ester group-containing polymerizable monomer) is converted into another product. It is carried out by copolymerizing with a polymerizable monomer.

【0019】このエステル化反応は、通常、窒素等の非
酸化性ガス雰囲気下、一般的には有機溶剤、好ましくは
メタノール、エタノール、n−プロパノール、イソプロ
パノール、n−ブタノール、s−ブタノール、t−ブタ
ノール、イソブタノール等のアルキルアルコール類、メ
チルセロソルブ、エチルセロソルブ、プロピルセロソル
ブ、ブチルセロソルブ、メチルカルビトール、エチルカ
ルビトール、プロピレングリコールメチルエーッテル、
プロピレングリコールエチルエーテル、ジプロピレング
リコールメチルエーテル、トリプロピレングリコールメ
チルエーテル等のエーテルエステル類、その他ジオキサ
ン、ジメチルホルムアミド、ジアセトンアルコール類等
の単独もしくは2種以上の混合溶剤の存在下、50〜1
50℃程度で1〜10時間程度加熱撹拌し、生成する水
を逐次反応系外へ除去することによって行なわれる。こ
の反応により、エポキシ樹脂中のエポキシ基と燐酸基含
有重合性単量体中の燐酸基がエステル化反応し、エポキ
シ燐酸エステル基含有重合性単量体が得られる。即ちこ
の単量体は、重合性2重結合を残したままで該分子中の
燐酸基がエポキシ樹脂のエポキシ基とエステル化反応に
より結合したものであり、エポキシ基の一部はエステル
化反応によって結合し、一部のエポキシ基は反応性を残
した状態で残存しているものと思われる。
This esterification reaction is usually carried out under an atmosphere of non-oxidizing gas such as nitrogen, generally an organic solvent, preferably methanol, ethanol, n-propanol, isopropanol, n-butanol, s-butanol, t-. Butanol, alkyl alcohols such as isobutanol, methyl cellosolve, ethyl cellosolve, propyl cellosolve, butyl cellosolve, methyl carbitol, ethyl carbitol, propylene glycol methyl ether,
50 to 1 in the presence of ether ester such as propylene glycol ethyl ether, dipropylene glycol methyl ether, tripropylene glycol methyl ether, etc., and other dioxane, dimethylformamide, diacetone alcohol, etc., alone or in a mixed solvent of two or more kinds.
It is carried out by heating and stirring at about 50 ° C. for about 1 to 10 hours, and successively removing the produced water out of the reaction system. By this reaction, the epoxy group in the epoxy resin and the phosphoric acid group in the phosphoric acid group-containing polymerizable monomer undergo an esterification reaction to obtain an epoxy phosphoric acid ester group-containing polymerizable monomer. That is, this monomer is one in which the phosphoric acid group in the molecule is bonded to the epoxy group of the epoxy resin by an esterification reaction while leaving a polymerizable double bond, and a part of the epoxy group is bonded by an esterification reaction. However, it is considered that some of the epoxy groups remain in a reactive state.

【0020】次いで、得られる反応生成物とその他の重
合性単量体を、アゾビスイソブチロニトリル等のアゾ系
化合物やベンゾイルパーオキサイド等の過酸化物などの
ラジカル重合開始剤を用いて共重合させる。この反応
は、同一の反応容器にその他の共重合成単量体およびラ
ジカル重合開始剤を追加することによって連続的に行な
ってもよく、あるいはエステル化反応生成物を一旦取り
出し、他の反応容器で共重合反応を行なうことも可能で
ある。
Next, the obtained reaction product and other polymerizable monomers are copolymerized with a radical polymerization initiator such as an azo compound such as azobisisobutyronitrile or a peroxide such as benzoyl peroxide. Polymerize. This reaction may be carried out continuously by adding other co-polymerizable monomers and radical polymerization initiators to the same reaction vessel, or the esterification reaction product is once taken out and placed in another reaction vessel. It is also possible to carry out a copolymerization reaction.

【0021】該共重合反応の条件も特に限定されない
が、一般的には上記エステル化反応に使用したのと同様
の有機溶剤を単独で若しくは2種以上の混合溶剤として
使用し、更にはこれらに少量の水を混合した溶剤を使用
し、0.1〜10重量%程度の重合開始剤の存在下、7
0〜150℃の範囲で行なわれる。反応時間も特に限定
されないが、1〜10時間程度で反応は十分に進行す
る。
The conditions of the copolymerization reaction are not particularly limited, but generally, the same organic solvent as that used in the above esterification reaction is used alone or as a mixed solvent of two or more kinds, and further in these. Using a solvent mixed with a small amount of water, in the presence of about 0.1 to 10% by weight of a polymerization initiator,
It is carried out in the range of 0 to 150 ° C. Although the reaction time is not particularly limited, the reaction proceeds sufficiently in about 1 to 10 hours.

【0022】かくして得られる共重合体溶液は、そのま
まの有機溶剤溶液としてガラス繊維処理剤として使用
し、或はこれに硬化剤として少量のアミノ樹脂を配合し
ガラス繊維処理剤としての性能を一段と高めて使用する
ことができる。ここで使用されるアミノ樹脂としては、
例えばアルキルエーテル化メラミン系樹脂、アルキルエ
ーテル化ベンゾグアナミン系樹脂、アルキルエーテル化
尿素系樹脂などが単独でもしくは適宜2種以上を組み合
わせて使用することができ、これらアミノ樹脂を併用す
ると、ガラス繊維処理剤として使用した時に、共重合体
中に残っているエポキシ基と上記アミノ樹脂との反応に
より、耐溶剤性、耐水性、耐熱性、耐アルカリ性等にお
いて一段と優れた効果を得ることができる。該アミノ樹
脂の併用効果は、前記エステル化反応の原料として使用
したエポキシ樹脂100重量部に対する固形分換算で5
重量部以上使用することによって有効に発揮されるが、
配合量が多過ぎると焼付硬化処理時の炉の汚染(ヒュー
ム)が生じ易くなるといった難点が現われてくるので、
50重量部以下に抑えることが望ましい。
The copolymer solution thus obtained is used as a glass fiber treating agent as it is as an organic solvent solution, or a small amount of an amino resin is added to this as a curing agent to further enhance the performance as a glass fiber treating agent. Can be used. As the amino resin used here,
For example, alkyl etherified melamine-based resin, alkyl etherified benzoguanamine-based resin, alkyl etherified urea-based resin and the like can be used singly or in a suitable combination of two or more kinds. When these amino resins are used in combination, a glass fiber treating agent can be used. When used as, the reaction between the epoxy group remaining in the copolymer and the amino resin makes it possible to obtain more excellent effects in solvent resistance, water resistance, heat resistance, alkali resistance and the like. The effect of using the amino resin in combination is 5 in terms of solid content based on 100 parts by weight of the epoxy resin used as the raw material for the esterification reaction.
It can be effectively used by using more than 1 part by weight,
If the blending amount is too large, there will be a problem that the furnace is likely to be contaminated (fumes) during the bake hardening treatment.
It is desirable to limit the amount to 50 parts by weight or less.

【0023】上記の様に本発明のガラス繊維処理剤は、
共重合反応によって得られる有機溶剤溶液をそのままで
或はこれにアミノ樹脂を配合することにより、有機溶剤
溶液の状態で電気絶縁用、強化プラスチック用、強化セ
メント用等として用いられるガラス繊維用処理剤として
使用できるが、より好ましくは、ガラス繊維に対する処
理効果を一層高めると共に取扱い性を高めるため、得ら
れる有機溶剤溶液を水に分散せしめ、水性分散液として
使用するのがよく、その様な水分散液は、上記共重合反
応によって得られる反応液を適量の水に分散させること
によって容易に得られる。この時、その他の重合性単量
体としてカルボキシル基含有単量体や反応性乳化剤を使
用したものは、水への分散を一層容易に行なうことがで
きると共に、より安定な水性分散液を得ることができる
ので好ましい。この水分散液には、更に必要に応じてシ
ランカップリング剤等の改質補助剤を、本発明の特徴を
阻害しない範囲で配合することも勿論可能である。
As described above, the glass fiber treating agent of the present invention is
A treatment agent for glass fiber, which is used for electrical insulation, reinforced plastics, reinforced cement, etc. in an organic solvent solution as it is or by adding an amino resin to the organic solvent solution obtained by the copolymerization reaction. However, it is more preferable to disperse the obtained organic solvent solution in water and to use it as an aqueous dispersion in order to further enhance the treatment effect on the glass fiber and the handleability, and such an aqueous dispersion. The liquid is easily obtained by dispersing the reaction liquid obtained by the above copolymerization reaction in an appropriate amount of water. At this time, those using a carboxyl group-containing monomer or a reactive emulsifying agent as the other polymerizable monomer can be more easily dispersed in water, and a more stable aqueous dispersion can be obtained. It is possible to do so, which is preferable. It is of course possible to further mix a modification aid such as a silane coupling agent with the aqueous dispersion within a range not impairing the features of the present invention, if necessary.

【0024】また、水分散液とするに当たっては、共重
合反応液に予め水分散液のpHが4〜11になる程度の
量の塩基性化合物、例えばアンモニアやアミン等を加え
て反応液を中和しておけば、水への分散を一層容易に行
なうことができるので好ましい。
In preparing the aqueous dispersion, a basic compound such as ammonia or amine is added to the copolymerization reaction solution in an amount such that the pH of the aqueous dispersion is 4 to 11 beforehand. It is preferable to mix them, because they can be more easily dispersed in water.

【0025】アミノ樹脂を配合する場合の配合時期は、
共重合反応液を水に分散させる前とするのがよく、それ
により、水に難溶性(難分散性)である比較的高分子量
のアミノ樹脂であっても、容易に分散が可能になるとい
う利点を享受することができる。即ち、上記の様にして
得た共重合反応液にアミノ樹脂を混合してから水に分散
させる方法を採用すると、上記共重合反応生成物との共
存によってアミノ樹脂の水分散性が著しく高められ、比
較的高分子量のアミノ樹脂であっても支障なく簡単に分
散させることができ、その結果、ガラス繊維処理剤とし
て用いた時の焼付処理工程で揮発性低分子量物による処
理炉の汚染がより効果的に抑えられると共に、耐溶剤
性、耐熱性、耐水性、耐アルカリ性等の点でも一段と優
れた性能を発揮するガラス繊維処理剤を得ることが可能
となる。
When compounding the amino resin,
It is preferable to disperse the copolymerization reaction liquid in water, which allows even a relatively high molecular weight amino resin that is poorly soluble in water (hardly dispersible) to be easily dispersed. You can enjoy the benefits. That is, when a method of mixing an amino resin with the copolymerization reaction liquid obtained as described above and then dispersing it in water is employed, the coexistence with the copolymerization reaction product remarkably enhances the water dispersibility of the amino resin. However, even a relatively high molecular weight amino resin can be easily dispersed without any trouble, and as a result, contamination of the processing furnace due to volatile low molecular weight substances during the baking process when used as a glass fiber processing agent is more effective. It is possible to obtain a glass fiber treating agent which is effectively suppressed and exhibits further excellent performance in terms of solvent resistance, heat resistance, water resistance, alkali resistance and the like.

【0026】[0026]

【実施例】以下、実施例を挙げて本発明の構成および作
用効果をより詳細に説明するが、本発明はもとより下記
実施例によって制限を受けるものではなく、前後記の趣
旨に適合し得る範囲で適当に変更して実施することも可
能であり、それらはいずれも本発明の技術的範囲に含ま
れる。尚、下記実施例において%および部とあるのは、
特に断らない限り重量%および重量部を意味する。
EXAMPLES The constitutions and effects of the present invention will be described below in more detail with reference to Examples. However, the present invention is not limited by the following Examples, and is within a range applicable to the points of the preceding and following statements. It is also possible to carry out by appropriately changing the above, and all of them are included in the technical scope of the present invention. In the following examples,% and parts mean
Unless otherwise specified, it means% by weight and part by weight.

【0027】実施例1 撹拌機、還流冷却器、滴下ロート、温度計および窒素ガ
ス吹き込み管を備えた反応器に、エポキシ樹脂(「エピ
コート#1009」油化シェルエポキシ社製)300
部、モノ(2−メタクリロイルオキシエチル)アシッド
ホスフェート(「ライトエステルPM」共栄化学社製)
40部、ブチルセロソルブ300部、N−ブタノール7
3部を仕込み、窒素置換の後105℃に昇温し、撹拌下
に2時間保持することによってエステル化反応を行なっ
た。
Example 1 A reaction vessel equipped with a stirrer, a reflux condenser, a dropping funnel, a thermometer and a nitrogen gas blowing tube was charged with 300 epoxy resin (“Epicoat # 1009” manufactured by Yuka Shell Epoxy Co., Ltd.).
Part, mono (2-methacryloyloxyethyl) acid phosphate (“Light Ester PM” manufactured by Kyoei Chemical Co., Ltd.)
40 parts, butyl cellosolve 300 parts, N-butanol 7
After 3 parts were charged and the atmosphere was replaced with nitrogen, the temperature was raised to 105 ° C., and the mixture was kept under stirring for 2 hours to carry out an esterification reaction.

【0028】次いでこの反応液に、メチルメタクリレー
ト40部、ブチルアクリレート40部、スチレン80
部、アゾビスイソブチロニトリル6部の混合液を、撹拌
下に1.5時間かけて滴下し、105℃で2時間撹拌を
続けて共重合を行なった後、ブチルセロソルブ500部
で希釈してから、50℃以下まで冷却し、次いでメラミ
ン樹脂[「ニカラックMX−706」三和ケミカル社
製]306部を加え、1時間撹拌することによりガラス
繊維処理剤Aを得た。
Next, 40 parts of methyl methacrylate, 40 parts of butyl acrylate and 80 parts of styrene were added to this reaction solution.
Part, and a mixed solution of 6 parts of azobisisobutyronitrile were added dropwise over 1.5 hours with stirring, and the mixture was continuously stirred at 105 ° C. for 2 hours for copolymerization, and then diluted with 500 parts of butyl cellosolve. Then, the mixture was cooled to 50 ° C. or lower, and then 306 parts of melamine resin [“NICALAC MX-706” manufactured by Sanwa Chemical Co., Ltd.] was added, and the mixture was stirred for 1 hour to obtain a glass fiber treatment agent A.

【0029】実施例2 撹拌機、還流冷却器、滴下ロート、温度計および窒素ガ
ス吹き込み管を備えた反応器に、エポキシ樹脂(「エピ
コート#1009」油化シェルエポキシ社製)300
部、モノ(2−メタクリロイルオキシエチル)アシッド
ホスフェート(「ライトエステルPM」共栄化学社製)
40部、ブチルセロソルブ300部、N−ブタノール7
3部を仕込み、窒素置換の後105℃に昇温し、撹拌下
に2時間保持することによってエステル化反応を行なっ
た。
Example 2 A reactor equipped with a stirrer, a reflux condenser, a dropping funnel, a thermometer and a nitrogen gas blowing tube was charged with 300 epoxy resin (“Epicoat # 1009” manufactured by Yuka Shell Epoxy Co., Ltd.).
Part, mono (2-methacryloyloxyethyl) acid phosphate (“Light Ester PM” manufactured by Kyoei Chemical Co., Ltd.)
40 parts, butyl cellosolve 300 parts, N-butanol 7
After 3 parts were charged and the atmosphere was replaced with nitrogen, the temperature was raised to 105 ° C. and the mixture was kept under stirring for 2 hours to carry out an esterification reaction.

【0030】次いでこの反応液に、メチルメタクリレー
ト40部、ブチルアクリレート40部、スチレン80
部、アゾビスイソブチロニトリル6部の混合液を、撹拌
下に1.5時間かけて滴下し、105℃で2時間撹拌を
続けて共重合を行なった後、トリエチルアミン15部を
添加し、撹拌混合した後、撹拌下に脱イオン水535部
を30分かけて滴下した。その後更に60分間撹拌して
水分散性樹脂液を得た。
Then, 40 parts of methyl methacrylate, 40 parts of butyl acrylate and 80 parts of styrene were added to the reaction solution.
Part, and a mixed solution of 6 parts of azobisisobutyronitrile were added dropwise with stirring over 1.5 hours, and the mixture was continuously stirred at 105 ° C. for 2 hours to perform copolymerization, and then 15 parts of triethylamine was added, After stirring and mixing, 535 parts of deionized water was added dropwise with stirring over 30 minutes. Then, the mixture was further stirred for 60 minutes to obtain a water-dispersible resin liquid.

【0031】上記水分散樹脂液に、メラミン樹脂[「ニ
カラックMX−706」三和ケミカル社製]306部を
加え、1時間撹拌した後、脱イオン水122部を加えて
均一に混合し、ガラス繊維処理剤Bを得た。
To the above water-dispersed resin solution, 306 parts of melamine resin ["Nikalac MX-706" manufactured by Sanwa Chemical Co., Ltd.] was added, and after stirring for 1 hour, 122 parts of deionized water was added and uniformly mixed to obtain a glass. A fiber treatment agent B was obtained.

【0032】実施例3〜7 表1に示す様に使用原料の種類と使用量を変えた以外は
上記実施例2と同様にして、ガラス繊維処理剤C〜Gを
得た。 実施例8 前記実施例2と全く同様にしてエステル化反応および共
重合反応を行なった後、トリエチルアミン6部を加えて
からメラミン樹脂(同前)306部を加えて撹拌混合
し、次いで撹拌下に脱イオン水657部を30分かけて
滴下し、更に60分間強撹拌してガラス繊維処理剤Hを
得た。
Examples 3 to 7 As shown in Table 1, glass fiber treating agents C to G were obtained in the same manner as in Example 2 except that the kind and amount of raw materials used were changed. Example 8 After performing an esterification reaction and a copolymerization reaction in exactly the same manner as in Example 2, 6 parts of triethylamine was added, and then 306 parts of a melamine resin (same as above) was added and mixed with stirring, and then, with stirring. Deionized water (657 parts) was added dropwise over 30 minutes, followed by vigorous stirring for 60 minutes to obtain a glass fiber treating agent H.

【0033】[0033]

【表1】 [Table 1]

【0034】(性能評価試験)市販のガラスフィラメン
トペーパー(坪量60g/m2 )を電気炉で550℃で
2分間加熱することによってバインダーを分解除去し、
上記実施例1〜7で得たガラス繊維処理剤A〜Gをガラ
スフィラメントペーパーに対し10%となる様に含浸
し、次いで140℃で30分間加熱して乾燥・硬化させ
た。このガラス繊維処理紙の耐溶剤性と耐熱性を下記の
方法で測定し、表2に示す結果を得た。
(Performance Evaluation Test) Commercially available glass filament paper (basis weight: 60 g / m 2 ) was heated in an electric furnace at 550 ° C. for 2 minutes to decompose and remove the binder,
The glass fiber treating agents A to G obtained in Examples 1 to 7 were impregnated into the glass filament paper so as to be 10%, and then heated at 140 ° C. for 30 minutes to be dried and cured. The solvent resistance and heat resistance of this glass fiber treated paper were measured by the following methods, and the results shown in Table 2 were obtained.

【0035】また、上記で得た各ガラス繊維処理紙に、
下記組成のエポキシ樹脂含浸液を含浸・乾燥してプリプ
レグを作り、該プリプレグ16枚と片面に銅箔を積み重
ね、温度170℃、圧力50kg/cm2 で60分間プ
レスし、積層成形して厚み1.6mmの銅張り積層板を
得、その絶縁抵抗および積層板の外観を調べ、結果を表
2に併記した。 (エポキシ樹脂含浸液組成) エピコート#1001−B−80 50部 メチルエチルケトン 32部 ジシアンジアミド 1.6部 メチルセロソルブ 16部 ベンジルジメチルアミン 0.008部
In addition, each glass fiber treated paper obtained above,
An epoxy resin impregnating solution having the following composition is impregnated and dried to form a prepreg, 16 prepregs and a copper foil are stacked on one side, pressed at a temperature of 170 ° C. and a pressure of 50 kg / cm 2 for 60 minutes, and laminated to have a thickness of 1 A copper-clad laminate having a thickness of 0.6 mm was obtained, its insulation resistance and the appearance of the laminate were examined, and the results are also shown in Table 2. (Epoxy resin impregnating liquid composition) Epicoat # 1001-B-80 50 parts Methyl ethyl ketone 32 parts Dicyandiamide 1.6 parts Methyl cellosolve 16 parts Benzyldimethylamine 0.008 parts

【0036】(物性試験法) 耐溶剤性:50℃のメチルセロソルブに5分間浸漬した
後、直ちにJISP 8113に従って引張強度を測定
する。 耐熱性:120℃の雰囲気中における引張強度をJIS
P 8113に従って測定する。 絶縁抵抗:JIS C 6481に規定する印刷回路用
銅張積層板試験法に従って測定する。 耐ヒューム性:厚さ0.23mmのブリキ板を15×2
0cmに切って精秤し(これをW1 とする)、ガラス繊
維処理剤を10g/m2 となる様に塗布し、100℃で
60分間乾燥して精秤する(これをW2とする)。更に
160℃で20分間乾燥して精秤し(これをW3 とす
る)、次式により加熱減量率M(%)を算出してヒュー
ム発生量の基準とする。 M=[(W2 −W3 )/(W2 −W1 )]×100
(Physical property test method) Solvent resistance: Immersed in methyl cellosolve at 50 ° C. for 5 minutes and then immediately measured the tensile strength according to JISP 8113. Heat resistance: JIS tensile strength in an atmosphere of 120 ° C
Measure according to P 8113. Insulation resistance: Measured according to the copper clad laminate test method for printed circuits specified in JIS C 6481. Fume resistance: 0.23 mm thick tin plate 15 x 2
Cut to 0 cm and precisely weigh (this is W 1 ), apply glass fiber treating agent to 10 g / m 2 , dry at 100 ° C. for 60 minutes, and weigh accurately (this is W 2 ). ). Further, it is dried at 160 ° C. for 20 minutes and precisely weighed (this is referred to as W 3 ), and the heating weight loss rate M (%) is calculated by the following formula and used as the standard of fume generation amount. M = [(W 2 -W 3 ) / (W 2 -W 1)] × 100

【0037】[0037]

【表2】 [Table 2]

【0038】比較例1〜6 前記実施例例に従い、表3に示す原料組成で比較ガラス
繊維処理剤a〜fを製造した。得られた各比較ガラス繊
維処理剤を使用し、上記と同様の方法で性能試験を行な
い、表4に示す結果を得た。
Comparative Examples 1 to 6 Comparative glass fiber treating agents a to f having the raw material compositions shown in Table 3 were produced according to the above-mentioned Examples. Using each of the obtained comparative glass fiber treating agents, a performance test was conducted in the same manner as above, and the results shown in Table 4 were obtained.

【0039】[0039]

【表3】 [Table 3]

【0040】[0040]

【表4】 [Table 4]

【0041】[0041]

【発明の効果】本発明は以上の様に構成されており、ガ
ラス繊維および各種の熱可塑性・熱硬化性樹脂との親和
性に優れ且つ硬化速度が速く、しかも硬化後は優れた耐
溶剤性、耐酸性、耐アルカリ性、耐水性、耐熱性、電気
的特性を示す、卓越した性能のガラス繊維処理剤を提供
し得ることになった。しかもアミノ樹脂を複合すること
によって得られるガラス繊維処理剤は、該アミノ樹脂の
エポキシ樹脂に対する硬化剤としての作用によりガラス
繊維処理剤としての性能が一段と高められると共に、焼
付硬化処理時のおける揮発性低分子量物の発生が少なく
なって炉の汚染が抑えられるといった効果も享受でき
る。また、その他の重合性単量体としてカルボキシル基
含有単量体や反応性乳化剤を使用すると、水に対する分
散性および分散安定性の非常に良好なものを得ることが
できる。
EFFECTS OF THE INVENTION The present invention is constituted as described above, has excellent affinity with glass fibers and various thermoplastic / thermosetting resins, has a high curing rate, and has excellent solvent resistance after curing. Therefore, it has become possible to provide a glass fiber treating agent having excellent performance, which exhibits acid resistance, alkali resistance, water resistance, heat resistance, and electrical characteristics. Moreover, the glass fiber treating agent obtained by compounding the amino resin further enhances the performance as the glass fiber treating agent by the action of the amino resin as a curing agent for the epoxy resin, and at the same time, has a volatility at the time of bake hardening treatment. The effect that the generation of low molecular weight substances is reduced and the pollution of the furnace is suppressed can also be enjoyed. Further, when a carboxyl group-containing monomer or a reactive emulsifying agent is used as the other polymerizable monomer, it is possible to obtain one having very good dispersibility in water and dispersion stability.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 エポキシ樹脂に燐酸基含有重合性単量体
をエステル化反応させて得られる反応生成物に、その他
の重合性単量体を共重合させることを特徴とするガラス
繊維処理剤の製造法。
1. A glass fiber treating agent comprising a reaction product obtained by subjecting an epoxy resin to an esterification reaction of a phosphoric acid group-containing polymerizable monomer with another polymerizable monomer. Manufacturing method.
【請求項2】 エポキシ樹脂に燐酸基含有重合性単量体
をエステル化反応させて得られる反応生成物に、その他
の重合性単量体を有機溶剤の存在下で共重合させ、得ら
れた生成物を水性媒体中に分散させる請求項1に記載の
製造法。
2. A reaction product obtained by subjecting an epoxy resin to an esterification reaction of a phosphoric acid group-containing polymerizable monomer, with another polymerizable monomer in the presence of an organic solvent to obtain a copolymer. The method according to claim 1, wherein the product is dispersed in an aqueous medium.
【請求項3】 その他の重合性単量体として反応性乳化
剤を使用する請求項2に記載の製造法。
3. The production method according to claim 2, wherein a reactive emulsifier is used as the other polymerizable monomer.
【請求項4】 その他の重合性単量体としてカルボキシ
ル基含有重合性単量体を使用する請求項2または3に記
載の製造法。
4. The method according to claim 2, wherein a carboxyl group-containing polymerizable monomer is used as the other polymerizable monomer.
【請求項5】 有機溶剤の存在下で共重合させた生成物
に、アミノ樹脂を混合してから水性媒体中に分散させる
請求項4に記載の製造法。
5. The production method according to claim 4, wherein the amino resin is mixed with the product copolymerized in the presence of an organic solvent and then dispersed in an aqueous medium.
JP06168440A 1994-07-20 1994-07-20 Manufacturing method of glass fiber treatment agent Expired - Fee Related JP3139295B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP06168440A JP3139295B2 (en) 1994-07-20 1994-07-20 Manufacturing method of glass fiber treatment agent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP06168440A JP3139295B2 (en) 1994-07-20 1994-07-20 Manufacturing method of glass fiber treatment agent

Publications (2)

Publication Number Publication Date
JPH0826779A true JPH0826779A (en) 1996-01-30
JP3139295B2 JP3139295B2 (en) 2001-02-26

Family

ID=15868162

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Application Number Title Priority Date Filing Date
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Country Link
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