JPS60139331A - Stabilized organic peroxide composition - Google Patents

Stabilized organic peroxide composition

Info

Publication number
JPS60139331A
JPS60139331A JP25159883A JP25159883A JPS60139331A JP S60139331 A JPS60139331 A JP S60139331A JP 25159883 A JP25159883 A JP 25159883A JP 25159883 A JP25159883 A JP 25159883A JP S60139331 A JPS60139331 A JP S60139331A
Authority
JP
Japan
Prior art keywords
peroxide
org
unsaturated polyester
polyester 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.)
Pending
Application number
JP25159883A
Other languages
Japanese (ja)
Inventor
Hitoshi Imamura
均 今村
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.)
Sanken Kako KK
Original Assignee
Sanken Kako KK
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 Sanken Kako KK filed Critical Sanken Kako KK
Priority to JP25159883A priority Critical patent/JPS60139331A/en
Publication of JPS60139331A publication Critical patent/JPS60139331A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J13/00Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
    • B01J13/02Making microcapsules or microballoons
    • B01J13/06Making microcapsules or microballoons by phase separation
    • B01J13/14Polymerisation; cross-linking
    • B01J13/18In situ polymerisation with all reactants being present in the same phase

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Manufacturing Of Micro-Capsules (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Anti-Oxidant Or Stabilizer Compositions (AREA)

Abstract

PURPOSE:To obtain an org. peroxide composition containing a specific amount of an unsaturated polyester resin and stabilized to shock, by microencapsulating org. peroxide sensible to shock by the unsaturated polyester resin. CONSTITUTION:Org. peroxide (e.g., dibenzoyl peroxide) sensible to shock and solid at a room temp. is microencapsulated by an unsaturated polyester resin to obtain an org. peroxide composition containing 20-70wt% of the aforementioned resin and stabilized to shock. That is, org. peroxide is preliminarily dispersed in a solvent not dissolving org. peroxide, for example, water and a resin solution, in which the unsaturated polyester resin is dissolved, is dripped in the aforementioned aqueous phase and the unsaturated polyester resin becoming insoluble is deposited to the surface of org. peroxide to microencapsulate said org. peroxide. Furthermore, the concn. of org. peroxide in a product can be freely regulated by the amount of the unsaturated polyester resin to be added.

Description

【発明の詳細な説明】 本発明は、衝撃に鋭敏な室温で固体のを機過酸化物を不
飽和ポリエステル樹脂によりマイクロカプセル化するこ
とで得られた、前記樹脂を20乃至70市狽%含むこと
を特徴とする衝撃に対し安定化された有機過酸化物組成
物に関するものである。ここでいうgiIIRに鋭敏な
室温で固体の有機過酸化物とは、JLSK’4810法
により20−以下で爆発的分解を示すものを指す。
DETAILED DESCRIPTION OF THE INVENTION The present invention is a method of producing a shock-sensitive, room-temperature solid organic peroxide, obtained by microencapsulating it with an unsaturated polyester resin, containing 20 to 70% of said resin. The present invention relates to a shock-stabilized organic peroxide composition characterized by the following characteristics. The organic peroxides that are solid at room temperature and are sensitive to gIIIR as used herein refer to those that show explosive decomposition at 20- or less according to the JLSK'4810 method.

室温で固体の衝撃に鋭敏な有機過酸化物例えばジベンゾ
イルペルオキシド(以下B 、P Oと記す)、2・4
−ジクロルベンゾイルペルオキシド等は、純品では取り
扱いに十分注意を払わなければならない。そこで従来よ
り、水を加えて湿体としたり、ジオクチルフタレートや
シリコン油等の可塑剤おるいは溶剤によりペースト状に
され、安定化がはかられ、これら添加剤との混合物とし
て市販され触媒として利用されて来た。しかし、これら
従来の方法では以下に上げる欠点があった。たとえば、
これら触媒を重合反応や硬化反応に使用した場合、これ
ら触媒中の添加剤か樹脂中から抽出されたり、また樹脂
が可塑化されるなどの問題があり、さらにこれらの有機
過酸化物組成物は保管中に添加剤と分離するなどの欠点
かあった。たとえば硬化剤の分野、つまり不飽和ポリエ
ステル樹脂の硬化用触媒として上記の欠点の改良か希求
されていた。
Organic peroxides that are sensitive to solid impacts at room temperature, such as dibenzoyl peroxide (hereinafter referred to as B and PO), 2.4
- Dichlorobenzoyl peroxide, etc. must be handled with great care in pure form. Conventionally, this has been stabilized by adding water to make it into a wet form, or adding plasticizers or solvents such as dioctyl phthalate or silicone oil to make it into a paste. It has been used. However, these conventional methods have the following drawbacks. for example,
When these catalysts are used in polymerization or curing reactions, there are problems such as the additives in these catalysts being extracted from the resin, or the resin being plasticized, and furthermore, these organic peroxide compositions There were drawbacks such as separation from additives during storage. For example, in the field of curing agents, that is, as catalysts for curing unsaturated polyester resins, it has been desired to improve the above-mentioned drawbacks.

本発明者等は、*j 14に鋭敏な有機過酸化物を不飽
和ポリエステル樹脂でマイクロカプセル化することによ
り安定化するべく鋭意研究した結果本発明に至つtこも
のである。すなわち不飽和ポリエステル樹脂が有機過酸
化物の衝撃安定性を増し、JiSK4810法に準して
行なった落槌感度試験の結果、(3Qctにおいて不爆
の有機過酸化物組成物か得られた。
The present inventors have conducted intensive research to stabilize organic peroxides that are sensitive to *j14 by microencapsulating them with unsaturated polyester resin, and have thus arrived at the present invention. That is, the unsaturated polyester resin increases the impact stability of the organic peroxide, and as a result of a drop hammer sensitivity test conducted according to the JiSK4810 method, a non-exploding organic peroxide composition was obtained at 3 Qct.

さらに具体的に説明すると、本発明で得られる有機過酸
化物組成物の製造法は危険な有機過酸化物を取り扱うこ
とから、安全上溶剤系での樹脂の相分離法が最も適当で
あると考えられた。
To explain more specifically, since the method for producing the organic peroxide composition obtained in the present invention involves handling dangerous organic peroxides, it is believed that a solvent-based resin phase separation method is most appropriate for safety reasons. it was thought.

すなわち有機過酸化物を有機過酸化物が不溶である溶剤
、たとえは水に分散させておき、不飽和ポリエステル樹
脂を溶解した樹脂溶液を水相へ滴下することにより、不
溶化してくる不飽和ポリエステル樹脂か有機過酸化物表
面へ析出することでマイクロカプセル化するものである
In other words, by dispersing the organic peroxide in a solvent in which the organic peroxide is insoluble, for example, water, and dropping a resin solution containing the unsaturated polyester resin into the aqueous phase, the unsaturated polyester becomes insolubilized. Microcapsules are formed by depositing on the surface of resin or organic peroxide.

尚こごて添加される不飽和ポリエステル樹脂のbl: 
C製品中の有機過酸化物産1すか自由にコントロール出
来る。尚、衝撃に対する安全性を増す目的から製品中の
樹脂含有量は20重し5以上が」帥当であった。ただし
有機過酸化物以外の添加剤は出来るだけ少なくしたいと
いうユーザーの希望及び一般的に市販されている有機過
酸化物組成物中の有機過酸化物濃度か30重量%以上が
普通であることから本発明で得られる製品中の樹脂鼠は
好ましくは70重惜%以下か適当であった。さて、衝撃
に鋭敏な室温で固体の有機過酸化物類としては、ベンゾ
イルペルオキシド、2・4−ンクロルベンゾイルペルオ
キシド、P−クロルベンゾイルペルオキシド、P−1−
ルイルペルオキシド、売−トルイルペルオキシド、ジア
セチルペルオキシド、アセチルシクロへキシルスルホニ
ルペルオキシドなどが例示される。ここでいう不飽和ポ
リエステル樹脂とは、脂肪族もしくは芳香族飽和多塩基
酸及び脂肪族不飽和多塩酸からなる多塩基酸成分と、脂
肪族多価アルコール又は/及び環状多価アルコールとを
反応させることにより得られる不飽和ポリエステル樹脂
である。ここで脂肪族不飽和多塩基酸としては無水マレ
イン酸、フマル酸、シトラコン酸、イタコン酸などか例
示され、これらは単独あるいは混合物として用いられる
。かかる不飽和多塩基酸と併用して用いられる飽和多塩
基酸としては、たとえばフタル酸、イソフタル酸、テレ
フタル酸、無水フタル酸、ヘキサヒドロ無水フタル酸、
トリメリット酸、ピロメリット酸等の芳香族飽和多塩基
酸やコ/’%り酸、グルタル酸、アジピン酸、セバシン
酸、アゼライン酸等の脂肪族飽和多塩基酸かあけられ、
これらは単独或は2種以上の混合物として(71用する
ことが出来る。又、脂肪族多価アルコールとしてはたと
えはプロピレングリコール、1・3−ブチレンクリコー
ル、1・2−ブチレングリコール、2・3−ブチレング
リコール、ネオペンチルグリコール等の多価アルコール
であり、環状多価アルコールとはビスフェノールAのプ
ロピレンオキサイド付加物、水素化ビスフェノールA等
の環状構造を有する多価アルコールであって、これらは
単独或は、2種以上の混合物として用いられる。ここで
1)1記以外の多価アルコールとしてはエチレングリコ
ール、ジエチレングリコールなどが用いられる。さて本
発明で使用するに適した不飽和ポリエステル樹脂として
は以下の特性を有するものであればよい。すなわち一般
的に行なわれるマイクロカプセル化の手法は溶剤を利用
した相分離法であるため、マイクロカプセルの壁材とな
る不飽和ポリエステル樹脂は、アセトン、ジオキサン、
テトラヒト口°フラン、その他有機過酸化物を誘発分解
することのない適当な溶剤へ溶解すること。さらに本発
明の目的である有機過酸化物の衝撃安定性を高める効果
を示すことである。好ましくは不飽和ポリエステル樹脂
の軟化点がマイクロカプセルの芯材となる有機過酸化物
の自己分解促進温度(たとえばBPOの場合は106℃
である。)より低い温度を有するもののなかから選ばれ
る。
The bl of unsaturated polyester resin added by troweling:
Organic peroxide production in C products can be easily controlled. In addition, for the purpose of increasing safety against impact, the resin content in the product was generally 20% by weight or more. However, due to the user's desire to reduce the amount of additives other than organic peroxide as much as possible, and the organic peroxide concentration in commercially available organic peroxide compositions, it is normal to have an organic peroxide concentration of 30% by weight or more. The resin content in the product obtained by the present invention was preferably 70% or less. Organic peroxides that are solid at room temperature and are sensitive to impact include benzoyl peroxide, 2,4-chlorobenzoyl peroxide, P-chlorobenzoyl peroxide, and P-1-chlorbenzoyl peroxide.
Examples include toluyl peroxide, toluyl peroxide, diacetyl peroxide, and acetylcyclohexylsulfonyl peroxide. The unsaturated polyester resin here refers to the reaction between a polybasic acid component consisting of an aliphatic or aromatic saturated polybasic acid and an aliphatic unsaturated polyhydrochloric acid, and an aliphatic polyhydric alcohol or/and a cyclic polyhydric alcohol. It is an unsaturated polyester resin obtained by. Examples of the aliphatic unsaturated polybasic acids include maleic anhydride, fumaric acid, citraconic acid, and itaconic acid, which may be used alone or as a mixture. Saturated polybasic acids used in combination with such unsaturated polybasic acids include, for example, phthalic acid, isophthalic acid, terephthalic acid, phthalic anhydride, hexahydrophthalic anhydride,
Aromatic saturated polybasic acids such as trimellitic acid and pyromellitic acid and aliphatic saturated polybasic acids such as co/'% phosphoric acid, glutaric acid, adipic acid, sebacic acid, azelaic acid, etc.
These can be used alone or as a mixture of two or more (71).Also, examples of aliphatic polyhydric alcohols include propylene glycol, 1,3-butylene glycol, 1,2-butylene glycol, 2- These are polyhydric alcohols such as 3-butylene glycol and neopentyl glycol, and cyclic polyhydric alcohols are polyhydric alcohols with a cyclic structure such as propylene oxide adducts of bisphenol A and hydrogenated bisphenol A. Alternatively, they may be used as a mixture of two or more.Here, 1) ethylene glycol, diethylene glycol, etc. are used as the polyhydric alcohol other than those mentioned above. Now, unsaturated polyester resins suitable for use in the present invention may be those having the following characteristics. In other words, since the commonly used microencapsulation method is a phase separation method using a solvent, the unsaturated polyester resin that becomes the wall material of the microcapsules is made of acetone, dioxane,
Dissolve in tetrahydrofuran or other suitable solvent that will not induce decomposition of organic peroxides. Furthermore, it is an object of the present invention to demonstrate the effect of increasing the impact stability of organic peroxides. Preferably, the softening point of the unsaturated polyester resin is the self-decomposition promoting temperature of the organic peroxide serving as the core material of the microcapsule (for example, 106°C in the case of BPO).
It is. ) are selected from among those having a lower temperature.

次に具体的に実施例を上げて説明を行うが本発明を限定
するものではない。
Next, specific examples will be given and explained, but the present invention is not limited thereto.

実施例1 攪拌ベラ付き、31の丸底コルベン中へ三建化工■製品
て水湿体品BPOを1477と蒸留水660vを仕込み
、攪拌下にてB P Oパウダーを水中へ分散しておく
。その後757のアセトン中へ、イソフタル醗、無水マ
レイン酸及びネオペンチルグリコールを原料として常法
により得られた不飽和ポリエステル樹脂(以下[J P
=1と記す。)ilclを溶解した樹脂溶液をすみやか
に滴ドする。しかる後樹脂によりマイクロカプセル化さ
れた13 ]) OパウダーをP;(=’S L、1虱
’j’′1.することにより自由at仙件のパウダーか
得られる。尚ここで収−は2167であった。
Example 1 A 31-sized round-bottom colben equipped with a stirring spatula was charged with water wet product BPO 1477 manufactured by Sanken Kako and 660 V of distilled water, and the BPO powder was dispersed in the water while stirring. Thereafter, unsaturated polyester resin (hereinafter [J P
It is written as =1. ) Immediately drop a resin solution containing ilcl. After that, a free at-effect powder can be obtained by converting the 13]) O powder microencapsulated by resin into P;(='SL, 1'j''1. It was 2167.

パウダー中の13 P O含有−は試料をクロロホルム
に溶解後、通常の化学分析法により50車殴%であった
。さらにこの製品についてJISK4810法に準じて
行なった落槌感度試験は60(罪において不爆てあった
The content of 13 PO in the powder was determined to be 50% by standard chemical analysis after dissolving the sample in chloroform. Furthermore, a drop hammer sensitivity test conducted on this product in accordance with the JIS K4810 method was 60 (non-explosive).

実%+B例2 フタル酸、無水マレイン酸及びプロピレングリコールを
原料として常法により得られた不飽和ポリエステル樹脂
(以下tJ P−2と記す。)を用いて実施例1と同一
の条件下でマイクロカプセル化した結果、得られた製品
は常温においてブロッキングしゴム状を呈した。また落
槌感度試験においては100(7)でも不爆であった。
Actual %+B Example 2 An unsaturated polyester resin (hereinafter referred to as tJ P-2) obtained by a conventional method using phthalic acid, maleic anhydride, and propylene glycol as raw materials was subjected to microcoagulation under the same conditions as in Example 1. As a result of encapsulation, the resulting product was blocked and rubbery at room temperature. In addition, in the drop hammer sensitivity test, even 100 (7) was not explosive.

比較例3 実施例1と同様の方法(ただし不一飽和ポリエステル樹
脂としてUP−1を132使用)で得られたパウダー中
にはBPOが90%含有していた。さらにこの製品につ
いてJISK4810法に準して行った落槌感度試験は
30引で不爆、60(iて爆発した。
Comparative Example 3 A powder obtained by the same method as in Example 1 (but using 132 UP-1 as the unsaturated polyester resin) contained 90% BPO. Furthermore, in a drop hammer sensitivity test conducted on this product in accordance with the JIS K4810 method, it did not explode at 30 pulls, but exploded at 60 pulls.

尚、実施例1.2及び比較例3の結果をまとめて表1に
示す。
The results of Example 1.2 and Comparative Example 3 are summarized in Table 1.

表1 ※I BPO純品=10cIn爆発 尚、BPOの自己分解促進温度は106℃(不飽和ポリ
エステル樹脂中)である。
Table 1 *I BPO pure product = 10 cIn explosion The self-decomposition acceleration temperature of BPO is 106°C (in unsaturated polyester resin).

さらに、実用テストの目的で不飽和ポリエステル樹脂の
硬化テストを市販の不飽和ポリエステル樹脂を用いJI
SK6901法により行った。その結果を表2に示す。
Furthermore, for the purpose of practical testing, we conducted a curing test of unsaturated polyester resin using commercially available unsaturated polyester resin.
This was carried out using the SK6901 method. The results are shown in Table 2.

表2 使用樹脂・三建化工■製不飽和ポリエステル樹脂スミア
ノブP−100
Table 2 Resin used: Unsaturated polyester resin smear knob P-100 manufactured by Sanken Kako ■

Claims (1)

【特許請求の範囲】[Claims] 衝撃に鋭敏な室温で固体の有機過酸化物を不飽和ポリエ
ステル樹脂によりマイクロカプセル化することで得られ
た、前記樹脂を20乃至70重量%含むことを特徴とす
る、衝撃に対し安定化された有機過酸化物組成物。
A shock-stabilized product obtained by microencapsulating a shock-sensitive room-temperature solid organic peroxide with an unsaturated polyester resin and containing 20 to 70% by weight of said resin. Organic peroxide composition.
JP25159883A 1983-12-27 1983-12-27 Stabilized organic peroxide composition Pending JPS60139331A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25159883A JPS60139331A (en) 1983-12-27 1983-12-27 Stabilized organic peroxide composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25159883A JPS60139331A (en) 1983-12-27 1983-12-27 Stabilized organic peroxide composition

Publications (1)

Publication Number Publication Date
JPS60139331A true JPS60139331A (en) 1985-07-24

Family

ID=17225195

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25159883A Pending JPS60139331A (en) 1983-12-27 1983-12-27 Stabilized organic peroxide composition

Country Status (1)

Country Link
JP (1) JPS60139331A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0987299A1 (en) * 1998-09-18 2000-03-22 Elf Atochem Deutschland GmbH Compositions containing radical-generating agents and phlegmatizers, use and process for the preparation of such compositions
US8715543B2 (en) 2011-03-31 2014-05-06 Ocv Intellectual Capital, Llc Microencapsulated curing agent
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 (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0987299A1 (en) * 1998-09-18 2000-03-22 Elf Atochem Deutschland GmbH Compositions containing radical-generating agents and phlegmatizers, use and process for the preparation of such compositions
CZ298322B6 (en) * 1998-09-18 2007-08-29 Elf Atochem Deutschland Gmbh Composition in the form of a solution containing substances providing radicals and phlegmatizing 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
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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