JP2002030119A - Maleimide copolymer and method for producing the same - Google Patents

Maleimide copolymer and method for producing the same

Info

Publication number
JP2002030119A
JP2002030119A JP2000213684A JP2000213684A JP2002030119A JP 2002030119 A JP2002030119 A JP 2002030119A JP 2000213684 A JP2000213684 A JP 2000213684A JP 2000213684 A JP2000213684 A JP 2000213684A JP 2002030119 A JP2002030119 A JP 2002030119A
Authority
JP
Japan
Prior art keywords
monomer
maleimide
weight
polymerization
based copolymer
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
JP2000213684A
Other languages
Japanese (ja)
Inventor
Kenichi Ueda
賢一 上田
Minoru Yamaguchi
稔 山口
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.)
Dai Nippon Printing Co Ltd
Nippon Shokubai Co Ltd
Original Assignee
Dai Nippon Printing Co Ltd
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 Dai Nippon Printing Co Ltd, Nippon Shokubai Co Ltd filed Critical Dai Nippon Printing Co Ltd
Priority to JP2000213684A priority Critical patent/JP2002030119A/en
Publication of JP2002030119A publication Critical patent/JP2002030119A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To obtain a new maleimide copolymer excellent in heat resistance and heat stability and further excellent in alkali solubility, which copolymer has a specified amount of N-substituted maleimide groups, aromatic vinyl monomer groups, and unsaturated monocarboxylic acid monomer groups. SOLUTION: There is provided a maleimide copolymer containing (1) a maleimide copolymer prepared by polymerizing a monomer component containing an N-substituted maleimide monomer, an aromatic vinyl monomer, and an unsaturated monocarboxylic acid monomer, having a content of insolubles in an aqueous alkali solution of at most 10%, and containing at most 10% compound (2) of a specified structure represented by formula I (wherein R1s, which are independent of each other, are each an alkyl, a cycloalkyl, an aryl, an alkyl-substituted aryl, or a halogen-substituted aryl; R2 is hydrogen or methyl; and R3 to R6 are each independently hydrogen, an alkyl, a cycloalkyl, or a cycloalkyl-, aryl- alkylaryl-, or halogen-substituted aryl).

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、新規なマレイミド
系共重合体に関する。より詳しくは、マレイミド系共重
合体が特定量のN置換マレイミド系単量体基、芳香族ビ
ニル系単量体基及び不飽和モノカルボン酸単量体基を持
ち、耐熱性や流熱安定性に優れ、更にアルカリ水溶液可
溶能にも優れた新規なマレイミド系共重合体に関する。
TECHNICAL FIELD The present invention relates to a novel maleimide-based copolymer. More specifically, the maleimide-based copolymer has a specific amount of N-substituted maleimide-based monomer group, aromatic vinyl-based monomer group and unsaturated monocarboxylic acid monomer group, and has heat resistance and flow heat stability. And a novel maleimide-based copolymer excellent in solubility in an aqueous alkali solution.

【0002】[0002]

【従来の技術】N置換マレイミド系単量体と芳香族ビニ
ル系単量体を共重合してなる共重合体は、高い耐熱性と
熱安定性を有するため、各種プラスチックの耐熱向上剤
として用いられたり、そのもの自体をフィルム状や成形
体として耐熱性と透明性を有する樹脂材料とすることが
出来る。
2. Description of the Related Art Copolymers obtained by copolymerizing an N-substituted maleimide monomer and an aromatic vinyl monomer have high heat resistance and thermal stability. Or a resin material having heat resistance and transparency as a film or molded product itself.

【0003】例えば、N置換マレイミド系単量体と芳香
族ビニル系単量体を共重合してなる共重合体が、AS樹
脂との相溶性に優れていることから、これら2種類の樹
脂をABS樹脂に配合してなる組成物(特開昭63−1
59458)が提案されている。また、アルキルマレイ
ミド系単量体と芳香族ビニル系単量体からなる共重合体
で透明性に優れた耐熱樹脂(特開平2−127407)
が提案されている。一方、アルカリ可溶性重合体は、塩
基性液体で溶解除去されるので、包装、表面保護、接着
層など種々の用途に利用し、不要になれば内容物や被保
護物表面を損傷することなく容易に除去できる。これま
で、(メタ)アクリル酸エステルと不飽和カルボン酸と
を共重合してなる重合体で塩基性液体に溶解可能なフィ
ルム用材料(特開平7−149837)が提案されてい
る。また、マレイミド系単量体と芳香族ビニル系単量体
のラジカル重合を行ってマレイミド系共重合体を作る場
合、マレイミド系単量体と芳香族ビニル系単量体のデイ
ールスアルダー反応を経由して化合物(1)が副生する
ことが知られており、その量を出来るだけ少なくする方
法も提案されている。(特開平6−93044)しか
し、これら共重合体の製造方法を持ってしても、耐熱性
や流熱安定性に優れ、しかもアルカリ水溶液可溶能にも
優れたマレイミド系共重合体を得ることはできなかっ
た。また、一般的にマレイミド系単量体と芳香族ビニル
系単量体は交互重合性が高く、通常のラジカル重合下で
重合を行った場合、まず交互共重合体が生成する傾向が
ある。第3成分として不飽和モノカルボン酸系単量体を
導入した場合も同様に重合初期にマレイミド系単量体と
芳香族ビニル系単量体を多く含んだ共重合体を生成し、
その結果、不飽和モノカルボン酸系単量体が残存しやす
く、重合後半に不飽和モノカルボン酸系単量体を多く含
んだ共重合体が生成しやすいという傾向がある。その結
果、得られた共重合体は、組成分布が多いものとなり、
熱安定性やアルカリ水溶液可溶能に劣った成分を含み、
重合体全体としても性能が劣ったものとなる。そのた
め、単にマレイミド系単量体と芳香族ビニル系単量体及
び不飽和モノカルボン酸系単量体を共重合しても、耐熱
性や流熱安定性に優れ、しかもアルカリ水溶液可溶能に
も優れたマレイミド系共重合体組成物を得ることはでき
なかった。
For example, a copolymer obtained by copolymerizing an N-substituted maleimide monomer and an aromatic vinyl monomer has excellent compatibility with an AS resin. Compositions blended with ABS resin (JP-A-63-1
59458) has been proposed. Further, a heat-resistant resin excellent in transparency and made of a copolymer comprising an alkylmaleimide-based monomer and an aromatic vinyl-based monomer (JP-A-2-127407)
Has been proposed. On the other hand, alkali-soluble polymers are dissolved and removed with a basic liquid, so they can be used for various purposes such as packaging, surface protection, and adhesive layers. Can be removed. Heretofore, there has been proposed a film material which is a polymer obtained by copolymerizing a (meth) acrylic acid ester and an unsaturated carboxylic acid and which can be dissolved in a basic liquid (JP-A-7-149837). In addition, when a maleimide-based copolymer is produced by radical polymerization of a maleimide-based monomer and an aromatic vinyl-based monomer, via a Diels-Alder reaction between the maleimide-based monomer and the aromatic vinyl-based monomer As a result, it is known that compound (1) is produced as a by-product, and a method for minimizing the amount has been proposed. (JP-A-6-93044) However, even with the method for producing these copolymers, a maleimide-based copolymer having excellent heat resistance and flow heat stability and excellent solubility in an aqueous alkali solution can be obtained. I couldn't do that. Generally, the maleimide-based monomer and the aromatic vinyl-based monomer have a high alternating polymerizability, and when the polymerization is performed under ordinary radical polymerization, an alternating copolymer tends to be formed first. Similarly, when an unsaturated monocarboxylic acid-based monomer is introduced as the third component, a copolymer containing a large amount of a maleimide-based monomer and an aromatic vinyl-based monomer is generated in the early stage of polymerization,
As a result, the unsaturated monocarboxylic acid monomer tends to remain, and a copolymer containing a large amount of the unsaturated monocarboxylic acid monomer tends to be formed in the latter half of the polymerization. As a result, the obtained copolymer has a large composition distribution,
Contains components with poor thermal stability and poor solubility in alkaline aqueous solutions,
The performance of the polymer as a whole is inferior. Therefore, simply copolymerizing a maleimide-based monomer with an aromatic vinyl-based monomer and an unsaturated monocarboxylic acid-based monomer is excellent in heat resistance and flow heat stability, and furthermore, in solubility in an aqueous alkali solution. However, no excellent maleimide copolymer composition could be obtained.

【0004】[0004]

【発明が解決しようとする課題】本発明の課題は、マレ
イミド系重合体の優れた耐熱性、熱安定性を有し、更に
優れたアルカリ水溶液可溶能を合わせ持った重合体を提
供することを課題とする。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a maleimide-based polymer which has excellent heat resistance and thermal stability, and also has excellent solubility in an aqueous alkali solution. As an issue.

【0005】[0005]

【課題を解決するための手段】本願発明者は、上記従来
の問題点を解決すべく、マレイミド系単量体と芳香族ビ
ニル系単量体及び不飽和カルボン酸系単量体の共重合体
の製造方法について鋭意検討した結果した。その結果、
N置換マレイミド系単量体(a)10〜80重量%、芳
香族ビニル系単量体(b)10〜80重量%および不飽
和モノカルボン酸系単量体(c)1〜70重量%を含む
単量体成分を重合してなるマレイミド系共重合体(1)
を製造する方法において、単量体(b)および単量体
(c)及び必要に応じて溶剤を反応器に供給後、重合を
開始するとともに残った単量体(b)および単量体
(c)と、単量体(a)を予め混合することなく連続的
又は断続的に重合系中に供給しながら重合反応を行うこ
とにより、重合体の組成分布を少なくし、その結果アル
カリ水溶液可溶能のない成分の生成をできるだけ抑える
ことができることを見出した。そして、上記方法を採用
することにより、耐熱性や熱安定性に優れ、しかもアル
カリ水溶液可溶能にも優れたマレイミド系共重合体組成
物を得ることが出来ることを見出して、本発明を完成さ
せるに至った。即ち、請求項1のマレイミド系共重合体
は、上記の課題を解決する為に、 N置換マレイミド系単
量体(a)10〜80重量%、芳香族ビニル系単量体
(b)10〜80重量%および不飽和モノカルボン酸系
単量体(c)1〜70重量%を含む単量体成分を重合し
てなるマレイミド系共重合体であって、アルカリ水溶液
不溶分が10重量%以下であるであることを特徴として
いる。また、請求項2記載のマレイミド系共重合体組成
物は、上記の課題を解決する為に、 N置換マレイミド系
単量体(a)10〜80重量%、芳香族ビニル系単量体
(b)10〜80重量%および不飽和モノカルボン酸系
単量体(c)1〜70重量%を含む単量体成分を重合し
てなるマレイミド系共重合体であって、下記一般式
(1)で示される特定構造の化合物(2)の含有量が1
0重量%以下であるマレイミド系共重合体であることを
特徴としている。
In order to solve the above-mentioned conventional problems, the present inventor has proposed a copolymer of a maleimide monomer, an aromatic vinyl monomer and an unsaturated carboxylic acid monomer. As a result of intensive studies on the manufacturing method of the product. as a result,
10 to 80% by weight of an N-substituted maleimide monomer (a), 10 to 80% by weight of an aromatic vinyl monomer (b) and 1 to 70% by weight of an unsaturated monocarboxylic acid monomer (c) Maleimide copolymer obtained by polymerizing monomer components containing
In the method for producing the above, after the monomer (b) and the monomer (c) and, if necessary, the solvent are supplied to the reactor, the polymerization is started and the remaining monomer (b) and the monomer ( By carrying out the polymerization reaction while continuously or intermittently feeding the monomer (a) into the polymerization system without previously mixing the monomer (a) and the monomer (a), the composition distribution of the polymer is reduced, and as a result It has been found that the generation of insoluble components can be suppressed as much as possible. By adopting the above method, it was found that a maleimide-based copolymer composition having excellent heat resistance and thermal stability, and also having excellent solubility in an aqueous alkali solution, could be obtained, and the present invention was completed. It led to. That is, in order to solve the above-mentioned problems, the maleimide-based copolymer according to claim 1 has an N-substituted maleimide-based monomer (a) of 10 to 80% by weight and an aromatic vinyl-based monomer (b) of 10 to 10% by weight. A maleimide-based copolymer obtained by polymerizing a monomer component containing 80% by weight and 1 to 70% by weight of an unsaturated monocarboxylic acid-based monomer (c), wherein an insoluble content of an alkaline aqueous solution is 10% by weight or less. It is characterized by being. Further, in order to solve the above-mentioned problems, the maleimide-based copolymer composition according to claim 2 has an N-substituted maleimide-based monomer (a) of 10 to 80% by weight and an aromatic vinyl-based monomer (b). A) a maleimide-based copolymer obtained by polymerizing a monomer component containing 10 to 80% by weight and 1 to 70% by weight of an unsaturated monocarboxylic acid monomer (c); The content of the compound (2) having a specific structure represented by
It is characterized by being a maleimide-based copolymer having a content of 0% by weight or less.

【0006】[0006]

【化2】 Embedded image

【0007】(但し上記一般式(1)において、R1
互いに独立してアルキル基、シクロアルキル基、アリー
ル基、アルキル置換アリール基またはハロゲン置換アリ
ール基を表し;R2は水素またはメチル基を表し;R3
6はそれぞれ独立に水素、アルキル基、シクロアルキ
ル基、シクロアルキル基、アリール基、アルキル置換ア
リール基またはハロゲン置換アリール基を表す。)であ
る。
(Wherein, in the general formula (1), R 1 independently represents an alkyl group, a cycloalkyl group, an aryl group, an alkyl-substituted aryl group or a halogen-substituted aryl group; R 2 represents hydrogen or a methyl group. Represents; R 3 to
R 6 each independently represents hydrogen, an alkyl group, a cycloalkyl group, a cycloalkyl group, an aryl group, an alkyl-substituted aryl group, or a halogen-substituted aryl group. ).

【0008】更に、請求項3記載のマレイミド系共重合
体の製造方法は、上記の課題を解決する為に、 N置換マ
レイミド系単量体(a)10〜80重量%、芳香族ビニ
ル系単量体(b)10〜80重量%および不飽和モノカ
ルボン酸系単量体(c)1〜70重量%を含む単量体成
分を重合してなるマレイミド系共重合体(1)を製造す
る方法において、単量体(b)および単量体(c)及び
必要に応じて溶剤を反応器に供給後、重合を開始すると
ともに残った単量体(b)および単量体(c)と、単量
体(a)を連続的又は断続的に重合系中に供給しながら
重合反応を行うことを特徴としている。
Further, in order to solve the above-mentioned problems, the method for producing a maleimide-based copolymer according to the third aspect of the present invention provides an N-substituted maleimide-based monomer (a) in an amount of 10 to 80% by weight and an aromatic vinyl-based monomer. A maleimide copolymer (1) produced by polymerizing a monomer component containing 10 to 80% by weight of the monomer (b) and 1 to 70% by weight of the unsaturated monocarboxylic acid monomer (c) is produced. In the method, after supplying the monomers (b) and (c) and, if necessary, a solvent to the reactor, the polymerization is started and the remaining monomers (b) and (c) The polymerization reaction is carried out while continuously or intermittently supplying the monomer (a) into the polymerization system.

【0009】また、請求項4記載のマレイミド系共重合
体の製造方法は、上記の課題を解決する為に、 N置換マ
レイミド系単量体(a)10〜80重量%、芳香族ビニ
ル系単量体(b)10〜80重量%および不飽和モノカ
ルボン酸系単量体(c)1〜70重量%を含む単量体成
分を重合してなるマレイミド系共重合体(1)を製造す
る方法において、単量体(b)および単量体(c)及び
必要に応じて溶剤を反応器に供給後、重合を開始すると
ともに残った単量体(b)および単量体(c)と、単量
体(a)を連続的又は断続的に重合系中に供給しながら
重合反応を行う際に、単量体(a)と単量体(b)は予
め混合することなく供給することを特徴としている。
In order to solve the above-mentioned problems, a method for producing a maleimide-based copolymer according to claim 4 is to provide an N-substituted maleimide-based monomer (a) in an amount of 10 to 80% by weight and an aromatic vinyl-based monomer. A maleimide copolymer (1) produced by polymerizing a monomer component containing 10 to 80% by weight of the monomer (b) and 1 to 70% by weight of the unsaturated monocarboxylic acid monomer (c) is produced. In the method, after supplying the monomers (b) and (c) and, if necessary, a solvent to the reactor, the polymerization is started and the remaining monomers (b) and (c) When conducting the polymerization reaction while continuously or intermittently supplying the monomer (a) into the polymerization system, the monomers (a) and (b) are supplied without being mixed in advance. It is characterized by.

【0010】以下本発明を詳しく説明する。マレイミド
系共重合体(1)を構成するN置換マレイミド系単量体
(a)、芳香族ビニル系単量体(b)及び、不飽和モノ
カルボン酸系単量体(c)を含む単量体成分等の構成割
合としては、 N置換マレイミド系単量体(a)、芳香族
ビニル系単量体(b)及び、不飽和カルボン酸系単量体
(c)を含む単量体成分が、さらに必要に応じて共重合
可能なその他の単量体(d)を含んでなる場合、その単
量体成分の総量を100重量%とした時に、各単量体成
分の構成割合が、 (a)10〜80重量%、(b)10
〜80重量%及び(c)1〜70重量%、及びその他共
重合可能な単量体(d)0〜20重量%である事が好ま
しい。さらに好ましくは、(a)20〜60重量%、
(b)20〜60重量%、(c)5〜60重量%、
(d)0〜15重量%である。 さらに好ましくは、
(a)30〜50重量%、(b)30〜50重量%、
(c)10〜50重量%、(d)0〜10重量%であ
る。
Hereinafter, the present invention will be described in detail. Monomer containing an N-substituted maleimide monomer (a), an aromatic vinyl monomer (b), and an unsaturated monocarboxylic acid monomer (c) constituting the maleimide copolymer (1) As the composition ratio of the body components, etc., the monomer components including the N-substituted maleimide monomer (a), the aromatic vinyl monomer (b), and the unsaturated carboxylic acid monomer (c) And, if necessary, other copolymerizable monomer (d), when the total amount of the monomer components is 100% by weight, the constitutional ratio of each monomer component is represented by ( a) 10 to 80% by weight, (b) 10
It is preferable that the content is from about 80% by weight and from 1 to 70% by weight of (c), and from 0 to 20% by weight of another copolymerizable monomer (d). More preferably, (a) 20 to 60% by weight,
(B) 20 to 60% by weight, (c) 5 to 60% by weight,
(D) 0 to 15% by weight. More preferably,
(A) 30 to 50% by weight, (b) 30 to 50% by weight,
(C) 10 to 50% by weight, and (d) 0 to 10% by weight.

【0011】不飽和モノカルボン酸系単量体(c)の含
有量が上記範囲を下回る場合、アルカリ水溶液可溶能が
低下する恐れがある。上記範囲を超えると、耐熱性や熱
安定性が低下する恐れがある。また、N置換マレイミド
系単量体(a)の含有量が上記範囲以下であると、耐熱
性が低下する恐れがあり、上記範囲を超えると、本発明
のマレイミド系共重合体(1)のアルカリ水溶液可溶能
が低下する他、包装、表面保護、接着層等の用途に用い
た場合、機械強度が低下する恐れがある。
When the content of the unsaturated monocarboxylic acid monomer (c) is less than the above range, the solubility of the aqueous alkali solution may be reduced. If it exceeds the above range, heat resistance and thermal stability may be reduced. When the content of the N-substituted maleimide-based monomer (a) is less than the above range, heat resistance may be reduced. When the content exceeds the above range, the content of the maleimide-based copolymer (1) of the present invention may be reduced. In addition to reducing the solubility of the aqueous alkali solution, when used for applications such as packaging, surface protection, and adhesive layers, the mechanical strength may be reduced.

【0012】本発明の、マレイミド系共重合体(1)
は、アルカリ水溶液不溶分が10重量%以下であること
が好ましく、5重量%以下であることが更に好ましく、
3重量%以下であることが最も好ましい。上記のアルカ
リ水溶液不溶分は、本発明のマレイミド系共重合体
(1)の0.5%−KOH水溶液に対する溶解性で評価
した。より具体的には、本発明のマレイミド系共重合体
(1)からなる厚さ50μmのフィルムの、50℃にお
ける200mlの0.5%KOH水溶液に対する溶解性
テストでアルカリ不溶分の存在量を求め、評価する事が
できる。
The maleimide copolymer (1) of the present invention
Is preferably not more than 10% by weight, more preferably not more than 5% by weight of an alkali aqueous solution insoluble matter,
Most preferably, it is at most 3% by weight. The insoluble content of the alkali aqueous solution was evaluated based on the solubility of the maleimide copolymer (1) of the present invention in a 0.5% -KOH aqueous solution. More specifically, the alkali insoluble content of a 50 μm thick film made of the maleimide copolymer (1) of the present invention was determined by a solubility test in 200 ml of a 0.5% KOH aqueous solution at 50 ° C. , Can be evaluated.

【0013】マレイミド系共重合体(1)中に含まれ
る、下記一般式(1)で表わされる特定構造の化合物
(2)は、10重量%以下が好ましく、5重量%以下が更
に好ましく、2重量%以下が更に好ましく、1重量%以下
であることが最も好ましい。一般式(1)で表わされる
化合物(2)が上記範囲より多いと、マレイミド系共重
合体の熱安定性やアルカリ水溶液可溶能が低下する恐れ
がある。
The compound (2) having a specific structure represented by the following general formula (1) contained in the maleimide copolymer (1) is preferably at most 10% by weight, more preferably at most 5% by weight. It is more preferably at most 1% by weight, most preferably at most 1% by weight. When the amount of the compound (2) represented by the general formula (1) is larger than the above range, the thermal stability and the solubility of the maleimide-based copolymer in an aqueous alkali solution may be reduced.

【0014】[0014]

【化3】 Embedded image

【0015】(但し上記一般式(1)において、R1
互いに独立してアルキル基、シクロアルキル基、アリー
ル基、アルキル置換アリール基またはハロゲン置換アリ
ール基を表し;R2は水素またはメチル基を表し;R3
6はそれぞれ独立に水素、アルキル基、シクロアルキ
ル基、シクロアルキル基、アリール基、アルキル置換ア
リール基またはハロゲン置換アリール基を表す。) 上記、 N置換マレイミド系単量体(a)としては、具体
的には、フェニルマレイミド、ベンジルマレイミド、ナ
フチルマレイミド、o−クロロフェニルマレイミドなど
の芳香族置換マレイミド、メチルマレイミド、エチルマ
レイミド、プロピルマレイミド、イソプロピルマレイミ
ド、シクロヘキシルマレイミドなどのアルキル置換マレ
イミドが挙げられる。これらマレイミド系単量体は、1
種または2種以上混合して使用することも出来る。この
なかで、工業的な入手のし易さ、及び単量体の毒性が比
較的少ないことから、フェニルマレイミド、シクロヘキ
シルマレイミドが好ましい。更に、透明性、熱安定性の
観点からシクロヘキシルマレイミドがもっとも好まし
い。シクロヘキシルマレイミドを使用する場合は、シク
ロヘキシルマレイミド中に副生物として含まれるシクロ
ヘキシルアミノ無水コハク酸の含有量を1重量%以下に
低減した上で使用することが好ましい。
(However, in the general formula (1), R 1 independently represents an alkyl group, a cycloalkyl group, an aryl group, an alkyl-substituted aryl group or a halogen-substituted aryl group; R 2 represents hydrogen or a methyl group. Represents; R 3 to
R 6 each independently represents hydrogen, an alkyl group, a cycloalkyl group, a cycloalkyl group, an aryl group, an alkyl-substituted aryl group, or a halogen-substituted aryl group. Examples of the N-substituted maleimide-based monomer (a) include, specifically, aromatic-substituted maleimides such as phenylmaleimide, benzylmaleimide, naphthylmaleimide, and o-chlorophenylmaleimide, methylmaleimide, ethylmaleimide, propylmaleimide, Examples include alkyl-substituted maleimides such as isopropyl maleimide and cyclohexyl maleimide. These maleimide-based monomers include 1
Species or a mixture of two or more can be used. Of these, phenylmaleimide and cyclohexylmaleimide are preferred because of their industrial availability and relatively low toxicity of monomers. Furthermore, cyclohexylmaleimide is most preferred from the viewpoint of transparency and thermal stability. When using cyclohexylmaleimide, it is preferable to use it after reducing the content of cyclohexylaminosuccinic anhydride contained as a by-product in cyclohexylmaleimide to 1% by weight or less.

【0016】上記、芳香族ビニル系単量体(b)として
は、具体的には、スチレン、α−メチルスチレン、p−
メチルスチレン、p−クロロスチレンなどが挙げられ
る。これら芳香族ビニル系単量体は、1種または2種以
上混合して使用することも出来る。この中で、工業的入
手のし易さ、及び重合性の点からスチレンが好ましい。
As the aromatic vinyl monomer (b), specifically, styrene, α-methylstyrene, p-
Methyl styrene, p-chlorostyrene and the like can be mentioned. These aromatic vinyl monomers can be used alone or in combination of two or more. Of these, styrene is preferred from the viewpoint of industrial availability and polymerizability.

【0017】上記、不飽和モノカルボン酸系単量体
(c)としては、具体的にはメタアクリル酸、アクリル
酸などが挙げられる。これら不飽和モノカルボン酸系単
量体は、1種または2種混合して使用することができ
る。
Specific examples of the unsaturated monocarboxylic acid monomer (c) include methacrylic acid and acrylic acid. These unsaturated monocarboxylic acid monomers can be used alone or in combination of two or more.

【0018】上記(a)、(b)、(c)以外の、その
他共重合可能な単量体(d)は、本発明の趣旨を逸脱し
ない限り特に限定はないが、具体的には、メタクリル酸
メチル、メタアクリル酸エチル、メタクリル酸プロピ
ル、メタクリル酸2−エチルヘキシルなどのメタクリル
酸エステル、アクリル酸メチル、アクリル酸ブチルなど
のアクリル酸エステル、アクリロニトリル、メタクリロ
ニトリルなどのシアン化ビニル、無水マレイン酸などの
不飽和ジカルボン酸無水物等が挙げられる。これら、そ
の他共重合可能な単量体は1種または2種以上混合して
使用することも出来る。マレイミド系共重合体(1)の
分子量は、アルカリ可溶能を発揮させるために、重量平
均分子量が5,000〜200,000の範囲である事が好ましく、
5,000〜100,000の範囲である事が更に好ましく、10,000
〜50,000が更に好ましい。重量平均分子量が上記範囲を
上回ると、アルカリ水溶液可溶能が低下する恐れがあ
る。一方、上記範囲を下回ると、耐熱性や熱安定性が低
下する恐れがある。
The other copolymerizable monomer (d) other than the above (a), (b) and (c) is not particularly limited as long as it does not depart from the gist of the present invention. Methacrylates such as methyl methacrylate, ethyl methacrylate, propyl methacrylate, 2-ethylhexyl methacrylate; acrylates such as methyl acrylate and butyl acrylate; vinyl cyanide such as acrylonitrile and methacrylonitrile; and maleic anhydride And unsaturated dicarboxylic anhydrides such as acids. These and other copolymerizable monomers can be used alone or in combination of two or more. The molecular weight of the maleimide-based copolymer (1) is preferably such that the weight average molecular weight is in the range of 5,000 to 200,000 in order to exhibit alkali-solubility,
More preferably in the range of 5,000 to 100,000, 10,000
~ 50,000 is more preferred. When the weight average molecular weight exceeds the above range, the solubility of the aqueous alkali solution may be reduced. On the other hand, when the ratio is below the above range, heat resistance and thermal stability may decrease.

【0019】また、本発明の、マレイミド系共重合体
(1)の、GPCで測定した重量平均分子量と数平均分
子量の比(Mw/Mn)は、4.0以下が好ましく、
3.0以下がさらに好ましく、2.5以下が最も好まし
い。Mw/Mnが4.0を超えると、熱安定性やアルカ
リ水溶液可溶能が低下する恐れがある。
Further, the ratio (Mw / Mn) of the weight average molecular weight to the number average molecular weight of the maleimide copolymer (1) of the present invention as measured by GPC is preferably 4.0 or less,
It is more preferably at most 3.0, most preferably at most 2.5. If Mw / Mn exceeds 4.0, thermal stability and alkali aqueous solution solubility may be reduced.

【0020】マレイミド系共重合体(1)は、50〜3
00mgKOH/g 、好ましくは70〜200mgKOH/g の酸価
を持つ。重合体(1)の酸価が前記範囲を下回ると重合
体にアルカリ水溶液可溶能がなくなり、前記範囲を上回
ると重合体(1)がもろくなり、各種成形品にした場合
強度物性が出にくくなる。例えば、フィルムや、被覆
材、コート材用途においては、フィルム強度が出にくく
なり,やぶれやすくなる。
The maleimide-based copolymer (1) contains 50 to 3
It has an acid number of 00 mg KOH / g, preferably 70-200 mg KOH / g. When the acid value of the polymer (1) falls below the above range, the polymer loses the solubility in an aqueous alkali solution, and when the acid value exceeds the above range, the polymer (1) becomes brittle, and when it is made into various molded articles, strength properties are hardly exhibited. Become. For example, in a film, a coating material, and a coating material, the film strength is hardly obtained, and the film is easily broken.

【0021】マレイミド系共重合体(1)の製造方法と
しては、公知の溶液重合、懸濁重合、乳化重合を採用す
ることが出来るが、懸濁重合、乳化重合では、懸濁剤や
乳化剤が混入するため、透明性低下の原因となる恐れが
ある。また、懸濁重合、乳化重合では、特定不純物
(2)が生成する恐れがある他、組成分布が出来やす
く、アルカリ水溶液可溶能が低下する恐れがある。更
に、懸濁重合法、乳化重合法では、水中での分散状態で
反応させるため、後述する、本発明に好適な原料単量体
の供給方法の工夫を行っても、後から供給する単量体が
十分混合せず、アルカリ可溶能や熱安定性が低下する恐
れがある。従って、本発明のマレイミド系共重合体
(1)としては、マレイミド系単量体を用いて、溶剤存
在下でその重合が行われる溶液重合方法によって得られ
た重合体である事が好ましい形態である。更に、マレイ
ミド系単量体を用いた回分式溶液重合方法によって得ら
れた共重合体である事が最も好ましい形態である。
As a method for producing the maleimide-based copolymer (1), known solution polymerization, suspension polymerization, and emulsion polymerization can be adopted. In the suspension polymerization and emulsion polymerization, a suspending agent and an emulsifier are used. Since it is mixed, it may cause a decrease in transparency. In addition, in the suspension polymerization and the emulsion polymerization, the specific impurity (2) may be generated, the composition may be easily distributed, and the solubility of the alkaline aqueous solution may be reduced. Further, in the suspension polymerization method and the emulsion polymerization method, the reaction is carried out in a dispersed state in water. There is a possibility that the body is not sufficiently mixed, and the alkali-solubility and thermal stability are reduced. Therefore, the maleimide-based copolymer (1) of the present invention is preferably a polymer obtained by a solution polymerization method in which a maleimide-based monomer is polymerized in the presence of a solvent using a maleimide-based monomer. is there. Further, the most preferred form is a copolymer obtained by a batch solution polymerization method using a maleimide-based monomer.

【0022】上記重合反応における重合温度は、使用す
る重合開始剤等に合わせて設定すれば良く、特に限定さ
れないが、50℃〜200℃が好ましく、80〜150
℃が更に好ましい。重合温度が上記範囲を下回ると、分
解温度の低い開始剤を用いる必要があり、開始剤を冷却
保存する設備が必要となるなど工業的製造に不利であ
る。上記範囲を上回ると、重合温度に昇温する途中でモ
ノマーが熱重合を始めるため好ましくない。
The polymerization temperature in the above polymerization reaction may be set according to the polymerization initiator to be used, etc., and is not particularly limited, but is preferably 50 ° C. to 200 ° C., and is preferably 80 ° C. to 150 ° C.
C is more preferred. If the polymerization temperature is lower than the above range, it is necessary to use an initiator having a low decomposition temperature, which is disadvantageous for industrial production such as requiring equipment for cooling and storing the initiator. Exceeding the above range is not preferable because the monomer starts thermal polymerization during the heating to the polymerization temperature.

【0023】上記溶液重合で使用する溶剤は特に限定な
く、例えば上記の溶液重合反応に支障がなく、また本発
明の重合体を得るための上記単量体と生成した本発明の
重合体の両方を溶解しうる液体であれば特に制限はな
く、たとえば、メタノール、エタノール、グリコールな
どの炭素原子数1〜3個の脂肪族アルコール、テトラヒ
ドロフランなどの環状エーテルやメチルエチルケトン、
メチルイソブチルケトンなどのケトン類、ジメチルスル
ホキシド、ジメチルホルムアミドなどの極性を有する有
機溶剤が挙げられる。非水系の分散重合に用いられる溶
剤は、この発明の重合体を得るための上記単量体が溶解
可能で、かつ、生成した本発明の重合体が不溶である液
体であれば特に制限はなく、たとえば、ベンゼン、トル
エン、ヘキサン、シクロヘキサンのような液状の炭化水
素などの非極性の有機溶剤が挙げられる。上記溶液重合
や非水系の分散重合に用いられる溶剤の量は、単量体の
合計重量に対して、20〜80重量%が好ましく、30
〜70重量%がより好ましい。前記範囲を下回ると重合
終了時に増粘のため攪拌が不充分になるおそれがあり、
上回ると生成する重合体の分子量が上記範囲内にまで上
がらないおそれがある。重合開始剤は、公知のラジカル
重合開始剤である過酸化物、アゾ化合物が好適に用いら
れ、重合温度に応じて適宜決定で、単量体の合計重量に
対して、通常、0.001〜1.0重量%の割合で使用
される。
The solvent used in the solution polymerization is not particularly limited. For example, the solvent does not interfere with the solution polymerization reaction, and both the monomer for producing the polymer of the present invention and the produced polymer of the present invention are used. There is no particular limitation as long as it is a liquid that can dissolve, for example, aliphatic alcohols having 1 to 3 carbon atoms such as methanol, ethanol and glycol, cyclic ethers such as tetrahydrofuran and methyl ethyl ketone,
Examples thereof include ketones such as methyl isobutyl ketone, and polar organic solvents such as dimethyl sulfoxide and dimethylformamide. The solvent used in the non-aqueous dispersion polymerization is not particularly limited as long as the above-mentioned monomer for obtaining the polymer of the present invention can be dissolved therein, and the produced polymer of the present invention is insoluble in liquid. Examples thereof include non-polar organic solvents such as liquid hydrocarbons such as benzene, toluene, hexane, and cyclohexane. The amount of the solvent used in the solution polymerization or the non-aqueous dispersion polymerization is preferably 20 to 80% by weight based on the total weight of the monomers.
~ 70% by weight is more preferred. If it is below the range, stirring may be insufficient due to thickening at the end of polymerization,
If the molecular weight exceeds the above range, the molecular weight of the produced polymer may not be increased within the above range. As the polymerization initiator, a peroxide or an azo compound, which is a known radical polymerization initiator, is suitably used, and is appropriately determined according to the polymerization temperature. It is used in a proportion of 1.0% by weight.

【0024】本発明の重合方法では、分子量の調整に連
鎖移動剤を用いることができる。例えば、αメチルスチ
レンやメルカプタン系の連鎖移動剤を用いることができ
る。
In the polymerization method of the present invention, a chain transfer agent can be used for adjusting the molecular weight. For example, α-methylstyrene or a mercaptan-based chain transfer agent can be used.

【0025】本発明におけるマレイミド系共重合体
(1)の重合方法は、使用する単量体の供給方法に特別
な工夫をすることが好ましい。上記単量体(b)および
単量体(c)及び必要に応じて溶媒を反応器に供給後、
開始剤を加えて重合を開始すると共に残った単量体
(b)および単量体(c)と、(a)を予め混合するこ
となく連続的又は断続的に重合系中に供給しながら重合
反応を行い、全ての単量体を供給し終えてから0.5時
間以上反応を継続する事が最も好ましい。上記、N置換
マレイミド系単量体(a)の、重合開始前に予め反応系
に供給する量と、重合反応の開始後、連続的または断続
的に供給する量の比は、0−5/100−95重量%の
範囲の比が好ましく、0−1/100−99重量%の範
囲の比が更に好ましいが、全量を連続的または断続的に
供給する事が最も好ましい。
In the polymerization method of the maleimide-based copolymer (1) in the present invention, it is preferable to take special measures for the method of supplying the monomers to be used. After supplying the monomer (b) and the monomer (c) and a solvent as necessary to the reactor,
The polymerization is started by adding an initiator, and the remaining monomers (b) and (c) and (a) are continuously or intermittently fed into the polymerization system without prior mixing. It is most preferable to continue the reaction for 0.5 hour or more after the completion of the reaction and supply of all the monomers. The ratio of the amount of the N-substituted maleimide-based monomer (a) supplied to the reaction system before the start of the polymerization and the amount of the N-substituted maleimide monomer (a) supplied continuously or intermittently after the start of the polymerization reaction is 0-5 / A ratio in the range of 100-95% by weight is preferred, a ratio in the range of 0-1 / 100-99% by weight is more preferred, but it is most preferred to supply the whole amount continuously or intermittently.

【0026】上記、芳香族ビニル系単量体(b)の、重
合開始前に予め反応系に供給する量と、上記重合反応開
始後、連続的または断続的に供給する量の比は、1−9
9/99−1重量%範囲の比が好ましく、5−90/9
5−10重量%の範囲の比が更に好ましく、15−75
/85−25重量%の範囲の比が更に好ましく、30−
60/70−40重量%の範囲の比が最も好ましい。
The ratio of the amount of the aromatic vinyl monomer (b) supplied to the reaction system before the start of the polymerization and the amount supplied continuously or intermittently after the start of the polymerization reaction is 1 -9
A ratio in the range of 9 / 99-1% by weight is preferred, and 5-90 / 9
More preferred is a ratio in the range of 5-10% by weight, 15-75%.
More preferred is a ratio in the range of / 85-25% by weight,
Most preferred is a ratio in the range of 60 / 70-40% by weight.

【0027】上記、不飽和モノカルボン酸系単量体
(c)の、重合開始前に予め反応系に供給する量と、開
始後連続的または断続的に供給する量の比は、1−99
/99−1重量%の範囲の比が好ましく、10−90/
90−10重量%の範囲の比が更に好ましく、25−7
5/75−25重量%の範囲の比が更に好ましく、30
−70/70−30重量%の範囲の比が最も好ましい。
The ratio of the amount of the unsaturated monocarboxylic acid monomer (c) supplied to the reaction system before the start of the polymerization and the amount supplied continuously or intermittently after the start of the polymerization is 1-99.
A ratio in the range of 9 / 99-1% by weight is preferred.
More preferred is a ratio in the range of 90-10% by weight, 25-25% by weight.
More preferred is a ratio in the range of 5 / 75-25% by weight,
Most preferred is a ratio in the range of -70 / 70-30% by weight.

【0028】この重合方法を採用する事により、上記一
般式(1)で示される特定構造の化合物(2)の生成を
抑制することができ、アルカリ水溶液可溶能の低下を抑
制するとともに、得られるマレイミド系共重合体中に残
存するマレイミド単量体量を効果的に低減することが出
来る。N置換マレイミド系単量体と芳香族ビニル系単量
体を重合初期から設定量の全量が投入され重合を開始す
ると、重合初期に交互共重合体が優先的に生成し、その
後、残った不飽和カルボン酸系単量体の構造単位を多く
持つ重合体が生成するため、交互共重合体と、不飽和カ
ルボン酸系単量体由来の構造単位の多いマレイミド系共
重合体の混合物になる。その結果得られたマレイミド系
共重合体は、組成分布が非常に大きくなり、アルカリ可
溶能が低下する為好ましくない。さらに、N置換マレイ
ミド系単量体(a)と芳香族ビニル系単量体(b)を予
め重合系に仕込んで重合を開始すると、昇温中及び重合
中に、上記一般式(1)で示される特定構造の化合物
(2)が副生しやすくなる。
By adopting this polymerization method, it is possible to suppress the formation of the compound (2) having the specific structure represented by the above general formula (1), and to suppress the decrease in the solubility of the aqueous alkali solution, The amount of maleimide monomer remaining in the resulting maleimide-based copolymer can be effectively reduced. When the total amount of the N-substituted maleimide monomer and the aromatic vinyl monomer is charged from the initial stage of polymerization and the polymerization is started, an alternating copolymer is preferentially formed in the early stage of polymerization, and thereafter, the remaining copolymer is formed. Since a polymer having a large number of structural units of a saturated carboxylic acid-based monomer is produced, a mixture of an alternating copolymer and a maleimide-based copolymer having a large number of structural units derived from an unsaturated carboxylic acid-based monomer is obtained. The resulting maleimide-based copolymer has an undesirably high composition distribution and reduced alkali-solubility. Further, when the N-substituted maleimide-based monomer (a) and the aromatic vinyl-based monomer (b) are previously charged into the polymerization system and the polymerization is started, the above-mentioned general formula (1) The compound (2) having the specific structure shown is easily produced as a by-product.

【0029】また、全てのN置換マレイミド系単量体
(a)を供給し終えてから0.5時間以上、更に好まし
くは1時間以上重合反応を継続する事で、残存するN置
換マレイミド系単量体(a)を低減することが出来る。
またN置換マレイミド系単量体(a)は、使用する量の
90重量%以上を、好ましくは95重量%以上、更に好
ましくは全量を重合系に連続的または断続的に投入する
条件で重合反応をする必要がある。N置換マレイミド系
単量体(a)の初期仕込み量が、上記範囲以外の、10
重量%を超えた条件で重合を開始すると、芳香族ビニル
系単量体(b)とN置換マレイミド系単量体(a)の交
互共重合体の生成量が多くなり、アルカリ可溶能が低減
する恐れがあるからである。
Further, after the supply of all the N-substituted maleimide monomer (a) is completed, the polymerization reaction is continued for 0.5 hour or more, more preferably for 1 hour or more, so that the remaining N-substituted maleimide monomer can be obtained. The monomer (a) can be reduced.
The N-substituted maleimide-based monomer (a) is used in a polymerization reaction under the condition that 90% by weight or more, preferably 95% by weight or more, more preferably the entire amount of the N-substituted maleimide monomer (a) is continuously or intermittently charged into the polymerization system. Need to do. If the initial amount of the N-substituted maleimide-based monomer (a) is 10
When the polymerization is started under the condition of more than 10% by weight, the production amount of the alternating copolymer of the aromatic vinyl monomer (b) and the N-substituted maleimide monomer (a) increases, and the alkali-solubility increases. This is because there is a risk of reduction.

【0030】またN置換マレイミド系単量体(a)と芳
香族ビニル系単量体(b)は、混合せず別々に重合系に
供給することが望ましい。混合供給すると、混合液中で
上記一般式(1)で示される特定構造の化合物(2)が
副生しやすくなる。重合反応終了後の溶液から揮発分を
除去してマレイミド系共重合体(1)を分離する方法と
しては、真空下で加熱する方法、貧溶媒中に投入してマ
レイミド系共重合体(1)を沈殿させ、濾別する方法等
を採用することが出来るが、貧溶媒に投入して濾別する
方法は、設備が過大になり工業的には不向きである。よ
って真空下の加熱により溶剤及び残存モノマーを揮発除
去することが好ましい。また、必要に応じて揮発除去さ
れて溶剤及び残存モノマーは回収される設備を備えてい
る事が好ましい。上記の加熱溶媒回収設備としては、脱
揮槽での真空加熱、2軸押出機での脱溶媒などが好まし
く用いられる。また、脱揮槽で予め予備濃縮を行い、2
軸押出機で脱溶媒を完結させることも出来る。
It is desirable that the N-substituted maleimide monomer (a) and the aromatic vinyl monomer (b) are separately supplied to the polymerization system without being mixed. When mixed and supplied, the compound (2) having the specific structure represented by the general formula (1) is easily produced as a by-product in the mixed solution. As a method of removing the volatile component from the solution after the polymerization reaction and separating the maleimide-based copolymer (1), a method of heating under vacuum, or a method of charging the maleimide-based copolymer (1) by pouring it into a poor solvent Can be employed, and a method of filtering the solution by adding it to a poor solvent is not industrially suitable because the equipment is excessively large. Therefore, it is preferable to volatilize and remove the solvent and the residual monomer by heating under vacuum. Further, it is preferable to provide a facility for volatilizing and removing the solvent and the residual monomer as required. As the above heated solvent recovery equipment, vacuum heating in a devolatilization tank, desolvation in a twin screw extruder, or the like is preferably used. In addition, preconcentration is performed in advance in a devolatilization tank,
Desolvation can be completed by a screw extruder.

【0031】本発明で使用することのできるマレイミド
系共重合体(1)は、N置換マレイミド系単量体(a)
以外の単量体成分、溶剤分などの残存する揮発分が2000
ppm以下、好ましくは1000ppm以下、更に好ましくは500p
pm以下である。残存揮発分が多いと、熱安定性が低下し
たり着色の原因となるため好ましくない。また、本発明
のマレイミド系共重合体(1)は、さらに好ましくは、
残存するN置換マレイミド系単量体(a)の含有量が特
定量以下である事が好ましい。具体的には、N置換マレ
イミド系単量体(a)の含有量としては、500ppm以下が
好ましく、より好ましくは、200ppm以下である。さらに
好ましくは、100ppm以下である。
The maleimide copolymer (1) which can be used in the present invention is an N-substituted maleimide monomer (a)
The remaining volatile components such as monomer components and solvents other than 2000
ppm or less, preferably 1000 ppm or less, more preferably 500p
pm or less. It is not preferable that the residual volatile matter is large because heat stability is reduced or coloring is caused. Further, the maleimide-based copolymer (1) of the present invention is more preferably
It is preferable that the content of the remaining N-substituted maleimide-based monomer (a) is not more than a specific amount. Specifically, the content of the N-substituted maleimide-based monomer (a) is preferably 500 ppm or less, more preferably 200 ppm or less. More preferably, it is 100 ppm or less.

【0032】本発明のマレイミド系共重合体(1)は、
他の熱可塑性樹脂である、ABS樹脂、AS樹脂、ポリ
スチレン、アクリル樹脂、塩化ビニル樹脂、ポリアミ
ド、ポリエステル、PPE樹脂、ポリエーテルサルファ
イド樹脂およびPBT樹脂から選択される1以上の樹脂と
配合して用いてもよい。さらに、不飽和ポリエステル系
アルキッド樹脂、エポキシ樹脂、ウレタン樹脂、ビスマ
レイミド/多官能アミン硬化系などの熱硬化樹脂を配合
してもよい。さらに、ガラス繊維、カーボンブラック、
タルク、クレイ、炭酸カルシウム、炭酸マグネシウムな
どの無機充填剤、ハロゲン系及び/またはリン系の難燃
剤、ステアリン酸塩等の成形助剤、紫外線吸収剤、酸化
防止剤、帯電防止剤、染料および/または顔料等の着色
剤、発泡剤などの各種添加剤を、使用目的に応じて添加
することが出来る。これらの添加量は、目的に応じて適
宜設定する事が可能であり、一般文献等の公知の使用量
を採用することができる。また、本発明のマレイミド系
共重合体(1)は、特定の単量体成分を用いて重合さ
せ、特定の物性を保有しているので、耐熱性や強度と併
せて良好なアルカリ水溶液可溶能を有している。そのた
め、各種カバーフィルム、コーテイング膜、基材保護マ
スク、保護用フィルム、被覆材として用いた後、アルカ
リ水溶液で容易にそのフィルムやカバーや被覆材を除去
することができる。また、本発明のフィルム等の使用形
態、用途、適応出来る分野は特に限定されるものではな
く、アルカリ水溶液可溶性と耐熱性、熱安定性が必要な
分野において使用することが出来る。
The maleimide copolymer (1) of the present invention comprises:
Used in combination with one or more resins selected from other thermoplastic resins such as ABS resin, AS resin, polystyrene, acrylic resin, vinyl chloride resin, polyamide, polyester, PPE resin, polyether sulfide resin and PBT resin You may. Further, a thermosetting resin such as an unsaturated polyester alkyd resin, an epoxy resin, a urethane resin, and a bismaleimide / polyfunctional amine curing system may be blended. In addition, glass fiber, carbon black,
Inorganic fillers such as talc, clay, calcium carbonate, and magnesium carbonate, halogen-based and / or phosphorus-based flame retardants, molding aids such as stearates, ultraviolet absorbers, antioxidants, antistatic agents, dyes and / or Alternatively, various additives such as a coloring agent such as a pigment and a foaming agent can be added according to the purpose of use. The amounts of these additives can be appropriately set according to the purpose, and known amounts such as general literatures can be employed. In addition, the maleimide-based copolymer (1) of the present invention is polymerized using a specific monomer component and has specific physical properties. Has ability. Therefore, after using as a cover film, a coating film, a base material protection mask, a protection film, and a coating material, the film, the cover, and the coating material can be easily removed with an alkaline aqueous solution. Further, the use form, application, and applicable field of the film etc. of the present invention are not particularly limited, and the film can be used in an area requiring alkali aqueous solution solubility, heat resistance and thermal stability.

【0033】また、本発明のマレイミド系共重合体
(1)からなるフィルムや被覆材等がカバーする基材の
材質も特に限定されない。例えば、各種金属、銅、鉄、
およびプラスチック材等、特に限定されるものではな
い。その被覆方法やコート方法も特に限定されるもので
はなく、例えば、本発明のマレイミド系共重合体(1)
をコーター等で、薄い膜等に成形しコートしてもよい。
また、キャストフィルムに成形して、対象物を被覆して
もよい。また、基材に直接塗布してもよい。塗布や被覆
やコートの各種方法に適応できる様に、必要に応じ、溶
媒等に本発明のマレイミド系共重合体(1)を溶解さ
せ、塗布、コート後、その溶媒を飛散させ、膜状態、フ
ィルム状態にする事ができる。
Further, the material of the base material covered by the film or the coating material made of the maleimide copolymer (1) of the present invention is not particularly limited. For example, various metals, copper, iron,
It is not particularly limited, such as plastic materials. The coating method and the coating method are not particularly limited either. For example, the maleimide-based copolymer (1) of the present invention
May be formed into a thin film or the like with a coater or the like and coated.
Moreover, you may shape | mold into a cast film and cover an object. Moreover, you may apply directly to a base material. If necessary, the maleimide copolymer (1) of the present invention is dissolved in a solvent or the like so that it can be applied to various methods of coating, coating, and coating. It can be made into a film.

【0034】また、本発明のマレイミド系共重合体
(1)のカルボキシル基に、カルボキシル基と反応する
事ができる官能基を持つ化合物を反応させて、本発明の
マレイミド系共重合体に各種機能を持たせる事もでき
る。この場合、本発明のマレイミド系共重合体のアルカ
リ水への溶解性に支障のない範囲で、その変性量や、変
性する化合物を選択する事ができる。上記のカルボキシ
ル基と反応する事ができる官能基を持つ化合物として
は、エポキシ化合物や、カルボキシル基とエステル交換
で反応する官能基を持つ化合物や、各種アミンが例示さ
れる。例えば、アミンを反応させればアミドエステル構
造を本発明のマレイミド系共重合体(1)に導入する事
ができるが、特に限定されるものではない。
The carboxyl group of the maleimide-based copolymer (1) of the present invention is reacted with a compound having a functional group capable of reacting with the carboxyl group to give various functions to the maleimide-based copolymer of the present invention. You can also have In this case, the modification amount and the compound to be modified can be selected as long as the solubility of the maleimide copolymer of the present invention in alkaline water is not hindered. Examples of the compound having a functional group that can react with the carboxyl group include an epoxy compound, a compound having a functional group that reacts with the carboxyl group by transesterification, and various amines. For example, if an amine is reacted, an amide ester structure can be introduced into the maleimide copolymer (1) of the present invention, but is not particularly limited.

【0035】[0035]

【実施例】以下、実施例により本発明を詳細に説明する
が、本発明の範囲はこれらの実施例によって限定される
ものではない。
EXAMPLES The present invention will be described below in detail with reference to examples, but the scope of the present invention is not limited by these examples.

【0036】本発明における、マレイミド系共重合体
の、芳香族ビニル系単量体単位、N置換マレイミド系単
量体単位の含有量は、元素分析法及びNMRから求め
た。また、マレイミド系共重合体中の残存揮発分、残存
マレイミド系単量体量は、ガスクロマトグラフィーによ
り測定した。また、重量平均分子量(Mw)や数平均分子量
(Mn)は、テトラヒドロフランを溶媒に用いたゲルパーミ
エーションクロマトグラフィの溶出曲線からポリスチレ
ンの標準重合体を規準として算出した。
In the present invention, the contents of the aromatic vinyl monomer unit and the N-substituted maleimide monomer unit in the maleimide copolymer were determined by elemental analysis and NMR. Further, the remaining volatile components and the amount of the remaining maleimide-based monomer in the maleimide-based copolymer were measured by gas chromatography. Also, weight average molecular weight (Mw) and number average molecular weight
(Mn) was calculated from an elution curve of gel permeation chromatography using tetrahydrofuran as a solvent, using a standard polymer of polystyrene as a standard.

【0037】マレイミド系共重合体中の、一般式(1)
で示される特定構造の化合物(2)は、ゲルパーミエー
ションクロマトグラフィ(GPC)測定での面積比から含
有量を求めた。また、GPCにより特定構造の化合物を分
取し、質量分析であるMASSスペクトル、IRスペクトル、
1H−NMRおよび13C−NMRスペクトルでその構造を確認し
た。
Formula (1) in the maleimide-based copolymer
The content of the compound (2) having a specific structure represented by is determined from the area ratio measured by gel permeation chromatography (GPC). In addition, a compound having a specific structure is fractionated by GPC, and MASS spectrum, IR spectrum,
Its structure was confirmed by 1 H-NMR and 13 C-NMR spectra.

【0038】上記のNMR分析は、重水素化クロロホル
ム(CDCl3)中でテトラメチルシランを標準物質と
して測定を行い、1H−NMRスペクトルおよび13C−NM
Rスペクトルを得た。使用したNMR装置は、VXR−
300S(バリアン株式会社製)であった。IR分析
は、臭化カリウム錠剤法により赤外分析装置(FT/IR-
3、島津製作所株式会社製)を用いて行った。質量分析
は、M-2000A質量分析装置(日立製作所株式会社製)を
用いて行った。
In the above NMR analysis, measurement was carried out in deuterated chloroform (CDCl 3 ) using tetramethylsilane as a standard substance, and 1 H-NMR spectrum and 13 C-NM
An R spectrum was obtained. The NMR apparatus used was VXR-
300S (manufactured by Varian Inc.). IR analysis is performed by an infrared analyzer (FT / IR-
3, Shimadzu Corporation). Mass spectrometry was performed using an M-2000A mass spectrometer (manufactured by Hitachi, Ltd.).

【0039】本発明の、マレイミド系共重合体のアルカ
リ水溶液可溶能は、以下の様に測定した。すなわち、共
重合体をMIBKに溶解し、ダイコーターを用いてガラ
ス板上に塗布後乾燥して、50μmのフィルムを作成
し、ガラス板から剥離後、一片10cmの正方形に切断
し、0.5%−KOH水溶液200mlに浸して、50
℃において1時間攪拌するという操作により重合体のア
ルカリ水溶液溶解性を測定した。また不溶物が認められ
る場合、濾別した不純物を乾燥させてその重量を測定
し、溶解前の上記フィルムの重量と比較し、アルカリ不
溶分の含有量を求めた。また、上記フィルムが溶解した
場合は、不溶分は0とした。
The solubility of the maleimide-based copolymer of the present invention in an aqueous alkali solution was measured as follows. That is, the copolymer was dissolved in MIBK, applied on a glass plate using a die coater, and dried to form a 50 μm film. After peeling off the glass plate, the film was cut into a 10 cm square, % -KOH aqueous solution
The solubility of the polymer in an aqueous alkali solution was measured by an operation of stirring at 1 ° C. for 1 hour. When an insoluble matter was found, the impurities separated by filtration were dried, the weight was measured, and the weight was compared with the weight of the film before dissolution to determine the content of alkali-insoluble components. When the film was dissolved, the insoluble content was set to 0.

【0040】マレイミド系共重合体のガラス転移点(T
g)は、DSCにより中点法で測定を行った。すなわ
ち、理学電気株式会社製のDSC-8230を用い、窒素気流
下、α−アルミナをリファレンスとして昇温速度5℃/
分で測定したDSC曲線から算出した。
The glass transition point of the maleimide-based copolymer (T
g) was measured by the midpoint method by DSC. That is, using a DSC-8230 manufactured by Rigaku Denki Co., Ltd., under a nitrogen gas flow, using α-alumina as a reference, the temperature rising rate was 5 ° C. /
Calculated from the DSC curve measured in minutes.

【0041】<実施例1>2Lフラスコを窒素置換し、
スチレン8部、メタクリル酸3部、メチルイソブチルケ
トン(MIBK)53部、αメチルスチレンダイマー
1.0部を仕込み、重合系を110℃に昇温しMIBK
が還流を開始した後、開始剤であるt-ブチルパーオキシ
イソプロピルカーボネート0.003部を添加し重合を
開始するとともに、滴下系(A)としてスチレン8部
と、メタクリル酸2部、t-ブチルパーオキシイソプロピ
ルカーボネート0.003部を、滴下系(B)としてN-シ
クロヘキシルマレイミド(CHMI)13部をMIBK
13部で、60℃で溶解したものを3時間かけて連続的
に供給し、さらに2時間重合を継続した。その重合液を
MIBKで希釈した後、ヘキサン中に注いで沈殿析出品
としてマレイミド系共重合体(1−1)を得た。得られ
たマレイミド系共重合体(1−1)の物性を表1に示
す。
<Example 1> A 2 L flask was purged with nitrogen.
8 parts of styrene, 3 parts of methacrylic acid, 53 parts of methyl isobutyl ketone (MIBK), and 1.0 part of α-methylstyrene dimer were charged, and the temperature of the polymerization system was raised to 110 ° C. to obtain MIBK.
Starts refluxing, 0.003 part of t-butylperoxyisopropyl carbonate as an initiator is added to initiate polymerization, and 8 parts of styrene, 2 parts of methacrylic acid, and t-butyl 0.003 parts of peroxyisopropyl carbonate was added dropwise to 13 parts of N-cyclohexylmaleimide (CHMI) as MIBK as MIBK.
In 13 parts, the solution dissolved at 60 ° C. was continuously supplied over 3 hours, and the polymerization was further continued for 2 hours. After diluting the polymerization solution with MIBK, it was poured into hexane to obtain a maleimide-based copolymer (1-1) as a precipitate. Table 1 shows the physical properties of the obtained maleimide-based copolymer (1-1).

【0042】<実施例2>初期仕込分のスチレンを6.
5部、メタクリル酸5部、滴下系のスチレンを6.5
部、メタクリル酸を6部、CHMIを10部に変更した
以外は製造例1と同様の操作を行い、その重合液をMI
BKで希釈した後、ヘキサン中に注いで沈殿析出品とし
てマレイミド系共重合体(1−2)を得た。得られたマ
レイミド系共重合体(1−2)の物性を表1に示す。
<Example 2> The initial charge of styrene was 6.
5 parts, methacrylic acid 5 parts, 6.5 drops of styrene
Parts, methacrylic acid was changed to 6 parts, and CHMI was changed to 10 parts, and the same operation as in Production Example 1 was performed.
After dilution with BK, the mixture was poured into hexane to obtain a maleimide copolymer (1-2) as a precipitate. Table 1 shows the physical properties of the obtained maleimide-based copolymer (1-2).

【0043】<実施例3>CHMIのかわりに、N−フ
ェニルマレイミドを使用した以外は製造例2と同じ操作
を行い、その重合液をMIBKで希釈した後、ヘキサン
中に注いで沈殿析出品としてマレイミド系共重合体(1
−3)を得た。得られたマレイミド系共重合体(1−
3)の物性を表1に示す。
Example 3 The same operation as in Production Example 2 was carried out except that N-phenylmaleimide was used instead of CHMI. The polymerization solution was diluted with MIBK, and then poured into hexane to obtain a precipitate. Maleimide copolymer (1
-3) was obtained. The obtained maleimide-based copolymer (1-
Table 1 shows the physical properties of 3).

【0044】<比較例1>2Lフラスコを窒素置換し、
メチルイソブチルケトン(MIBK)53部、αメチル
スチレンダイマー1.0部を仕込み、重合系を110℃
に昇温しMIBKが還流を開始した後、開始剤であるt-
ブチルパーオキシイソプロピルカーボネート0.004
3部を添加するとともに、滴下系(A)としてt-ブチルパ
ーオキシイソプロピルカーボネート0.0043部とM
IBK5部を、滴下系(B)としてスチレン13部と、メ
タクリル酸11部、N-シクロヘキシルマレイミド(CH
MI)13部をMIBK8部で、60℃で溶解したもの
を3時間かけて連続的に供給し、さらに2時間重合を継
続した。その重合液をMIBKで希釈した後、ヘキサン
中に注いで沈殿析出品としてマレイミド系共重合体(1
−4)を得た。得られたマレイミド系共重合体(1−
4)の物性を表1に示す。
<Comparative Example 1> A 2 L flask was purged with nitrogen.
53 parts of methyl isobutyl ketone (MIBK) and 1.0 part of α-methylstyrene dimer were charged, and the polymerization system was heated to 110 ° C.
And the MIBK starts refluxing, and then the initiator t-
Butyl peroxyisopropyl carbonate 0.004
3 parts and 0.0043 part of t-butyl peroxyisopropyl carbonate and M
13 parts of styrene, 11 parts of methacrylic acid, N-cyclohexylmaleimide (CH
MI) 13 parts were dissolved in MIBK 8 parts at 60 ° C. and continuously supplied over 3 hours, and the polymerization was further continued for 2 hours. After diluting the polymerization solution with MIBK, the mixture was poured into hexane to precipitate the maleimide-based copolymer (1
-4) was obtained. The obtained maleimide-based copolymer (1-
Table 1 shows the physical properties of 4).

【0045】<実施例4>実施例2で得られた重合液
を、MIBKで希釈せずに、脱揮装置であるベント付き
2軸押し出し機に導入し、減圧下、180℃で脱揮し、
押し出し機でマレイミド系共重合体を押し出し、得られ
たストランドを粉砕して、マレイミド系共重合体(1−
5)を得た。得られたマレイミド系共重合体(1−5)
の物性を表1に示す。
Example 4 The polymerization solution obtained in Example 2 was introduced into a twin-screw extruder equipped with a vent as a devolatilizer without dilution with MIBK, and devolatilized at 180 ° C. under reduced pressure. ,
The maleimide-based copolymer was extruded with an extruder, and the obtained strand was pulverized to obtain a maleimide-based copolymer (1-
5) was obtained. The obtained maleimide-based copolymer (1-5)
Table 1 shows the physical properties of the compound.

【0046】<実施例5>初期仕込分のスチレンを7.
5部、メタクリル酸10部、滴下系のスチレンを7.5
部、メタクリル酸を10部、CHMIを15部に変更し
た以外は製造例1と同様の操作を行い、マレイミド系共
重合体(1−6)を得た。得られたマレイミド系共重合
体(1−6)の物性を表1に示す。なお表中の残存揮発
分は、マレイミド系単量体以外の残存する単量体及び溶
媒の合計量である。
<Example 5> The initial charge of styrene was 7.
5 parts, 10 parts of methacrylic acid, 7.5 drops of styrene
Parts, methacrylic acid was changed to 10 parts and CHMI was changed to 15 parts, and the same operation as in Production Example 1 was performed to obtain a maleimide copolymer (1-6). Table 1 shows the physical properties of the obtained maleimide copolymer (1-6). In addition, the residual volatile matter in the table is the total amount of the remaining monomer and the solvent other than the maleimide-based monomer.

【0047】[0047]

【表1】 [Table 1]

【0048】<参考例>実施例2で得られたマレイミド
系共重合体(1−2)をセロソルブアセテートに溶解
し、ガラス板上にダイコーターを用いて塗布後、2日間
自然乾燥し更に120℃で2時間乾燥することにより、
膜厚50μmのフィルムを得た。本フィルムは、無色透
明で、240℃1時間オーブン中で放置しても変色等の
問題はなかった。また、本参考例におけるフィルムも、
上記実施例と同様な条件で、アルカリ水溶液可溶能テス
トを行い、アルカリ不溶分が0である事を確認した。
Reference Example The maleimide-based copolymer (1-2) obtained in Example 2 was dissolved in cellosolve acetate, applied on a glass plate using a die coater, dried naturally for 2 days, and dried for 120 days. By drying at ℃ for 2 hours,
A film having a thickness of 50 μm was obtained. This film was colorless and transparent, and had no problem such as discoloration even when left in an oven at 240 ° C. for 1 hour. Also, the film in this reference example,
An alkali aqueous solution solubility test was performed under the same conditions as in the above example, and it was confirmed that the alkali insoluble content was 0.

【0049】[0049]

【発明の効果】本発明は、 N置換マレイミド系単量体
、芳香族ビニル系単量体および不飽和モノカルボン酸
系単量体を含む単量体成分を重合してなるマレイミド系
共重合体において、単量体成分の供給方法を工夫するこ
とで、 N置換マレイミド系単量体と芳香族ビニル系単量
体からなる3量体の含有量が少なく、また組成分布が少
ない為、アルカリ水溶液可溶能に優れたマレイミド系共
重合体組成物を得ることができる。
The present invention provides a maleimide copolymer obtained by polymerizing monomer components including an N-substituted maleimide monomer, an aromatic vinyl monomer and an unsaturated monocarboxylic acid monomer. By devising the supply method of the monomer component, the content of the trimer composed of the N-substituted maleimide monomer and the aromatic vinyl monomer is small, and the composition distribution is small. A maleimide-based copolymer composition having excellent solubility can be obtained.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 山口 稔 大阪府吹田市西御旅町5番8号 株式会社 日本触媒内 Fターム(参考) 4J011 BB01 BB07 BB08 BB15 BB17 4J100 AB02Q AB03Q AB04Q AB08Q AJ02R AM45P AM47P AM48P AM49P BB01P BC04P BC43P BC49P CA05 DA01 FA19 FA35  ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Minoru Yamaguchi 5-8 Nishiburi-cho, Suita-shi, Osaka Nippon Shokubai Co., Ltd. F-term (reference) 4J011 BB01 BB07 BB08 BB15 BB17 4J100 AB02Q AB03Q AB04Q AB08Q AJ02R AM45P AM47P AM48P AM49P BB01P BC04P BC43P BC49P CA05 DA01 FA19 FA35

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】N置換マレイミド系単量体(a)10〜8
0重量%、芳香族ビニル系単量体(b)10〜80重量
%および不飽和モノカルボン酸系単量体(c)1〜70
重量%を含む単量体成分を重合してなるマレイミド系共
重合体であって、アルカリ水溶液不溶分が10重量%以
下である事を特徴とするマレイミド系共重合体(1)。
1. An N-substituted maleimide monomer (a) 10 to 8
0% by weight, 10 to 80% by weight of an aromatic vinyl monomer (b) and 1 to 70% of an unsaturated monocarboxylic acid monomer (c)
A maleimide-based copolymer obtained by polymerizing a monomer component containing 1% by weight of a maleimide-based copolymer, wherein an insoluble content of an aqueous alkali solution is 10% by weight or less.
【請求項2】N置換マレイミド系単量体(a)10〜8
0重量%、芳香族ビニル系単量体(b)10〜80重量
%および不飽和モノカルボン酸系単量体(c)1〜70
重量%を含む単量体成分を重合してなるマレイミド系共
重合体であって、下記一般式(1)で示される特定構造
の化合物(2)の含有量が10重量%以下である事を特
徴とするマレイミド系共重合体(1)。 【化1】 (但し上記一般式(1)において、R1は互いに独立し
てアルキル基、シクロアルキル基、アリール基、アルキ
ル置換アリール基またはハロゲン置換アリール基を表
し;R2は水素またはメチル基を表し;R3〜R6はそれ
ぞれ独立に水素、アルキル基、シクロアルキル基、シク
ロアルキル基、アリール基、アルキル置換アリール基ま
たはハロゲン置換アリール基を表す。)
2. N-substituted maleimide monomers (a) 10 to 8
0% by weight, 10 to 80% by weight of an aromatic vinyl monomer (b) and 1 to 70% of an unsaturated monocarboxylic acid monomer (c)
A maleimide-based copolymer obtained by polymerizing a monomer component containing 1% by weight, wherein the content of the compound (2) having a specific structure represented by the following general formula (1) is 10% by weight or less. Characterized maleimide-based copolymer (1). Embedded image (However, in the general formula (1), R 1 independently represents an alkyl group, a cycloalkyl group, an aryl group, an alkyl-substituted aryl group or a halogen-substituted aryl group; R 2 represents hydrogen or a methyl group; 3 to R 6 each independently represent hydrogen, an alkyl group, a cycloalkyl group, a cycloalkyl group, an aryl group, an alkyl-substituted aryl group or a halogen-substituted aryl group.
【請求項3】N置換マレイミド系単量体(a)10〜8
0重量%、芳香族ビニル系単量体(b)10〜80重量
%および不飽和モノカルボン酸系単量体(c)1〜70
重量%を含む単量体成分を重合してなるマレイミド系共
重合体(1)を製造する方法において、単量体(b)お
よび単量体(c)及び必要に応じて溶剤を反応器に供給
後、重合を開始するとともに残った単量体(b)および
単量体(c)と、単量体(a)を連続的又は断続的に重
合系中に供給しながら重合反応を行うことを特徴とする
マレイミド系共重合体の製造方法。
3. N-substituted maleimide monomers (a) 10 to 8
0% by weight, 10 to 80% by weight of an aromatic vinyl monomer (b) and 1 to 70% of an unsaturated monocarboxylic acid monomer (c)
In a method for producing a maleimide-based copolymer (1) obtained by polymerizing a monomer component containing 1% by weight, a monomer (b) and a monomer (c) and, if necessary, a solvent are added to a reactor. After the supply, the polymerization is started while the remaining monomer (b) and monomer (c) and the monomer (a) are continuously or intermittently fed into the polymerization system. A method for producing a maleimide-based copolymer, characterized in that:
【請求項4】単量体(b)および単量体(c)及び必要
に応じて溶剤を反応器に供給後、重合を開始するととも
に残った単量体(b)および単量体(c)と、単量体
(a)を連続的又は断続的に重合系中に供給しながら重
合反応を行う際に、単量体(a)と単量体(b)は予め
混合することなく供給することを特徴とする請求項3記
載のマレイミド系共重合体の製造方法。
4. After supplying the monomers (b) and (c) and, if necessary, a solvent to the reactor, polymerization is started and the remaining monomers (b) and (c) ) And the monomer (a) and the monomer (b) are supplied without prior mixing during the polymerization reaction while the monomer (a) is continuously or intermittently supplied into the polymerization system. The method for producing a maleimide-based copolymer according to claim 3, wherein
JP2000213684A 2000-07-14 2000-07-14 Maleimide copolymer and method for producing the same Pending JP2002030119A (en)

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Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010103956A1 (en) * 2009-03-09 2010-09-16 昭和電工株式会社 Material for organic light-emitting element, organic light-emitting element, and process for producing the organic light-emitting element
JP2016186024A (en) * 2015-03-27 2016-10-27 株式会社日本触媒 Production method of alkali-soluble resin and photosensitive resin composition comprising alkali-soluble resin produced by the production method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010103956A1 (en) * 2009-03-09 2010-09-16 昭和電工株式会社 Material for organic light-emitting element, organic light-emitting element, and process for producing the organic light-emitting element
JP2016186024A (en) * 2015-03-27 2016-10-27 株式会社日本触媒 Production method of alkali-soluble resin and photosensitive resin composition comprising alkali-soluble resin produced by the production method

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