JPH0578411A - Microencapsulated curing agent, its production, unsaturated polyester resin composition containing the same curing agent and method for curing and stabilizing the same - Google Patents

Microencapsulated curing agent, its production, unsaturated polyester resin composition containing the same curing agent and method for curing and stabilizing the same

Info

Publication number
JPH0578411A
JPH0578411A JP26694891A JP26694891A JPH0578411A JP H0578411 A JPH0578411 A JP H0578411A JP 26694891 A JP26694891 A JP 26694891A JP 26694891 A JP26694891 A JP 26694891A JP H0578411 A JPH0578411 A JP H0578411A
Authority
JP
Japan
Prior art keywords
unsaturated polyester
polyester resin
curing agent
curing
temperature
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
JP26694891A
Other languages
Japanese (ja)
Other versions
JP3168627B2 (en
Inventor
Norihisa Ujigawa
典久 氏川
Masumi Takamura
真澄 高村
Kazuo Matsuyama
一夫 松山
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.)
NOF Corp
Original Assignee
Nippon Oil and Fats 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 Oil and Fats Co Ltd filed Critical Nippon Oil and Fats Co Ltd
Priority to JP26694891A priority Critical patent/JP3168627B2/en
Publication of JPH0578411A publication Critical patent/JPH0578411A/en
Application granted granted Critical
Publication of JP3168627B2 publication Critical patent/JP3168627B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Manufacturing Of Micro-Capsules (AREA)
  • Polymerization Catalysts (AREA)
  • Macromonomer-Based Addition Polymer (AREA)

Abstract

PURPOSE:To obtain the subject curing agent, composed of a core substance of an organic peroxide for an unsaturated polyester resin and a film substance, soluble at a curing temperature and having the inside of a polyelectrolyte and the outside of a specific polymer, excellent in storage stability and pot life and providing sharp curing. CONSTITUTION:The objective microencapsulated curing agent is obtained by adding an organic peroxide which is a solid at ordinary temperature and has at least 5 deg.C difference between the melting point and the thermal decomposition temperature for forming a core to an aqueous solution of a substance for forming an inner film containing a polyelectrolyte, producing a liquid mixture at a temperature below the thermal decomposition temperature, then cooling the liquid mixture, forming grains composed of the organic peroxide core and the inner film, subsequently adding a monomer composed of at least one of an acrylic acid ester, a methacrylic acid ester and a vinyl aromatic compound for forming an outer resin film and forming a resin film of the polymerized monomer on the inner film. The above-mentioned curing agent is soluble at the curing temperature of the unsaturated polyester resin and contains the core substance which is the organic peroxide for curing the unsaturated polyester resin in the interior.

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、不飽和ポリエステル樹
脂用硬化剤に関する。詳しくは、取り扱い及び作業性が
良好で、且つ、不飽和ポリエステル樹脂中には安定に存
在し、樹脂硬化の際には、速やかな硬化を可能とする硬
化剤を芯物質として含有するマイクロカプセル化硬化
剤、同硬化剤の製造方法、同硬化剤を含有する不飽和ポ
リエステル樹脂組成物、不飽和ポリエステル樹脂硬化方
法及び貯蔵安定性の高い不飽和ポリエステル樹脂組成物
の製造方法に関する。
TECHNICAL FIELD The present invention relates to a curing agent for unsaturated polyester resins. Specifically, it is easy to handle and work, and is stable in the unsaturated polyester resin. When the resin is cured, a microcapsule containing a curing agent as a core substance that enables rapid curing. The present invention relates to a curing agent, a method for producing the curing agent, an unsaturated polyester resin composition containing the curing agent, a method for curing an unsaturated polyester resin, and a method for producing an unsaturated polyester resin composition having high storage stability.

【0002】[0002]

【従来の技術】従来、不飽和ポリエステル樹脂はガラス
繊維、無機充填剤、増粘剤、安定剤、離型剤等を配合
し、硬化剤を加えて加熱硬化又は必要に応じて硬化促進
剤を配合して常温硬化することによりFRPの成形に広
く使用されている。
2. Description of the Related Art Conventionally, an unsaturated polyester resin is blended with glass fiber, an inorganic filler, a thickener, a stabilizer, a release agent, etc., and a curing agent is added to heat-cure or, if necessary, a curing accelerator. It is widely used for FRP molding by compounding and curing at room temperature.

【0003】不飽和ポリエステル樹脂の硬化剤としては
一般的に有機過酸化物が使用されるが、硬化剤を含む樹
脂液には可使時間(ポットライフ)があり、例えばゲル
化したりするため樹脂液が長期の保存に耐えられない。
このため、現在は樹脂と硬化剤の二者又は硬化促進剤と
の三者を使用直前に混ぜ合せて使用している。一方実用
上は樹脂液のポットライフが長く且つ、不飽和ポリエス
テル樹脂の硬化温度において速やかに硬化する硬化剤が
強く求められている。特に生産性の観点からより低温で
作用する硬化剤が望まれている。然し、硬化温度が低く
なるほど樹脂中での硬化剤の安定性は悪くなる。この相
反する条件を満たす目的で種々の研究が行われてきた。
その結果硬化剤をマイクロカプセル化すれば前記の欠点
を排除しうることが確認され、近年マイクロカプセル化
された硬化剤の開発が盛んに行われている。例えば、特
開昭48−7086号公報には、染料又は顔料によって
着色された液体又は固体状の有機過酸化物をゼラチンや
ポリスチレンのように天然もしくは合成した結晶性又は
無定形の高分子物質で被覆した硬化剤カプセルと不飽和
ポリエステル樹脂から成る、常温では安定であり所定温
度で硬化性能を有する硬化性組成物が開示されている。
しかしながら着色された硬化剤カプセルは透明成形品に
は使用出来ない。又特開昭57−12017号公報には
10時間の半減期を得るための温度が74〜158℃の
液体又は固体状の有機過酸化物及びナフテン酸コバルト
などの硬化促進剤のマイクロカプセルを含有する低温、
低圧で圧縮成形できるシート・モールディング・コンパ
ウンド(SMC)に適する不飽和ポリエステル樹脂が、
更に又、特開昭59−502018号公報には液体又は
固体状硬化剤のマイクロカプセルを含有し、所定のプロ
セス条件によって放出されるまでポリエステル樹脂から
隔離されていることを特徴とする強化ポリエステル樹脂
製品の製法が開示されている。
Organic peroxides are generally used as a curing agent for unsaturated polyester resins, but the resin liquid containing the curing agent has a pot life, and for example, gels because it gels. The liquid cannot withstand long-term storage.
Therefore, at present, two of the resin and the curing agent or the three of the curing accelerator are mixed and used immediately before use. On the other hand, practically, there is a strong demand for a curing agent that has a long pot life of the resin liquid and that is rapidly cured at the curing temperature of the unsaturated polyester resin. In particular, a curing agent that acts at a lower temperature is desired from the viewpoint of productivity. However, the lower the curing temperature, the worse the stability of the curing agent in the resin. Various studies have been conducted for the purpose of satisfying these conflicting conditions.
As a result, it has been confirmed that the above drawbacks can be eliminated by encapsulating the curing agent in microcapsules, and in recent years, development of microencapsulated curing agents has been actively conducted. For example, JP-A-48-7086 discloses a crystalline or amorphous polymer substance obtained by natural or synthetic liquid or solid organic peroxide colored with a dye or pigment, such as gelatin or polystyrene. A curable composition comprising a coated hardener capsule and an unsaturated polyester resin, which is stable at room temperature and has curability at a predetermined temperature, is disclosed.
However, colored hardener capsules cannot be used for transparent moldings. Further, JP-A-57-12017 contains microcapsules of a liquid or solid organic peroxide having a temperature of 74 to 158 ° C. for obtaining a half-life of 10 hours and a curing accelerator such as cobalt naphthenate. Low temperature,
Unsaturated polyester resin suitable for sheet molding compound (SMC) that can be compression molded at low pressure
Furthermore, JP-A-59-502018 discloses a reinforced polyester resin containing microcapsules of a liquid or solid curing agent, which are isolated from the polyester resin until they are released under predetermined process conditions. A method of making the product is disclosed.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、常温で
液体状の有機過酸化物のマイクロカプセル化物において
実際は芯物質が徐々に膜物質を溶解し、それ自身の安定
性及びそれを配合した不飽和ポリエステル樹脂組成物の
安定性が阻害される。又固体状の有機過酸化物をそのま
まマイクロカプセル化した場合、前述の公知の硬化剤の
問題点を解消しておらず、更に芯物質の形状や表面状態
により完全に膜物質で覆うことは困難であるという欠点
を持っている。
However, in a microencapsulated product of an organic peroxide that is liquid at room temperature, the core substance actually gradually dissolves the membrane substance, and the stability of the core substance itself and the unsaturated polyester compounded with it are obtained. The stability of the resin composition is impaired. Further, when solid organic peroxides are directly encapsulated in microcapsules, the problems of the above-mentioned known curing agents are not solved, and it is difficult to completely cover with a film substance due to the shape and surface condition of the core substance. Has the drawback of being

【0005】更に不飽和ポリエステル樹脂の硬化は、一
般的には極く少量の硬化剤を用いることにより達成され
ており、硬化剤をマイクロカプセル化した場合少しでも
マイクロカプセル化されていないものが樹脂中に含まれ
れば硬化が始まり貯蔵安定性著しく阻害されたことにな
る。又、強固な皮膜で硬化剤を被覆した場合には、硬化
時に硬化遅れや不均一硬化の生じる虞れがある。このよ
うに、硬化剤を単にマイクロカプセル化しただけでは、
硬化に際して速やかに硬化し、貯蔵安定性の良い不飽和
ポリエステル樹脂組成物を得ることは容易でない。
Further, the curing of the unsaturated polyester resin is generally achieved by using a very small amount of the curing agent, and when the curing agent is microencapsulated, the resin which is not microencapsulated at all is a resin. If it is contained in the composition, it will start to cure and the storage stability will be significantly impaired. Further, when the hardener is coated with a strong film, there is a possibility that hardening delay or uneven hardening may occur during hardening. In this way, simply encapsulating the curing agent
It is not easy to obtain an unsaturated polyester resin composition which cures rapidly upon curing and has good storage stability.

【0006】又、不飽和ポリエステル樹脂にガラス繊
維、充填剤などを配合して得られるSMCにおいては、
硬化剤をマイクロカプセル化した場合、補強剤の摩擦に
よるマイクロカプセルの破壊が起こり、前記の性能を保
持することは困難である。そしてまた加圧や加熱だけで
は、カプセルの膜を完全に破壊し硬化剤を有効に樹脂中
に分散させることは容易ではない。
Further, in SMC obtained by blending unsaturated polyester resin with glass fiber, filler, etc.,
When the hardener is microencapsulated, the microcapsules are destroyed by friction of the reinforcing agent, and it is difficult to maintain the above performance. Further, it is not easy to completely destroy the capsule film and effectively disperse the curing agent in the resin only by applying pressure or heating.

【0007】[0007]

【課題を解決するための手段】本発明者らは取り扱い及
び作業性が良好で、且つ、不飽和ポリエステル樹脂に混
入した場合樹脂の貯蔵安定性を損なうことなく、しかも
樹脂の硬化に際しては速やかに、しかも均一な硬化を可
能とする有機過酸化物をマイクロカプセル化した不飽和
ポリエステル樹脂用硬化剤を開発する目的で研究した結
果、特定な有機過酸化物を特定な手段を用いて得られる
マイクロカプセル化した硬化剤により目的を達成出来る
ことを確認して本発明を完成した。
Means for Solving the Problems The present inventors have found that the handling and workability are good, the storage stability of the resin is not impaired when the resin is mixed with an unsaturated polyester resin, and the resin is promptly cured upon curing. Moreover, as a result of research for the purpose of developing a curing agent for unsaturated polyester resin in which an organic peroxide that enables uniform curing is encapsulated in a microcapsule, a specific organic peroxide can be obtained by a specific means. The present invention has been completed by confirming that the purpose can be achieved by the encapsulated curing agent.

【0008】即ち本発明は、(イ)常温で固体であり、
融点と熱分解温度との差が少なくとも5℃である不飽和
ポリエステル樹脂硬化用有機過酸化物である芯物質と、
(ロ)不飽和ポリエステル樹脂、前記芯物質との反応性
がなく、常温で固体であり、不飽和ポリエステル樹脂硬
化温度において溶解する性質を有し、内側皮膜が高分子
電解質からなり、外側皮膜がアクリル酸エステル、メタ
クリル酸エステル及びビニル芳香族の一種又は二種以上
からなる芯物質を覆っている膜物質とよりなる不飽和ポ
リエステル樹脂用マイクロカプセル化硬化剤;内側皮膜
形成物質水溶液に、常温で固体であり、融点と熱分解温
度との差が少なくとも5℃である芯形成用有機過酸化物
を加え、該熱分解温度以下の温度で液状混合物を生成さ
せ、次いで液状混合物を冷却して有機過酸化物芯と内側
皮膜とよりなる粒を生成させ、次に外側樹脂膜生成用単
量体の少なくとも1種を添加、該内側皮膜上に単量体重
合樹脂膜を形成させて不飽和ポリエステル樹脂用マイク
ロカプセル化硬化剤を製造する方法;不飽和ポリエステ
ル樹脂と前述のマイクロカプセル化硬化剤とより成る不
飽和ポリエステル樹脂組成物;本発明の硬化剤による不
飽和ポリエステル樹脂の硬化方法及び本発明の硬化剤を
不飽和ポリエステル樹脂に添加することにより成る貯蔵
安定性の高い不飽和ポリエステル樹脂組成物の製造方法
に関する。
That is, the present invention is (a) solid at room temperature,
A core substance which is an unsaturated polyester resin curing organic peroxide having a difference between the melting point and the thermal decomposition temperature of at least 5 ° C .;
(B) Unsaturated polyester resin, which has no reactivity with the core substance, is solid at room temperature, has a property of dissolving at the unsaturated polyester resin curing temperature, the inner coating is made of a polymer electrolyte, and the outer coating is Microencapsulating curing agent for unsaturated polyester resin consisting of a film substance covering a core substance consisting of one or more of acrylic acid ester, methacrylic acid ester and vinyl aromatic; A core-forming organic peroxide, which is a solid and has a difference between the melting point and the thermal decomposition temperature of at least 5 ° C., is added to form a liquid mixture at a temperature equal to or lower than the thermal decomposition temperature, and then the liquid mixture is cooled to cool the organic mixture. Particles composed of a peroxide core and an inner film are formed, and then at least one kind of a monomer for forming an outer resin film is added to form a monomer-polymerized resin film on the inner film. Method for producing microencapsulating curing agent for unsaturated polyester resin; unsaturated polyester resin composition comprising unsaturated polyester resin and the aforementioned microencapsulating curing agent; curing unsaturated polyester resin with curing agent of the present invention The present invention relates to a method and a method for producing an unsaturated polyester resin composition having high storage stability, which comprises adding the curing agent of the present invention to an unsaturated polyester resin.

【0009】本発明に用いる芯物質としては、常温(2
0℃)で固体の有機過酸化物であり、例えばペルオキシ
ジカーボネート類としてはジミリスチルペルオイキシジ
カーボネート、ジデシルペルオキシカーボネート、ジセ
チルペルオキシカーボネート等、ジアルキルペルオキシ
ド類としてはジクミルペルオキシド、α,α′−ビス
(t−ブチルペルオキシ)−m−イソプロピルベンゼ
ン、α,α′−ビス(t−ブチルペルオキシ)−p−イ
ソプロピルベンゼン等、ケトンペルオキシド類として
は、シクロヘキサノンペルオキシド、1,1−ジヒドロ
キシジシクロヘキシルペルオキシド等、ペルオキシエス
テル類としては、2,5−ジメチル2,5−ジ(ベンゾ
イルペルオキシ)ヘキサン、ジ−t−ブチルジペルオキ
シイソフタレート等、ペルオキシケタール類としては、
1,1−ビス(t−ブチルペルオキシ)シクロドデカ
ン、1,3−ジフェニル2,2−ビス(t−ブチルペル
オキシ)プロパン、1−フェニル3,3−ビス(t−ブ
チルペルオキシ)ブタン、1−ベンゾイル2−メチル
2,2−ビス(t−ブチルペルオキシ)エタン、1,1
−ビス(t−ブチルペルオキシ)シクロドデカン等、ジ
アシルペルオキシドとしては、ジデカノイルペルオキシ
ド、ジラウロイルペルオキシド、ビス(o−メチルベン
ゾイル)ペルオキシド、ビス(m−メチルベンゾイル)
ペルオキシド等、ヒドロペルオキシドとしては、2,5
−ジヒドロペルオキシ2,5−ジメチルヘキサンα−,
α′−ビス(ヒドロペルオキシ)−m−イソプロピルベ
ンゼン等を挙げることができるが、前述の条件を満足す
れば、これら二種以上の混合物ないし他の希釈媒体との
混合物としても使用しうる。
The core substance used in the present invention is at room temperature (2
It is an organic peroxide that is solid at 0 ° C., and examples thereof include dimyristyl peroxydicarbonate, didecyl peroxy carbonate, and dicetyl peroxy carbonate as peroxydicarbonates, and dicumyl peroxide, α, Examples of ketone peroxides such as α'-bis (t-butylperoxy) -m-isopropylbenzene and α, α'-bis (t-butylperoxy) -p-isopropylbenzene include cyclohexanone peroxide and 1,1-dihydroxydicyclohexyl. Peroxyesters such as peroxides include 2,5-dimethyl 2,5-di (benzoylperoxy) hexane and di-t-butyldiperoxyisophthalate, and peroxyketals include
1,1-bis (t-butylperoxy) cyclododecane, 1,3-diphenyl 2,2-bis (t-butylperoxy) propane, 1-phenyl 3,3-bis (t-butylperoxy) butane, 1- Benzoyl 2-methyl 2,2-bis (t-butylperoxy) ethane, 1,1
Examples of diacyl peroxides such as -bis (t-butylperoxy) cyclododecane include didecanoyl peroxide, dilauroyl peroxide, bis (o-methylbenzoyl) peroxide, and bis (m-methylbenzoyl).
Hydroperoxides such as peroxide are 2,5
-Dihydroperoxy 2,5-dimethylhexane α-,
Examples thereof include α'-bis (hydroperoxy) -m-isopropylbenzene and the like, and if they satisfy the above-mentioned conditions, they can be used as a mixture of two or more kinds thereof or a mixture with another diluent medium.

【0010】不飽和ポリエステル樹脂の硬化は加熱によ
り開始するが、50〜100℃で硬化する中温硬化と1
00℃以上で硬化する高温硬化に分類される。硬化剤で
ある有機過酸化物は前者においてはペルオキシジカーボ
ネート類、ジアシルペルオキシド類、ケトンペスオキシ
ド類、ペルオキシケタール類、ヒドロオエルオキシド類
或いはペルオキシエステル類が好ましく、単独或いは硬
化促進剤と併用で使用される。又後者にはペルオキシケ
タール類、ペルオキシエステル類或いはジアルキルペル
オキシド類が好ましい。
Curing of the unsaturated polyester resin is initiated by heating, but the intermediate temperature curing of 50 to 100 ° C. and 1
It is classified as high temperature curing that cures at 00 ° C or higher. In the former case, the organic peroxide which is a curing agent is preferably peroxydicarbonates, diacyl peroxides, ketone pesoxides, peroxyketals, hydrooyl oxides or peroxyesters, and used alone or in combination with a curing accelerator. To be done. The latter is preferably peroxyketals, peroxyesters or dialkyl peroxides.

【0011】表1には、代表的な有機過酸化物の融点と
熱分解温度を示した。有機過酸化物の融点については、
他の物質を混入させて下げることは可能であり、本発明
を実施するに支障のない範囲で利用することができる。
しかし、この場合には融点の幅が広くなるため、より一
層速硬化を期待する場合には単独で用いるほうが好まし
い。又熱分解温度は、雑誌“安全工学”記載の加熱試験
法(北川宏ほか:安全工学、第4巻第2号P133〜1
34、136,1965年)に基づいて求めた値であ
り、具体的には一定速度で有機過酸化物の温度を上昇さ
せた時、有機過酸化物の分解が急速に起こり始める温度
を意味する。
Table 1 shows melting points and thermal decomposition temperatures of typical organic peroxides. Regarding the melting point of the organic peroxide,
It is possible to mix and lower other substances and it can be used within a range that does not hinder the practice of the present invention.
However, in this case, the range of the melting point is widened, and therefore it is preferable to use them alone if further rapid curing is expected. The thermal decomposition temperature is the heating test method described in the magazine "Safety Engineering" (Hiro Kitagawa et al .: Safety Engineering, Vol. 4, No. 2, P133-1).
34, 136, 1965), and specifically means the temperature at which decomposition of the organic peroxide begins to occur rapidly when the temperature of the organic peroxide is increased at a constant rate. ..

【表1】 [Table 1]

【0012】次に本発明のマイクロカプセル化硬化剤の
製造法について述べる。即ち、前述の常温で固体であ
り、融点と熱分解温度との差が少なくとも5℃である有
機過酸化物を、水系においてその融点以上、熱分解温度
以下で1〜200μmの微小粒子溶融物を生成させ、そ
の表面を公知のマイクロカプセル化方法であるコアセル
ベーション法により高分子電解質で覆い内側皮膜を形成
する。コアセルベーション法の詳細は(株)総合技術セ
ンター著、“最新マイクロカプセル化技術”に記載され
ている。コアセルベーション法における高分子電解質と
しては、例えば、ゼラチン、カゼイン、アラビアゴム、
アルギン酸ソーダ、カルボキシメチルセルロース、ポリ
ビニルアルコール、メチルビニルエーテル、無水マレイ
ン酸共重合体等が使用でき、ホルムアルデヒド、グルタ
ルアルデヒド等によって硬化することができる。次いで
外側皮膜形成用単量体と重合開始剤を添加して有機過酸
化物の融点以下で重合し、前記の高分子電解質で覆われ
た有機過酸化物を更に前記単量体の重合体の外側皮膜で
覆うことにより粒径1〜200μmの本発明の不飽和ポ
リエステル樹脂用マイクロカプセル化硬化剤が得られ
る。
Next, a method for producing the microencapsulated curing agent of the present invention will be described. That is, the above-mentioned organic peroxide which is solid at room temperature and has a difference between the melting point and the thermal decomposition temperature of at least 5 ° C. is used to form a fine particle melt of 1 to 200 μm above the melting point and below the thermal decomposition temperature in an aqueous system. It is generated, and its surface is covered with a polymer electrolyte by a coacervation method which is a known microencapsulation method to form an inner film. Details of the coacervation method are described in "Latest Microencapsulation Technology" by Sogo Gijutsu Center. As the polyelectrolyte in the coacervation method, for example, gelatin, casein, gum arabic,
Sodium alginate, carboxymethyl cellulose, polyvinyl alcohol, methyl vinyl ether, maleic anhydride copolymer and the like can be used, and can be cured with formaldehyde, glutaraldehyde and the like. Then, an outer film-forming monomer and a polymerization initiator are added and polymerized at a temperature equal to or lower than the melting point of the organic peroxide, and the organic peroxide covered with the polyelectrolyte is further converted into a polymer of the monomer. By covering with an outer coating, the microencapsulating curing agent for unsaturated polyester resin of the present invention having a particle size of 1 to 200 μm can be obtained.

【0013】本発明における外側皮膜を形成する重合体
の製造に用いられる単量体としては具体的には以下のよ
うなものである。アクリル酸メチル及び、又はメタクリ
ル酸メチル[以下(メタ)アクリル酸メチルと総称す
る。以下同様]、(メタ)アクリル酸エチル、(メタ)
アクリル酸n−プロピル等の低級アルキル(メタ)アク
リル酸エステル、(メタ)アクリル酸−n−ブチル、
(メタ)アクリル酸−n−ヘキシル、(メタ)アクリル
酸−2−エチルヘキシル、(メタ)アクリル酸ラウリル
等の高級アルキル(メタ)アクリル酸エステル、ジ(メ
タ)アクリル酸ジエチレングリコール、ジ(メタ)アク
リル酸トリエチレングリコール、ジ(メタ)アクリル酸
デカエチレングリコール、ジ(メタ)アクリル酸1,3
−ブチレン、トリ(メタ)アクリル酸トリメチロールプ
ロパン、テトラ(メタ)アクリル酸ペンタエリストリー
ル、ジ(メタ)アクリル酸フタル酸ジエチレングリコー
ル等の多官能性(メタ)アクリル酸エステル、スチレ
ン、α−メチルスチレン、ビニルトルエン、ジビニルベ
ンゼン等のビニル芳香族が挙げられる。これらの単量体
は、1種又は2種以上が適宜選択して使用されるが、外
側皮膜の緻密さを上げるためには他官能性単量体を使用
することが好ましい。
Specific examples of the monomer used for the production of the polymer forming the outer film in the present invention are as follows. Methyl acrylate and / or methyl methacrylate [hereinafter collectively referred to as (meth) acrylate). The same applies hereinafter], ethyl (meth) acrylate, (meth)
Lower alkyl (meth) acrylates such as n-propyl acrylate, (meth) acrylate-n-butyl,
Higher alkyl (meth) acrylic acid esters such as (meth) acrylic acid-n-hexyl, (meth) acrylic acid-2-ethylhexyl, and lauryl (meth) acrylate, diethylene glycol di (meth) acrylate, di (meth) acrylic Acid triethylene glycol, di (meth) acrylic acid decaethylene glycol, di (meth) acrylic acid 1,3
-Multifunctional (meth) acrylic acid esters such as butylene, trimethylolpropane tri (meth) acrylate, pentaerythryl tetra (meth) acrylate, diethylene glycol di (meth) acrylate, styrene, α-methyl Examples include vinyl aromatics such as styrene, vinyltoluene, and divinylbenzene. One or two or more of these monomers are appropriately selected and used, but it is preferable to use another functional monomer in order to increase the denseness of the outer coating.

【0014】前記外側皮膜は前記単量体を有機過酸化
物、水溶性無機過酸化物を使用し、熱又は還元剤を併用
したレドックス系により重合することにより形成され
る。
The outer film is formed by polymerizing the above-mentioned monomer using an organic peroxide or a water-soluble inorganic peroxide by a redox system in which heat or a reducing agent is used in combination.

【0015】本発明において用いられる不飽和ポリエス
テル樹脂は、(a)不飽和二塩基酸として無水マレイン
酸、マレイン酸、フマル酸、メサコン酸、テトラコン
酸、イタコン酸、塩素化マレイン酸、飽和二塩基酸とし
て無水フタル酸、イソフタル酸、テレフタル酸、テトラ
ヒドロフタル酸、ハロゲン化無水フタル酸、アジピン
酸、コハク酸、セバシン酸と多価アルコールとしてエチ
レングリコール、ジエチレングリコール、プロピレング
リコール、ジプロピレングリコール、ブチレングリコー
ル、ネオペンチルグリコール、ヘキシレングリコール、
水素化ビスフェノールA、2,2−ジ(4−ヒドロキシ
エトキシフェニル)プロパン、2,2−ジ(4−ヒドロ
キシエトキシフェニル)プロパン,エチレンオキシド、
プロピレンオキシド等を特定の割合で、窒素気流下17
0〜200℃で脱水縮合させて得られるアルキッド樹脂
と、(b)スチレン、o−クロルスチレン、ビニルトル
エン、メタクリル酸メチル、ジアリルフタレート、トリ
アリルイソシアネート等の架橋性モノマーの混合物であ
る。
The unsaturated polyester resin used in the present invention is (a) an unsaturated dibasic acid such as maleic anhydride, maleic acid, fumaric acid, mesaconic acid, tetraconic acid, itaconic acid, chlorinated maleic acid and saturated dibasic acid. Phthalic acid as acid, isophthalic acid, terephthalic acid, tetrahydrophthalic acid, halogenated phthalic anhydride, adipic acid, succinic acid, sebacic acid and polyhydric alcohol ethylene glycol, diethylene glycol, propylene glycol, dipropylene glycol, butylene glycol, Neopentyl glycol, hexylene glycol,
Hydrogenated bisphenol A, 2,2-di (4-hydroxyethoxyphenyl) propane, 2,2-di (4-hydroxyethoxyphenyl) propane, ethylene oxide,
Propylene oxide, etc. at a specific ratio under a nitrogen stream 17
It is a mixture of an alkyd resin obtained by dehydration condensation at 0 to 200 ° C. and (b) a crosslinkable monomer such as styrene, o-chlorostyrene, vinyltoluene, methyl methacrylate, diallyl phthalate and triallyl isocyanate.

【0016】本発明において用いられるマイクロカプセ
ル化して得た硬化剤は単独で、又はレドックス系を形成
する硬化促進剤と併用して用いることができるが、その
硬化促進剤としては例えば、ナフテン酸コバルトのよう
な高級脂肪酸の金属塩、ベンゾイルチオ尿素、エチレン
チオ尿素等のチオ尿素類、エチレンジアミン、L−アス
コルビン酸、p−トルエンスルフィン酸ソーダ等が挙げ
られる。硬化剤との組合わせにより促進硬化が異なるた
め適宜選択する必要がある。
The curing agent obtained by microencapsulation used in the present invention can be used alone or in combination with a curing accelerator which forms a redox system. Examples of the curing accelerator include cobalt naphthenate. Examples thereof include metal salts of higher fatty acids, thioureas such as benzoylthiourea and ethylenethiourea, ethylenediamine, L-ascorbic acid and sodium p-toluenesulfinate. Since accelerated curing differs depending on the combination with a curing agent, it is necessary to select it appropriately.

【0017】本発明のマイクロカプセル化した硬化剤及
びレドックス系を形成する硬化促進剤から成る不飽和ポ
リエステル樹脂用硬化剤において、マイクロカプセル化
した硬化剤中の有機過酸化物純分と硬化促進剤の割合
は、所望の硬化速度に応じて90/10〜10/90
(重量比)の割合の中で選択できる。
In the curing agent for unsaturated polyester resin comprising the microencapsulated curing agent and the curing accelerator forming the redox system of the present invention, the organic peroxide content and the curing accelerator in the microencapsulated curing agent are Of 90/10 to 10/90 depending on the desired cure rate.
It can be selected in the ratio of (weight ratio).

【0018】本発明の不飽和ポリエステル樹脂組成物に
おいて、不飽和ポリエステル樹脂用硬化剤中の有機過酸
化物の純分は樹脂100重量部に対して0.1〜5重量
部であり、好ましくは0.5〜3重量部である。0.1
重量部未満では硬化剤としての作用が不充分であり、又
5重量部を越えて使用しても硬化剤の作用が5重量部の
場合と同等であり経済的に好ましくない。
In the unsaturated polyester resin composition of the present invention, the pure content of the organic peroxide in the curing agent for unsaturated polyester resin is 0.1 to 5 parts by weight, preferably 100 parts by weight of the resin. 0.5 to 3 parts by weight. 0.1
If it is less than 5 parts by weight, the action as a curing agent is insufficient, and if it is used in excess of 5 parts by weight, the action of the curing agent is equivalent to that of 5 parts by weight, which is not economically preferable.

【0019】本発明における不飽和ポリエステル樹脂組
成物においては、成形品の強度向上の目的でロービング
クロス、チョップドストランド、チョップドストランド
マット等のガラス繊維、或いは炭素繊維のような補強剤
や炭酸カルシウム、クレー、水酸化アルミニウムのよう
な充填剤を配合することができ、その配合量は総量の1
0〜90重量%であり、少なすぎたり多すぎる場合には
成形品の強度が著しく低下するため好ましくない。更に
目的に応じて酸化マグネシウム等のアルカリ土類金属の
酸化物或いは水酸化物等の増粘剤や、熱可塑性樹脂、そ
の共重合体、或いはブロック・グラフト共重合体等の低
収縮剤、ステアリン酸亜鉛のような離型剤或いはベンゾ
キノン等の重合禁止剤を使用することができる。
In the unsaturated polyester resin composition of the present invention, glass fibers such as roving cloth, chopped strands and chopped strand mats, or reinforcing agents such as carbon fibers, calcium carbonate and clay are used for the purpose of improving the strength of molded articles. , A filler such as aluminum hydroxide can be blended, and the blending amount is 1 of the total amount.
It is 0 to 90% by weight, and if the amount is too small or too large, the strength of the molded product is remarkably reduced, which is not preferable. Further, depending on the purpose, thickeners such as oxides or hydroxides of alkaline earth metals such as magnesium oxide, low shrinkage agents such as thermoplastic resins, copolymers thereof, block / graft copolymers, stearin, etc. A release agent such as zinc acid or a polymerization inhibitor such as benzoquinone can be used.

【0020】本発明における不飽和ポリエステル樹脂の
硬化温度は各成形方法により適宜選択でき、成形温度と
して表される。例えばレジンコンクリートの成形、波板
や平板の連続成形、フィラメントワインディング成形或
いはレジンインジェクション成形は50〜100℃で成
形され、ペルオキシジカーボネート類、ジアシルペルオ
キシド類、ケトンペルオキシド類、ペルオキシケタール
類、ヒドロペルオキシド類或いはペルオキシエステル類
の有機過酸化物をマイクロカプセル化した硬化剤が単独
又はレドックス系を形成する硬化促進剤と併用して用い
られる。又SMC、バルク・モールディング・コンパウ
ンド(BMC)或いはマッチドダイ成形は100℃以上
で行われ、ペルオキシケタール類、ペルオキシエステル
類或いはジアルキルペルオキシド類をマイクロカプセル
化した硬化剤が用いられる。
The curing temperature of the unsaturated polyester resin in the present invention can be appropriately selected according to each molding method and is expressed as a molding temperature. For example, molding of resin concrete, continuous molding of corrugated sheet or flat plate, filament winding molding or resin injection molding is performed at 50 to 100 ° C., and peroxydicarbonates, diacyl peroxides, ketone peroxides, peroxyketals, hydroperoxides are formed. Alternatively, a curing agent obtained by microencapsulating an organic peroxide of peroxyesters is used alone or in combination with a curing accelerator that forms a redox system. Further, SMC, bulk molding compound (BMC) or matched die molding is performed at 100 ° C. or higher, and a curing agent in which peroxyketals, peroxyesters or dialkyl peroxides are microencapsulated is used.

【0021】[0021]

【発明の効果】本発明のマイクロカプセル化した硬化剤
は、上述のように、特定の有機過酸化物に特定な手段を
用いて得られているため、幾つかの優れた特徴を有して
いる。
As described above, the microencapsulated curing agent of the present invention has several excellent characteristics because it is obtained by using a specific means for a specific organic peroxide. There is.

【0022】先ず、本発明のマイクロカプセル化した硬
化剤は芯物質が固体の有機過酸化物で、その周りをゼラ
チン等の高分子電解質を内側皮膜とし、アクリル酸エス
テル、メタクリル酸エステル及びビニル芳香族の一種又
はそれらの混合物の重合体を外側皮膜とする膜物質が不
溶性不浸透性の薄い隔壁を形成しているため、マイクロ
カプセル自身の貯蔵安定性に優れ、更にマイクロカプセ
ル化した硬化剤と硬化促進剤から成る硬化剤はマイクロ
カプセル化されていない同じ有機過酸化物と硬化促進剤
から成る硬化剤に比べはるかに貯蔵安定性に優れてい
る。又、本発明のマイクロカプセル化した硬化剤は外層
を親油性の樹脂膜で覆っているため球状の外観を有し、
同じ有機過酸化物をゼラチン等の高分子電解質のみで覆
ったマイクロカプセル化硬化剤に比べ、製造時の濾過及
び乾燥時間が短いため、取り扱い及び作業性が良好であ
り、不飽和ポリエステル樹脂への分散性が良好である。
又、マイクロカプセル化した硬化剤又はマイクロカプセ
ル化硬化剤と硬化促進剤から成る硬化剤を不飽和ポリエ
ステル樹脂に混合して得られる本発明の不飽和ポリエス
テル樹脂組成物は、マイクロカプセルの膜物質である高
分子電解質と前記単量体の重合体が不飽和ポリエステル
樹脂中の架橋性モノマーの浸透を防ぐため、マイクロカ
プセル化されていない同じ有機過酸化物又はそれと硬化
促進剤から成る硬化剤を混合して得られる樹脂組成物、
及び同じ有機過酸化物をゼラチン等の高分子電解質のみ
で覆った硬化剤又はそれと硬化促進剤とから成る硬化剤
を混合して成る樹脂組成物に比べ安定化され、はるかに
長いポットライフ又はフェルフライフを有する。
First, in the microencapsulated curing agent of the present invention, a core substance is a solid organic peroxide, and a polymer electrolyte such as gelatin is formed as an inner film around the core substance, and an acrylic acid ester, a methacrylic acid ester and a vinyl aroma are used. Since the membrane material having a polymer of one kind or a mixture thereof as an outer coating forms a thin partition wall that is insoluble and impermeable, the microcapsules themselves have excellent storage stability, and a microencapsulated curing agent. Curing agents consisting of curing accelerators are much more storage stable than curing agents consisting of the same non-microencapsulated organic peroxide and curing accelerator. Further, the microencapsulated curing agent of the present invention has a spherical appearance because the outer layer is covered with a lipophilic resin film,
Compared to a microencapsulating curing agent in which the same organic peroxide is covered only with a polyelectrolyte such as gelatin, the filtration and drying times during production are shorter, so handling and workability are better, and unsaturated polyester resin Good dispersibility.
Further, the unsaturated polyester resin composition of the present invention obtained by mixing a microencapsulated curing agent or a curing agent composed of a microencapsulated curing agent and a curing accelerator with an unsaturated polyester resin is a microcapsule film material. In order to prevent the penetration of the crosslinkable monomer in the unsaturated polyester resin by the polymer of a certain polyelectrolyte and the above-mentioned monomer, the same non-microencapsulated organic peroxide or a curing agent consisting of it and a curing accelerator is mixed. A resin composition obtained by
And a resin composition prepared by coating the same organic peroxide only with a polyelectrolyte such as gelatin, or a resin composition obtained by mixing a curing agent containing the same and a curing accelerator, and having a much longer pot life or a felt. Have a life.

【0023】又固体の有機過酸化物が融点において固体
から液体へと状態が物理変化すると急激な体積増加を引
き起こす。即ち本発明のマイクロカプセル化した硬化剤
は、不飽和ポリエステル樹脂の硬化の際、加熱により芯
物質である有機過酸化物が液体化し、体積を増加するこ
とによって膜物質を破壊して速やかな不飽和ポリエステ
ル樹脂の硬化を可能とするものである。更に、加圧、機
械的な摩擦などによっても、この破壊は促進される。
When the solid organic peroxide undergoes a physical change from the solid state to the liquid state at the melting point, it causes a rapid volume increase. That is, when the unsaturated polyester resin is cured, the microencapsulated curing agent of the present invention liquefies the organic peroxide which is the core substance by heating, and increases the volume to destroy the membrane substance and rapidly destroy the film. It enables curing of the saturated polyester resin. Further, the destruction is promoted by pressure, mechanical friction and the like.

【0024】このように本発明のマイクロカプセル化し
た硬化剤及びそれを含む不飽和ポリエステル樹脂組成物
は取り扱い及び作業性に優れ、且つ、貯蔵安定性に優
れ、長ポットライフ・シェルライフを有し、硬化に際し
ては立ち上がりのシャープな硬化反応を可能にするもの
である。
Thus, the microencapsulated curing agent of the present invention and the unsaturated polyester resin composition containing the same have excellent handling and workability, excellent storage stability, and a long pot life / shell life. When curing, it enables a sharp curing reaction at the start.

【0025】[0025]

【実施例】次に本発明を実施例、比較例により更に詳細
に説明する。例中、部は重量部を表す。 [本発明の不飽和ポリエステル樹脂用のマイクロカプセ
ル化硬化剤の製造] 実施例 1 撹拌棒、温度計及び還流冷却器を備えた4ツ口フラスコ
にゼラチン8g、アラビアゴム8g及び水500gを添
加して混合し、撹拌しながら系内の温度を45℃にし、
この水溶液にジミリスチリルペルオキシジカーボネート
50gを添加した。次いで系内の温度を50℃にしてジ
ミリスチリルペルオキシジカーボネートを溶融させ、約
5分撹拌後、50%酢酸水溶液を添加してpHを4.4
に調節した。この後約20分かけて溶液の温度を10℃
まで低下させた。そして37%ホルムアルデヒド水溶液
を6ml添加し4分撹拌した後、10%水酸化ナトリウ
ム水溶液を用いてpHを9.0とし2時間撹拌した。次
に水250gを加えて35℃に昇温し、1%ポリビニル
アルコール水溶液を加えた後、メタクリル酸メチル(M
MA)とトリアクリル酸トリメチロールプロパン(TM
PT)の混合物(MMA/TMPT=2/8、重量否)
250g及びジイソブチリルペルオキシド(商品名パー
ロイルIB、日本油脂製)を前記MMAとTMPTの混
合物に対して2重量%添加し、35℃で4時間加熱して
MMAとTMPTとを重合させ外側重合体膜を形成させ
た。ポリプロピレン製ろ布(商品名P254、敷島カン
バス(株)製)で15分で濾過後、n−ヘキサンとエタ
ノールの混合溶液(混合比50/50、体積比)でカプ
セル化されていないジミリスチルペルオキシジカーボネ
ートを洗浄した。その後乾燥させてジミリスチルペルオ
キシジカーボネート純分を15.8%含有する内側のゼ
ラチン膜と外側の重合体膜でマイクロカプセル化した平
均粒径50μの硬化剤273gを得た。電子顕微鏡(J
EOL JSM−T300,日本電子製)の観察により
夫々の粒子が均一な球状であることがわかった。
EXAMPLES The present invention will be described in more detail with reference to Examples and Comparative Examples. In the examples, parts represent parts by weight. [Production of Microencapsulated Curing Agent for Unsaturated Polyester Resin of the Present Invention] Example 1 8 g of gelatin, 8 g of gum arabic and 500 g of water were added to a 4-necked flask equipped with a stir bar, thermometer and reflux condenser. And mix, and while stirring, bring the temperature in the system to 45 ° C.,
50 g of dimyristyl peroxydicarbonate was added to this aqueous solution. Next, the temperature in the system is adjusted to 50 ° C. to melt the dimyristyl peroxydicarbonate, and after stirring for about 5 minutes, a 50% acetic acid aqueous solution is added to adjust the pH to 4.4.
Adjusted to. After this, the temperature of the solution is kept at 10 ° C for about 20 minutes.
Lowered. Then, 6 ml of 37% aqueous formaldehyde solution was added and stirred for 4 minutes, and then the pH was adjusted to 9.0 with 10% aqueous sodium hydroxide solution and stirred for 2 hours. Next, 250 g of water was added, the temperature was raised to 35 ° C., 1% aqueous solution of polyvinyl alcohol was added, and then methyl methacrylate (M
MA) and trimethylolpropane triacrylate (TM)
PT) mixture (MMA / TMPT = 2/8, no weight)
250 g and diisobutyryl peroxide (trade name Perloyl IB, manufactured by NOF CORPORATION) were added to the mixture of MMA and TMPT in an amount of 2% by weight, and the mixture was heated at 35 ° C. for 4 hours to polymerize MMA and TMPT to form an outer polymer. A film was formed. Dimyristyl peroxy which is not encapsulated with a mixed solution of n-hexane and ethanol (mixing ratio 50/50, volume ratio) after being filtered through a polypropylene filter cloth (trade name P254, Shikishima Canvas Co., Ltd.) for 15 minutes. The dicarbonate was washed. Then, it was dried to obtain 273 g of a curing agent having an average particle size of 50 μ which was microencapsulated with an inner gelatin film and an outer polymer film containing 15.8% of pure dimyristyl peroxydicarbonate. Electron microscope (J
It was found by observation with EOL JSM-T300, manufactured by JEOL Ltd. that each particle had a uniform spherical shape.

【0026】実施例 2 実施例1において、MMAとTMPTの比を5/5(重
量比)に変えた以外は実施例1に準じて、ジミリスチル
ペルオキシジカーボネート純分を15.9%含有する平
均粒径55μの硬化剤274gを得た。 実施例 3 実施例1において、MMAとTMPTの比を8/5(重
量比)に変えた以外は実施例1に準じて、ジミリスチル
ペルオキシジカーボネート純分を15.1%含有する平
均粒径60μの硬化剤250gを得た。 実施例 4 実施例1において、MMAとTMPTの混合物量を10
0gに変えた以外は実施例1に準じて、ジミリスチルペ
ルオキシジカーボネート純分を26.8%含有する平均
粒径70μの硬化剤132gを得た。
Example 2 In accordance with Example 1 except that the ratio of MMA to TMPT was changed to 5/5 (weight ratio) in Example 1, 15.9% pure dimyristyl peroxydicarbonate was contained. 274 g of a curing agent having an average particle diameter of 55 μm was obtained. Example 3 An average particle size containing 15.1% of pure dimyristyl peroxydicarbonate according to Example 1 except that the ratio of MMA to TMPT was changed to 8/5 (weight ratio). 250 g of 60 μ hardener was obtained. Example 4 In Example 1, the amount of the mixture of MMA and TMPT was adjusted to 10
In the same manner as in Example 1 except that the amount was changed to 0 g, 132 g of a curing agent containing 26.8% of pure dimyristyl peroxydicarbonate and having an average particle diameter of 70 μm was obtained.

【0027】実施例 5 実施例1において、MMAとTMPTの混合物量を35
gに変えた以外は実施例1に準じて、ジミリスチルペル
オキシジカーボネート純分を66.6%含有する平均粒
径75μの硬化剤40gを得た。 実施例 6 実施例1において有機過酸化物としてシクロヘキサノン
ペルオキシドを用い75℃で溶融させ、更に外側皮膜形
成単量体としてスチレンとジビニルベンゼンの混合物
(5/5、重量比)250gを使用しt−ブチルペルオ
キシ2−エチルヘキサノエート(商品名パーブチルO、
日本油脂製)を単量体混合物に対して1重量%添加して
5時間75℃で加熱して前記単量体を重合させた以外は
実施例1に準じて、シクロヘキサノンペルオキシド純分
を15.5%含有する平均粒径55μの硬化剤270g
を得た。
Example 5 In Example 1, the amount of the mixture of MMA and TMPT was changed to 35.
According to the same manner as in Example 1 except that the amount was changed to 40 g, 40 g of a curing agent containing 66.6% of pure dimyristyl peroxydicarbonate and having an average particle size of 75 μ was obtained. Example 6 In Example 1, cyclohexanone peroxide was used as the organic peroxide, melted at 75 ° C., and 250 g of a mixture of styrene and divinylbenzene (5/5, weight ratio) was used as the outer film forming monomer. Butyl peroxy 2-ethylhexanoate (trade name perbutyl O,
(Nippon Yushi Co., Ltd.) was added to the monomer mixture in an amount of 1% by weight, and the mixture was heated at 75 ° C. for 5 hours to polymerize the monomer. 270 g of curing agent containing 5% and having an average particle diameter of 55 μ
Got

【0028】[本発明の不飽和ポリエステル樹脂組成物
の製造] 実施例 7 オルソ系中反応性不飽和ポリエステル樹脂100部に実
施例1で得られたジミリスチルペルオキシジカーボネー
トをマイクロカプセル化した硬化剤を純分として2.5
部となるように混合して不飽和ポリエステル樹脂組成物
を得た。次いでこの組成物を#450のガラスマット2
枚に積層してポリエステルフィルムで包み、10℃のイ
ンキュベーター中でゲル化が起こるまでの時間を測定し
その時間をポットライフとした。結果を表2に示す。 実施例 8 実施例で得られた硬化剤を使用した以外は実施例7に準
じてポットライフを測定した。結果を表2に示す。 実施例 9 実施例3で得られた硬化剤を使用した以外は実施例7に
準じてポットライフを測定した。結果を表2に示す。
[Production of Unsaturated Polyester Resin Composition of the Present Invention] Example 7 A curing agent in which 100 parts of a reactive unsaturated polyester resin in an ortho type is microencapsulated with dimyristyl peroxydicarbonate obtained in Example 1. 2.5 as pure content
To obtain an unsaturated polyester resin composition. This composition is then applied to # 450 Glass Mat 2
It was laminated on one sheet and wrapped with a polyester film, and the time until gelation occurred in an incubator at 10 ° C. was measured, and the time was defined as the pot life. The results are shown in Table 2. Example 8 The pot life was measured according to Example 7 except that the curing agent obtained in Example was used. The results are shown in Table 2. Example 9 The pot life was measured according to Example 7 except that the curing agent obtained in Example 3 was used. The results are shown in Table 2.

【0029】実施例10 実施例4で得られた硬化剤を使用した以外は実施例7に
準じてポットライフを測定した。結果を表2に示す。 実施例 11 実施例5で得られた硬化剤を使用した以外は実施例7に
準じてポットライフを測定した。結果を表2に示す。 実施例 12 実施例6で得られたシクロヘキサノンペルオキシドをマ
イクロカプセル化した硬化剤100部とナフテン酸コバ
ルト20部とを混合して硬化剤を得た。次いでオルソ系
中反応性不飽和ポリエステル樹脂100部に上記の硬化
剤16部を配合して不飽和ポリエステル樹脂組成物と
し、実施例7と同様にしてポットライフを測定した。結
果を表2に示す。
Example 10 The pot life was measured according to Example 7 except that the curing agent obtained in Example 4 was used. The results are shown in Table 2. Example 11 The pot life was measured according to Example 7 except that the curing agent obtained in Example 5 was used. The results are shown in Table 2. Example 12 A curing agent was obtained by mixing 100 parts of the cyclohexanone peroxide microencapsulating curing agent obtained in Example 6 with 20 parts of cobalt naphthenate. Next, 100 parts of the ortho-based reactive unsaturated polyester resin was mixed with 16 parts of the above-mentioned curing agent to give an unsaturated polyester resin composition, and the pot life was measured in the same manner as in Example 7. The results are shown in Table 2.

【0030】[本発明の不飽和ポリエステル樹脂組成物
の硬化方法] 実施例 13 オルソ系中反応性不飽和ポリエステル樹脂100部に実
施例5で得られたマイクロカプセル化した硬化剤を純分
で1部となるように混合して不飽和ポリエステル樹脂組
成物を得た。次いでこの組成物を#450のガラスマッ
ト3枚に積層し、熱電対を差し込んで60℃の対流式恒
温槽で硬化させ、ゲルタイム(GT)、硬化時間(C
T)、硬度を測定した。結果を表3に示す。
[Curing Method for Unsaturated Polyester Resin Composition of the Present Invention] Example 13 100 parts of ortho-based reactive unsaturated polyester resin was mixed with 1 part of the microencapsulated curing agent obtained in Example 5 in a pure content. To obtain an unsaturated polyester resin composition. Then, this composition was laminated on three pieces of # 450 glass mat, and a thermocouple was inserted and cured in a convection constant temperature bath at 60 ° C. to obtain gel time (GT) and curing time (C
T) and hardness were measured. The results are shown in Table 3.

【0031】比較例 1 硬化剤としてマイクロカプセル化していないジミリスチ
ルペルオキシジカーボネートを2.5部使用した以外は
実施例7に準じてポットライフを測定した。結果を表2
に示す。 比較例 2 硬化剤としてマイクロカプセル化していないシクロヘキ
サノンペルオキシドを2.1部使用した以外は実施例1
3に準じてポットライフを測定した。結果を表2に示
す。 比較例 3 有機過酸化物としてメチルエチルケトンペルオキシド
(商品名パーメックN、日本油脂製)を用いエタノール
で洗浄した以外は実施例1に準じてメチルエチルケトン
ペルオキシド純分を15.5%含有するマイクロカプセ
ル80gを得た。芯物質が液体の有機過酸化物であるた
め洗浄工程においてマイクロカプセルの膜が破壊され易
く、収率はかなり悪化した。次いで硬化剤としてマイク
ロカプセル化したメチルエチルケトンペルオキシドを使
用した以外は実施例12に準じてポットライフを測定し
た。結果を表2に示す。
Comparative Example 1 The pot life was measured according to Example 7 except that 2.5 parts of non-microencapsulated dimyristyl peroxydicarbonate was used as a curing agent. The results are shown in Table 2.
Shown in. Comparative Example 2 Example 1 except that 2.1 parts of non-microencapsulated cyclohexanone peroxide was used as the curing agent.
The pot life was measured according to 3. The results are shown in Table 2. Comparative Example 3 80 g of microcapsules containing 15.5% of pure methyl ethyl ketone peroxide were obtained according to Example 1 except that methyl ethyl ketone peroxide (trade name Permec N, manufactured by NOF CORPORATION) was used as the organic peroxide and washed with ethanol. It was Since the core substance is a liquid organic peroxide, the microcapsule film is easily broken in the washing process, and the yield is considerably deteriorated. Then, the pot life was measured according to Example 12 except that microencapsulated methyl ethyl ketone peroxide was used as a curing agent. The results are shown in Table 2.

【0032】比較例 4 5.06%ゼラチン水溶液316gと5.06%のアラ
ビアゴム水溶液316gを混合し、撹拌しながら系内の
温度を45℃にし、この水溶液にジミリスチルペルオキ
シカーボネート100gを添加した。更に60℃の蒸留
水400gを添加して系内の温度を50℃にしてジミリ
スチルペルオキシカーボネートを溶融させた。溶融させ
5分撹拌後、50%酢酸水溶液を添加してpHを4.4
に調節した。この後約20分かけて溶液の温度を20℃
まで低下させた。そして37%ホルムアルデヒド水溶液
6mlを添加し4分撹拌した後、10%水酸化ナトリウ
ム水溶液を用いてpHを9.0まで上げ15分撹拌し
た。以上の処理により平均粒径30μmのジミリスチル
ペルオキシカーボネート分散液を得た。33℃の温水1
000mlにて2回洗浄し、ポリプロピレン製ろ布(P
254)で3時間かけて濾過した。次いでn−ヘキサン
とエタノール(重合比50:50、体積比)の混合溶液
でカプセル化させていないジミリスチルペルオキシカー
ボネートを洗浄した。その後乾燥させて、ジミリスチル
ペルオキシカーボネート純分を85重量%含有するゼラ
チン膜でマイクロカプセル化した平均粒径35μmの硬
化剤70gを得た。電子顕微鏡の観察から、粒子が葡萄
の房状に固まっていることが分かった。得られた硬化剤
を3部使用した以外は実施例7に準じてポットライフを
測定した。結果を表2に示す。
Comparative Example 4 316 g of 5.06% gelatin aqueous solution and 316 g of 5.06% arabic gum aqueous solution were mixed, the temperature of the system was raised to 45 ° C. with stirring, and 100 g of dimyristyl peroxycarbonate was added to this aqueous solution. .. Further, 400 g of distilled water at 60 ° C. was added to bring the temperature in the system to 50 ° C. to melt the dimyristyl peroxycarbonate. After melting and stirring for 5 minutes, add 50% acetic acid aqueous solution to adjust pH to 4.4.
Adjusted to. After this, the temperature of the solution is kept at 20 ° C for about 20 minutes.
Lowered. Then, 6 ml of 37% aqueous formaldehyde solution was added and stirred for 4 minutes, and then the pH was raised to 9.0 using 10% aqueous sodium hydroxide solution and stirred for 15 minutes. A dimyristyl peroxycarbonate dispersion having an average particle diameter of 30 μm was obtained by the above treatment. 33 ° C warm water 1
Washed twice with 000ml, polypropylene filter cloth (P
254) for 3 hours. Then, the non-encapsulated dimyristyl peroxycarbonate was washed with a mixed solution of n-hexane and ethanol (polymerization ratio 50:50, volume ratio). Then, it was dried to obtain 70 g of a curing agent having an average particle diameter of 35 μm which was microencapsulated with a gelatin film containing 85% by weight of pure dimyristyl peroxycarbonate. Observation with an electron microscope revealed that the particles were clustered in a tuft of grapes. The pot life was measured according to Example 7 except that 3 parts of the obtained curing agent was used. The results are shown in Table 2.

【0033】比較例 5 硬化剤としてマイクロカプセル化していないジミリスチ
ルペルオキシジカーボネートを1部使用する以外は実施
例5に準じてGT、CT、硬度を測定した。結果を表3
に示す。
Comparative Example 5 GT, CT and hardness were measured according to Example 5 except that 1 part of non-microencapsulated dimyristyl peroxydicarbonate was used as a curing agent. The results are shown in Table 3.
Shown in.

【表2】 [Table 2]

【表3】 [Table 3]

【0034】表2より本発明のマイクロカプセル化した
硬化剤単独又はレドックス系を形成する硬化促進剤を併
用した硬化剤を含む不飽和ポリエステル樹脂は比較例よ
りはるかに長いポットライフを有しており、安定化され
ていることが確認された。更に表3において硬化の立ち
上がりのシャープさの目安である(CT−GT)/CT
の値が比較例よりも小さいことから、本発明の硬化剤は
速硬化性であることが確認された。
From Table 2, the unsaturated polyester resin containing the microencapsulated curing agent of the present invention alone or the curing agent combined with the curing accelerator forming the redox system has a much longer pot life than the comparative examples. It was confirmed that it was stabilized. Further, in Table 3, it is a measure of the sharpness of the rising of the curing (CT-GT) / CT
It was confirmed that the curing agent of the present invention was fast-curing because the value of was smaller than that of the comparative example.

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 (イ)常温で固体であり、融点と熱分解
温度との差が少なくとも5℃である不飽和ポリエステル
樹脂硬化用有機過酸化物である芯物質と、(ロ)不飽和
ポリエステル樹脂、前記芯物質との反応性がなく、常温
で固体であり、不飽和ポリエステル樹脂硬化温度におい
て溶解する性質を有し、内側皮膜が高分子電解質、外側
皮膜がアクリル酸エステル、メタクリル酸エステル及び
ビニル芳香族の一種又は二種以上の混合物の重合体から
なる該芯物質を覆っている膜質とよりなる不飽和ポリエ
ステル樹脂用マイクロカプセル化硬化剤。
1. A core material which is (a) an organic peroxide for curing an unsaturated polyester resin which is solid at room temperature and has a difference between a melting point and a thermal decomposition temperature of at least 5 ° C., and (b) an unsaturated polyester. Resin, having no reactivity with the core substance, being solid at room temperature and having a property of dissolving at the unsaturated polyester resin curing temperature, the inner film is a polyelectrolyte, the outer film is an acrylic ester, a methacrylic acid ester and A microencapsulating curing agent for unsaturated polyester resin, which comprises a film material covering the core substance made of a polymer of one kind or a mixture of two or more kinds of vinyl aromatic.
【請求項2】 内側皮膜形成物質水溶液に、常温で固体
であり、融点と熱分解温度との差が少なくとも5℃であ
る芯形成用有機過酸化物を加え、該熱分解温度以下の温
度で液状混合物を生成させ、次いで液状混合物を冷却し
て有機過酸化物芯と内側皮膜とよりなる粒を生成させ、
次に外側樹脂膜生成用単量体の少なくとも1種を添加、
該内側皮膜上に単量体重合樹脂膜を形成させて不飽和ポ
リエステル樹脂用マイクロカプセル化硬化剤を製造する
方法。
2. A core-forming organic peroxide, which is solid at room temperature and has a difference between the melting point and the thermal decomposition temperature of at least 5 ° C., is added to the aqueous solution of the inner film-forming substance, and the temperature is lower than the thermal decomposition temperature. Forming a liquid mixture, then cooling the liquid mixture to form particles consisting of an organic peroxide core and an inner coating,
Next, at least one of the monomers for forming the outer resin film is added,
A method for producing a microencapsulated curing agent for unsaturated polyester resin by forming a monomer-polymerized resin film on the inner film.
【請求項3】 請求項1に記載の不飽和ポリエステル樹
脂用マイクロカプセル化硬化剤及びレドックス系硬化促
進剤からなる不飽和ポリエステル樹脂用硬化剤。
3. A curing agent for unsaturated polyester resin comprising the microencapsulated curing agent for unsaturated polyester resin according to claim 1 and a redox curing accelerator.
【請求項4】 不飽和ポリエステル樹脂と請求項1又は
3のいずれか1項に記載の硬化剤から成る不飽和ポリエ
ステル樹脂組成物。
4. An unsaturated polyester resin composition comprising an unsaturated polyester resin and the curing agent according to claim 1 or 3.
【請求項5】 請求項1又は3のいずれか1項に記載の
硬化剤を用いて不飽和ポリエステル樹脂を硬化する不飽
和ポリエステル樹脂の硬化方法。
5. A method for curing an unsaturated polyester resin, which comprises curing the unsaturated polyester resin with the curing agent according to claim 1.
【請求項6】 不飽和ポリエステル樹脂に請求項1又は
3のいずれか1項に記載の硬化剤を添加することよりな
る貯蔵安定性の高い不飽和ポリエステル樹脂組成物の製
造方法。
6. A method for producing an unsaturated polyester resin composition having high storage stability, which comprises adding the curing agent according to claim 1 to an unsaturated polyester resin.
JP26694891A 1991-09-19 1991-09-19 Microencapsulated curing agent, method for producing the same, unsaturated polyester resin composition containing the same, curing method and stabilization method Expired - Fee Related JP3168627B2 (en)

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DE10216550A1 (en) * 2002-04-15 2003-10-30 Schenectady Int Inc Microcapsules for the production of storage-stable unsaturated polymer compositions
WO2012148629A1 (en) * 2011-03-31 2012-11-01 Ocv Intellectual Capital, Llc Microencapsulated curing agent
JP2013500844A (en) * 2009-07-31 2013-01-10 サントル ナスィオナル ド ラ ルシェルシュ スィアンティフィク Core / shell materials, manufacturing methods, and applications for thermal stimulation of target substances
CN103102431A (en) * 2011-11-10 2013-05-15 中国石油化工股份有限公司 Wax-wrapped peroxide microcapsule and preparation method thereof
US9315655B2 (en) 2011-12-08 2016-04-19 Ocv Intellectual Capital, Llc Fiber reinforced resin molding compound and manufacturing method for fiber reinforced resin molded article therefrom

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0798312A4 (en) * 1995-12-06 1998-01-07 Asahi Chemical Ind Coated granular curing agent for radical-curable compounds and anchor bolt fixing composition prepared therefrom
DE10216550A1 (en) * 2002-04-15 2003-10-30 Schenectady Int Inc Microcapsules for the production of storage-stable unsaturated polymer compositions
JP2013500844A (en) * 2009-07-31 2013-01-10 サントル ナスィオナル ド ラ ルシェルシュ スィアンティフィク Core / shell materials, manufacturing methods, and applications for thermal stimulation of target substances
WO2012148629A1 (en) * 2011-03-31 2012-11-01 Ocv Intellectual Capital, Llc Microencapsulated curing agent
CN103534287A (en) * 2011-03-31 2014-01-22 Ocv智识资本有限责任公司 Microencapsulated curing agent
US8715543B2 (en) 2011-03-31 2014-05-06 Ocv Intellectual Capital, Llc Microencapsulated curing agent
US9725575B2 (en) 2011-03-31 2017-08-08 Ocv Intellectual Capital, Llc Microencapsulated curing agent
CN103102431A (en) * 2011-11-10 2013-05-15 中国石油化工股份有限公司 Wax-wrapped peroxide microcapsule and preparation method thereof
US9315655B2 (en) 2011-12-08 2016-04-19 Ocv Intellectual Capital, Llc Fiber reinforced resin molding compound and manufacturing method for fiber reinforced resin molded article therefrom

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