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JPH0617417B2 - Method for producing α-methylstyrene copolymer - Google Patents
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JPH0617417B2 - Method for producing α-methylstyrene copolymer - Google Patents

Method for producing α-methylstyrene copolymer

Info

Publication number
JPH0617417B2
JPH0617417B2 JP60166697A JP16669785A JPH0617417B2 JP H0617417 B2 JPH0617417 B2 JP H0617417B2 JP 60166697 A JP60166697 A JP 60166697A JP 16669785 A JP16669785 A JP 16669785A JP H0617417 B2 JPH0617417 B2 JP H0617417B2
Authority
JP
Japan
Prior art keywords
methylstyrene
copolymer
producing
divinylbenzene
carboxylic acid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP60166697A
Other languages
Japanese (ja)
Other versions
JPS6227407A (en
Inventor
浅沼  正
淳子 武田
由子 十倉
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP60166697A priority Critical patent/JPH0617417B2/en
Publication of JPS6227407A publication Critical patent/JPS6227407A/en
Publication of JPH0617417B2 publication Critical patent/JPH0617417B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Polymerisation Methods In General (AREA)
  • Graft Or Block Polymers (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はα−メチルスチレンの共重合体の製造方法に関
する。詳しくはセラミックバインダーなどとして好適な
分解性と相溶性に優れたα−メチルスチレンの共重合体
の製造する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for producing a copolymer of α-methylstyrene. More specifically, the present invention relates to a method for producing a copolymer of α-methylstyrene which is suitable as a ceramic binder and has excellent decomposability and compatibility.

〔従来の技術〕[Conventional technology]

α−メチルスチレンの重合体は極めて容易に分解して低
分子量の単量体等となり、容易に飛散することからセラ
ミックのバインダー、光記録材料などに利用することが
期待されている。しかしながら、α−メチルスチレンは
天井温度が低く、高分子量体を得るためには、低温アニ
オン重合を行う必要があるため、α−メチルスチレンを
主成分とする共重合体はほとんど知られていなかった。
A polymer of α-methylstyrene is extremely easily decomposed to form a low molecular weight monomer or the like and easily scattered, so that it is expected to be used as a ceramic binder, an optical recording material, or the like. However, since α-methylstyrene has a low ceiling temperature, and low-temperature anionic polymerization needs to be performed to obtain a high molecular weight substance, a copolymer containing α-methylstyrene as a main component was hardly known. .

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

α−メチルスチレンの単独重合体は熱、光などによって
容易に分解し、単量体となる優れた重合体であるが、セ
ラミックのバイダンーや光記録材料として用いようとす
ると、アルミナ、シリカ、シリコンカーバイト、シリコ
ンナイトライド、ボロンカーバイト、ボロンナイトライ
ドなどのセラミック粉となじみが悪く、バイダーとして
不適であり、光記録材料としても基板に塗布して乾燥し
た後基板とのなじみが悪く、はがれるなどという問題が
あった。これに対しては、カルボン酸、カルボン酸アミ
ド、カルボン酸エステルなどの極性基を有する単量体と
共重合することが考えられるが、α−メチルスチレンは
上述のような重合特性を有するため他の極性基含有単量
体と共重合することが容易でなく、α−メチルスチレン
と極性基含有単量体を共重合した共重合体の開発が望ま
れていた。
The homopolymer of α-methylstyrene is an excellent polymer that is easily decomposed by heat, light, etc. and becomes a monomer, but when it is used as a ceramic binder or an optical recording material, it is alumina, silica, or silicon. It is not suitable as a ceramic powder such as carbide, silicon nitride, boron carbide, boron nitride, etc., it is not suitable as a binder, and also as an optical recording material, it is not compatible with the substrate after it is dried and peeled off. There was a problem such as. On the other hand, it may be possible to copolymerize with a monomer having a polar group such as carboxylic acid, carboxylic acid amide, and carboxylic acid ester. It is not easy to copolymerize with the polar group-containing monomer, and development of a copolymer obtained by copolymerizing α-methylstyrene and the polar group-containing monomer has been desired.

〔問題点を解決するための手段〕[Means for solving problems]

本発明者らは上記問題点を解決する方法について鋭意検
討し、本発明に到達した。
The present inventors have earnestly studied a method for solving the above problems and arrived at the present invention.

即ち、本発明は、α−メチルスチレンとジビニルベンゼ
ン及び/又はジイソプロペニルベンゼンとの不飽和基含
有共重合体と不飽和カルボン酸及び/又はその誘導体及
びラジカル重合開始剤を有機溶媒に溶解し、水の不存在
下に共重合することを特徴とするα−メチルスチレン共
重合体の製造方法である。
That is, in the present invention, an unsaturated group-containing copolymer of α-methylstyrene and divinylbenzene and / or diisopropenylbenzene, an unsaturated carboxylic acid and / or its derivative, and a radical polymerization initiator are dissolved in an organic solvent. The method for producing an α-methylstyrene copolymer is characterized in that the copolymerization is carried out in the absence of water.

本発明において用いる不飽和基含有共重合体はα−メチ
ルスチレンとジビニルベンゼン及び/又はジイソプロペ
ニルベンゼンの共重合体である。この際α−メチルスチ
レンの30重量%程度をスチレンやその誘導体を使用し
ていてもかまわない。但し、30重量%を越えると分解
性が不良となるので好ましくない。
The unsaturated group-containing copolymer used in the present invention is a copolymer of α-methylstyrene and divinylbenzene and / or diisopropenylbenzene. At this time, styrene or its derivative may be used in about 30% by weight of α-methylstyrene. However, if it exceeds 30% by weight, decomposability becomes poor, which is not preferable.

α−メチルスチレンとジビニルベンゼン及び/又はジイ
ソプロペニルベンゼンの共重合体はラジカル重合法或い
はアニオン重合法で製造することが可能であり、α−メ
チルスチレンとジビニルベンゼン及び/又はジイソプロ
ペニルベンゼンとの総和に対するジビニルベンゼン及び
/又はイソプロペニルベンゼンの割合は2〜30重量%で
あるのが、共重合体の製造時の問題が少く、また次の反
応のためにも好ましい。
The copolymer of α-methylstyrene and divinylbenzene and / or diisopropenylbenzene can be produced by a radical polymerization method or an anionic polymerization method, and α-methylstyrene and divinylbenzene and / or diisopropenylbenzene can be produced. The proportion of divinylbenzene and / or isopropenylbenzene with respect to the total amount of is 2 to 30% by weight, so that there are few problems during the production of the copolymer, and it is also preferable for the next reaction.

上記重合に際しては、過酸化物或いはアゾビスニトリル
などの公知のラジカル重合開始剤及び/又は、アルキル
リチウム、ナトリウムナフタレンなどの公知のアニオン
重合開始剤を用いることが可能であり、その重合条件に
格別の制限はないが、特開昭59−207905号など
に記載された方法を利用することもできる。
In the above-mentioned polymerization, it is possible to use a known radical polymerization initiator such as peroxide or azobisnitrile and / or a known anionic polymerization initiator such as alkyllithium or sodium naphthalene, and the polymerization conditions are special. However, the method described in JP-A-59-207905 or the like can also be used.

上述の方法で得られた共重合体は未反応の単量体から分
離され、ビニル基及び/又はイソプロペニル基含有共重
合体(以下、重合体Aと略記する)が得られる。これを
後述の反応に用いる。
The copolymer obtained by the above method is separated from the unreacted monomer to obtain a vinyl group- and / or isopropenyl group-containing copolymer (hereinafter abbreviated as polymer A). This is used in the reaction described below.

本発明において用いられる不飽和カルボン酸及び/又は
その誘導体としては、アクリル酸、メタクリル酸、アク
リルアミド、N,N−ジメチルアクリルアミド、メタク
リルアミド、N,N−ジメチルメタクリルアミド、アク
リル酸エステル、メタクリル酸エステル類があげられ
る。
Examples of the unsaturated carboxylic acid and / or its derivative used in the present invention include acrylic acid, methacrylic acid, acrylamide, N, N-dimethylacrylamide, methacrylamide, N, N-dimethylmethacrylamide, acrylic acid ester, and methacrylic acid ester. Kind of things.

これらの不飽和カルボン酸及び/又はその誘導体は、得
られるα−メチルスチレンの共重合体中で0.01〜30重
量%となるように用いられる。0.01重量%未満ではセラ
ミック等とのなじみの改善がほとんどなされず、又は3
0重量%を越えるとポリ−α−メチルスチレンの特性が
失なわれ好ましくない。
These unsaturated carboxylic acids and / or their derivatives are used in the resulting α-methylstyrene copolymer in an amount of 0.01 to 30% by weight. If it is less than 0.01% by weight, the compatibility with ceramics is hardly improved, or 3
When it exceeds 0% by weight, the characteristics of poly-α-methylstyrene are lost, which is not preferable.

上記重合体Aと不飽和カルボン酸及び/又はその誘導体
との共重合方法としては、ラジカル重合開始剤の存在下
に行われるかぎり特に制限はないが、通常重合体Aを溶
解した溶液にラジカル重合開始剤(前述のものが使用可
能である)と不飽和カルボン酸及び/又はその誘導体を
加え、ラジカル重合開始剤が作用する条件(加熱、光照
射など)に保つことで行われる。この際、通常重合体A
の濃度は、5〜60重量%、不飽和カルボン酸及び/又
はその誘導体の濃度は0.05〜20重量%、ラジカル重合
開始剤の濃度は0.001〜1重量%に保たれるのが好まし
い。また反応温度としては−30℃〜150℃、好まし
くは0℃〜100℃が適当である。
The copolymerization method of the polymer A and the unsaturated carboxylic acid and / or its derivative is not particularly limited as long as it is carried out in the presence of a radical polymerization initiator, but it is usually radical polymerization in a solution in which the polymer A is dissolved. It is carried out by adding an initiator (the above-mentioned ones can be used) and an unsaturated carboxylic acid and / or a derivative thereof and keeping the conditions (heating, light irradiation, etc.) under which the radical polymerization initiator acts. At this time, the normal polymer A
It is preferable to maintain the concentration of 5 to 60% by weight, the concentration of unsaturated carboxylic acid and / or its derivative is 0.05 to 20% by weight, and the concentration of the radical polymerization initiator is 0.001 to 1% by weight. The reaction temperature is -30 ° C to 150 ° C, preferably 0 ° C to 100 ° C.

本発明においては、共重合は水の不存在下に行われる。In the present invention, the copolymerization is carried out in the absence of water.

〔実施例〕〔Example〕

以下、実施例を挙げ、本発明をさらに説明する。 Hereinafter, the present invention will be further described with reference to examples.

なお、重合体の極限粘度数は30°トルエン溶液で測定
した。
The intrinsic viscosity number of the polymer was measured with a 30 ° toluene solution.

実施例1 トルエン溶媒中でα−メチルスチレン(10vol%)と
ジビニルベンゼン(0.5vol%)をアニオン重合開始剤ブ
チルリチウム(15wt%ヘキサン溶液、0.15vol%)に
より−10℃で重合し、次いで大量のメタノール中に投
じて得たα−メチルスチレン−ジビニルベンゼン共重合
体(極限粘度数0.19、ジビニルベンゼン5.2wt%含有)
5gをトルエン90mlに溶解し、N,N−ジメチルアク
リルアミド0.5ml、アクリル酸0.1mlおよび重合開始剤と
して過酸化ベンゾイル0.25gを加え、80℃で5時間反
応した後、多量のメタノール中に投じた。得られた重合
体(共重合体1)の極限粘度数0.21であり、元素分析及
び赤外吸収スペクトルより算出したN,N−ジメチルア
クリルアミド及びアクリル酸の含量はそれぞれ2.5wt
%、0.8wt%であった。
Example 1 α-Methylstyrene (10 vol%) and divinylbenzene (0.5 vol%) were polymerized at −10 ° C. with an anionic polymerization initiator butyllithium (15 wt% hexane solution, 0.15 vol%) in a toluene solvent, and then a large amount. Α-methylstyrene-divinylbenzene copolymer obtained by throwing it in methanol (containing an intrinsic viscosity of 0.19 and divinylbenzene of 5.2 wt%)
5 g was dissolved in 90 ml of toluene, 0.5 ml of N, N-dimethylacrylamide, 0.1 ml of acrylic acid and 0.25 g of benzoyl peroxide as a polymerization initiator were added, reacted at 80 ° C. for 5 hours, and then poured into a large amount of methanol. . The intrinsic viscosity of the obtained polymer (copolymer 1) was 0.21, and the contents of N, N-dimethylacrylamide and acrylic acid calculated by elemental analysis and infrared absorption spectrum were 2.5 wt.
% And 0.8 wt%.

実施例2 アクリル酸にかえてヒドロキシエチルメタクリル酸エス
テル0.1mlを用いる他は実施例1と同様にして重合体
(共重合体2)を得た。得られた共重合体の極限粘度数
は0.20であり、N,N−ジメチルアクリルアミド及びヒ
ドロキシエチルメタクリル酸エステルの含量はそれぞれ
2.4wt%、0.7wt%であった。
Example 2 A polymer (copolymer 2) was obtained in the same manner as in Example 1 except that 0.1 ml of hydroxyethyl methacrylic acid ester was used instead of acrylic acid. The intrinsic viscosity of the obtained copolymer was 0.20, and the contents of N, N-dimethylacrylamide and hydroxyethyl methacrylate were respectively
It was 2.4 wt% and 0.7 wt%.

実施例3 トルエン溶媒中でα−メチルスチレン(20vol%)、
ジイソプロペニルベンゼン(1vol%)をブチルリチウ
ム(10wt%ヘキサン溶液、0.2vol%)により−10℃
で0.5時間重合し、実施例1と同様に大量のメタノール
中に投じ分離した。得られた共重合体は極限粘度数1.6
3、ジイソプロペニルベンゼン含量5.7wt%であった。
Example 3 α-methylstyrene (20 vol%) in a toluene solvent,
Diisopropenylbenzene (1vol%) was added to -10 ℃ with butyllithium (10wt% hexane solution, 0.2vol%).
Polymerization was carried out for 0.5 hours at room temperature, and the mixture was poured into a large amount of methanol and separated in the same manner as in Example 1. The copolymer obtained has an intrinsic viscosity of 1.6.
3. The diisopropenylbenzene content was 5.7 wt%.

この共重合体10gをジメチルホルムアミド100mlに溶
解し、アクリルアミド0.5gおよびアゾビスイソブチロ
ニトリル0.5gを加え、70℃で10時間重合した。得
られた共重合体3は元素分析よりアクリルアミドを3wt
%含しており、その極限粘度数は1.72であった。
10 g of this copolymer was dissolved in 100 ml of dimethylformamide, 0.5 g of acrylamide and 0.5 g of azobisisobutyronitrile were added, and polymerization was carried out at 70 ° C. for 10 hours. The copolymer 3 thus obtained contained 3 wt% of acrylamide by elemental analysis.
%, And the intrinsic viscosity was 1.72.

以上の実施例1〜3で得られた共重合体1〜3、実施例
1および3で得たα−メチルスチレンとジビニルベンゼ
ンまたはジイソプロペニルベンゼンとの共重合体を用
い、各10gを30mlのトルエンに溶解した溶液にアル
ミナ(粒径2μm)30gを入れ混練して分散性を調べ
た。
Using the copolymers 1 to 3 obtained in Examples 1 to 3 and the copolymers of α-methylstyrene and divinylbenzene or diisopropenylbenzene obtained in Examples 1 and 3, 10 g of each was added to 30 ml. 30 g of alumina (particle size: 2 μm) was added to the solution prepared by dissolving in toluene and kneaded, and the dispersibility was examined.

共重合体1〜3を用いたものでは、アルミナが均一に分
散したスラリーとなったが、不飽和カルボン酸及び/又
はその誘導体を共重合していない重合体を用いた場合に
はアルミナが均一に分散しなかった。
In the case of using the copolymers 1 to 3, a slurry in which alumina was uniformly dispersed was obtained, but when a polymer in which the unsaturated carboxylic acid and / or its derivative was not copolymerized was used, the alumina was uniform. Did not disperse in.

〔発明の効果〕〔The invention's effect〕

本発明の方法を実施することによりポリ−α−メチルス
チレン自身のもつ分解性を保持し、しかもセラミック、
基板などとのなじみのよいα−メチルスチレンの共重合
体を得ることが可能となり、工業的に極めて価値があ
る。
By carrying out the method of the present invention, the degradability possessed by poly-α-methylstyrene itself is retained, and ceramic,
It is possible to obtain a copolymer of α-methylstyrene that is well compatible with substrates and the like, which is extremely valuable industrially.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】α−メチルスチレンとジビニルベンゼン及
び/又はジイソプロペニルベンゼンとの不飽和基含有共
重合体と不飽和カルボン酸及び/又はその誘導体及びラ
ジカル重合開始剤を有機溶媒に溶解し、水の不存在下に
共重合することを特徴とするα−メチルスチレンの共重
合体の製造方法。
1. An unsaturated group-containing copolymer of α-methylstyrene and divinylbenzene and / or diisopropenylbenzene, an unsaturated carboxylic acid and / or its derivative, and a radical polymerization initiator are dissolved in an organic solvent, A method for producing an α-methylstyrene copolymer, which comprises copolymerizing in the absence of water.
JP60166697A 1985-07-30 1985-07-30 Method for producing α-methylstyrene copolymer Expired - Lifetime JPH0617417B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60166697A JPH0617417B2 (en) 1985-07-30 1985-07-30 Method for producing α-methylstyrene copolymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60166697A JPH0617417B2 (en) 1985-07-30 1985-07-30 Method for producing α-methylstyrene copolymer

Publications (2)

Publication Number Publication Date
JPS6227407A JPS6227407A (en) 1987-02-05
JPH0617417B2 true JPH0617417B2 (en) 1994-03-09

Family

ID=15836065

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60166697A Expired - Lifetime JPH0617417B2 (en) 1985-07-30 1985-07-30 Method for producing α-methylstyrene copolymer

Country Status (1)

Country Link
JP (1) JPH0617417B2 (en)

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5817526B2 (en) * 1978-12-20 1983-04-07 旭化成株式会社 Method for producing packing material for chromatography
JPS58201682A (en) * 1982-05-20 1983-11-24 Matsushita Electric Ind Co Ltd optical printer
JPS5966406A (en) * 1982-10-07 1984-04-14 Sumitomo Chem Co Ltd Preparation of fine particulate polymer
JPS59128512A (en) * 1983-01-12 1984-07-24 Matsushita Electric Ind Co Ltd Light printer
JPS6083865A (en) * 1983-10-14 1985-05-13 Matsushita Electric Ind Co Ltd optical printer
JPS60166696A (en) * 1984-02-08 1985-08-29 Asahi Chem Ind Co Ltd Dna of novel physiologically active polypeptide

Also Published As

Publication number Publication date
JPS6227407A (en) 1987-02-05

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