JPS58201814A - Synthesis of novel copolymer - Google Patents

Synthesis of novel copolymer

Info

Publication number
JPS58201814A
JPS58201814A JP8330782A JP8330782A JPS58201814A JP S58201814 A JPS58201814 A JP S58201814A JP 8330782 A JP8330782 A JP 8330782A JP 8330782 A JP8330782 A JP 8330782A JP S58201814 A JPS58201814 A JP S58201814A
Authority
JP
Japan
Prior art keywords
polymerization
methyl
polymer
fumarate
diester
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
JP8330782A
Other languages
Japanese (ja)
Inventor
Takayuki Otsu
大津 隆行
Takashige Murata
村田 敬重
Yasuyoshi Koinuma
康美 鯉沼
Toshihisa Takeuchi
竹内 利久
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
NOF Corp
Original Assignee
NOF Corp
Nippon Oil and Fats Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by NOF Corp, Nippon Oil and Fats Co Ltd filed Critical NOF Corp
Priority to JP8330782A priority Critical patent/JPS58201814A/en
Publication of JPS58201814A publication Critical patent/JPS58201814A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain a copolymer capable of regulating easily the introduction ratio and position of a functional group, by polymerizing a compound containing an unsaturated double bond with a fumaric dialkyl ester having a specific molecular structure. CONSTITUTION:A compound containing a polymerizable unsaturated double bond is polymerized with an unsymmetrical fumaric dialkyl ester (e.g., fumaric acid methyl t-butyl diester, etc.) shown by the formula (X and Y are alkyl and one or more are bulky branched alkyl) in the presence of a polymerization initiator.

Description

【発明の詳細な説明】 本発明は、重合体中に官能基を導入するために、ジカル
ボン酸ジエステルを共重合させる方法に関する〇 さらに詳しくは不飽和二重結合を有し1金性能をもつ化
合物を原料として種々のラジカル重合開始剤を用い重合
させる際に、当該化合物と7マル酸ジフルキルエステル
とを共1台させることにより特異な優れた性能を有する
共重合体を製造する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method of copolymerizing diester dicarboxylic acid in order to introduce a functional group into a polymer. This invention relates to a method for producing a copolymer having unique and excellent performance by combining the compound and difurkyl heptalate in one unit when polymerizing the compound using various radical polymerization initiators as a raw material.

従来より、1台可能な不飽和二重納金を有する化合物と
して例えば、エチレン、ブーピレン、イア ソプチレン、1−プfン、塩化ビニル、スチレン、アク
!Ip+二)!Jル等の化合物が実用に供されており、
それらの重合方法および共重合法は数多く知られている
0これらの重合物はそのまま種々の製品として用いられ
る他に、他の有機化合物、無機化合物もしくはそれらの
複合物、例えばラミネート、エマルジョン等の形で生産
され利用されている。
Conventionally, examples of compounds having single unsaturated double deposits include ethylene, boopylene, isoptylene, 1-propylene, vinyl chloride, styrene, and Aku! Ip+2)! Compounds such as Jru are in practical use,
Many polymerization and copolymerization methods are known. In addition to being used as they are in various products, these polymers can also be used with other organic compounds, inorganic compounds, or composites thereof, such as in the form of laminates, emulsions, etc. is produced and used.

しかし、これらの重合物、特に単独重合物はそれらの有
する長所と共に多くの性能上の欠点を有している。例え
ば、ポリエチレン、ポリプルピレンなどのポリオレフィ
ン類では共通の性質として毘分子鎖中に反応性を有する
官能基が存在しないため、成形品、フィルム、ラミネー
トなどの製品化工程において、染色加工、接着加工、あ
るいは他の有機化合物、無機化合物、ならびにそれらの
複合物との混合加工を不可能または困難にしている◎他
の重合物、例えばポリスチレン、ポリ塩化ビニル等につ
いても染色性、接着性、等の点で改良されるべき点が多
い。
However, these polymers, especially homopolymers, have many performance drawbacks along with their advantages. For example, polyolefins such as polyethylene and polypropylene have a common property that they do not have reactive functional groups in their molecular chains. This makes mixing processing with other organic compounds, inorganic compounds, and their composites impossible or difficult. ◎ Other polymers, such as polystyrene and polyvinyl chloride, also have problems in terms of dyeability, adhesion, etc. There are many points that should be improved.

一般に、この様な欠点を改善するため多くの技術が公開
されており、例えばポリオレフィン、置換ポリオレフィ
ン類の重合に際し、重金物に反応性を持たせる為特定の
官能基を有しべ重合性能を持つ化合物を添加し、該オレ
フィン類と〆適当な重合方法により共重合させ鍵る方法
などがあげられる。
In general, many techniques have been published to improve these drawbacks. For example, in the polymerization of polyolefins and substituted polyolefins, in order to make them reactive to heavy metals, they have a specific functional group and have polymerization performance. Examples include a method in which a compound is added and then copolymerized with the olefin by an appropriate polymerization method.

しかし、これらの公知の方法を応用する場合には、添加
された適当な官能基を有し重合性能を持つ化合物が、本
来のポリオンフィンの有する長所を低下させずに同時に
望ましい性能を付与することが要求される。
However, when applying these known methods, it is necessary to ensure that the added compound having a suitable functional group and polymerization performance simultaneously imparts desired performance without reducing the advantages of the original polyion fin. is required.

この添加物としてはカルボン酸、カルボン酸エステル等
の不飽和化合物がよく知られておシ、例えばアクリル酸
、アクリル酸エステル類、メタクリル酸、メタクリル酸
−エステル類、酢酸ビニル等のビニルエステル しかし、これらの添加物は該オレフィンに対する1合反
応性の点で必ずしも好ましいものでない。
Unsaturated compounds such as carboxylic acids and carboxylic esters are well known as such additives, such as acrylic acid, acrylic esters, methacrylic acid, methacrylic acid-esters, and vinyl esters such as vinyl acetate. These additives are not necessarily preferable in terms of single-component reactivity with the olefin.

例えば、エチレン、プロピレンの重合に際してアクリル
酸、メタクリル酸、あるいはそれらのエステル類を添加
した場合、その添加物の単独重金性が大きすぎて生成共
重合体中に好ましい位置,割合で添加した化合物の官能
基を導入させることは困難でちる。
For example, when acrylic acid, methacrylic acid, or their esters are added during the polymerization of ethylene or propylene, the monoheavy metal properties of the additives are too large and the compound added at the desired position and ratio in the resulting copolymer is It is difficult to introduce functional groups.

また、最初に適当な重合方法でポリオレフィン類を合成
しておき.後に官能基を有する添加物を添加猿適当な方
法で該ポリオレフィンに付加させる方法もよく用いられ
るが、これには、重合性能ノ比較的低い無水マレイン酸
,フマル酸,マレイン酸エステル類.フマル酸エステル
類が使用される。
Also, first synthesize polyolefins using an appropriate polymerization method. A method in which an additive having a functional group is subsequently added to the polyolefin by an appropriate method is also often used, but this method involves the use of maleic anhydride, fumaric acid, maleic acid esters, etc., which have relatively low polymerization performance. Fumaric acid esters are used.

ジャーナル オン ポリマーサイエンス( Journ
al of Polymer science ) A
 − 1第5巻。
Journal on Polymer Science
al of Polymer science) A
- 1 Volume 5.

1539頁にはポリエチレンと無水マレイン酸の付加反
応例が.また工業イヒ学雑誌71巻7432Nにはポリ
プロピレンと無水マレイン酸の付加反応等の例が見られ
るが、官能基を有する添加物の好ましい導入割合や位置
の調節は困難であることがわかる。
On page 1539 there is an example of addition reaction between polyethylene and maleic anhydride. In addition, an example of an addition reaction between polypropylene and maleic anhydride is found in Kogyo Ihigaku Zasshi Vol. 71, 7432N, but it is clear that it is difficult to adjust the preferred introduction ratio and position of additives having functional groups.

本発明者らはこれら従来法の欠点を改善すべく鋭意検討
した結果、官能基を有する重合可能な添加物として、特
定の分子構造をもつフマル酸ジアルキルエステルを用い
ることにより、種々の化合物との共重合体を容易に合成
することができ、しかも官能基の導入割合や位置の調節
も容易であることを見出し、本発明を完成した。
The present inventors conducted intensive studies to improve the shortcomings of these conventional methods, and found that by using a fumaric acid dialkyl ester with a specific molecular structure as a polymerizable additive with a functional group, it was possible to combine it with various compounds. The present invention was completed based on the discovery that a copolymer can be easily synthesized and that the introduction ratio and position of functional groups can also be easily adjusted.

本発明は、重合可能な不飽和二重結合を有する化合物を
重合させる際に、少くとも1個のかさ高い分校アルキル
基をもつ非対称の7マル酸ジアルキルエステルを用いる
ことを特徴とする共重合体の合成法に関するものである
The present invention provides a copolymer characterized in that an asymmetric heptalic acid dialkyl ester having at least one bulky branched alkyl group is used when polymerizing a compound having a polymerizable unsaturated double bond. It concerns the synthesis method of

本発明に用いる重合可能な不飽和二重結合を有する化合
物としては、例えばエチレン、プロピレン、インブチレ
ン、1−ブテン、1−ペンテン。
Examples of the compound having a polymerizable unsaturated double bond used in the present invention include ethylene, propylene, imbutylene, 1-butene, and 1-pentene.

l−ヘキセン、等のオレフィン炭化水素.ブタジェン、
イソプレン等のジオレフィン炭化水素,塩化ビニル、ク
ロロプレン等の塩素化メレフィンまたはジオレフィン炭
化水素,シクロヘキセン、シクqペンタジェン、ビニル
シクロヘキセン等の環状オレフィン捷たはジオレフィン
、7ラン、ビニルピリジン、ビニルカルバゾール等の炭
素−炭素5− 二重結合を含む複素環式化合物,スチレン、α−メチル
スチレン、ジビニルベンゼン、等ノビニルア 基を含む芳香族化合物.ビニルlンスシセン,ビニルフ
ェナンスレン等のビニル基を含む給金環系芳香族化合物
,アクリル酸,フマル酸,メタクリル酸,等の不飽和カ
ルボン酸,アルクル酸メチル。
Olefinic hydrocarbons such as l-hexene. butadiene,
Diolefin hydrocarbons such as isoprene, vinyl chloride, chlorinated melefins or diolefin hydrocarbons such as chloroprene, cyclic olefins or diolefins such as cyclohexene, cyclopentadiene, vinylcyclohexene, 7ran, vinylpyridine, vinylcarbazole, etc. Heterocyclic compounds containing a carbon-carbon 5- double bond, aromatic compounds containing a novinyl group such as styrene, α-methylstyrene, divinylbenzene, etc. Aromatic compounds containing vinyl groups such as vinyl chloride and vinylphenanthrene; unsaturated carboxylic acids such as acrylic acid, fumaric acid, and methacrylic acid; and methyl alkuroates.

メタクリル酸メチル、フマル酸メチル勢の不飽和カルボ
ン酸エステル、メチルビニルエーテル、エチルビニルエ
ーテル等のビニルエーテル、酢酸ビニル、ビニルベンゾ
エート、ビニルブチレート等のビニルエステル、アクリ
ロニトリル、メタクリルニトリル等のシアン化オレフィ
ンまたはジオレフィン化合物.アクリル酸アミド、メタ
クリル酸アミド等の不飽和カルボン酸アミド等があけら
れるが、これらの混合物もまた使用可能である。
Unsaturated carboxylic acid esters such as methyl methacrylate and methyl fumarate, vinyl ethers such as methyl vinyl ether and ethyl vinyl ether, vinyl esters such as vinyl acetate, vinyl benzoate and vinyl butyrate, cyanated olefins or diolefins such as acrylonitrile and methacrylonitrile. Compound. Unsaturated carboxylic acid amides such as acrylamide and methacrylic acid amide can be used, but mixtures thereof can also be used.

本発明に使用されるフマル酸ジアルキルエステルは、以
下の化学式に示される化合物である。
The fumaric acid dialkyl ester used in the present invention is a compound represented by the following chemical formula.

1 〇 6一 式中XとYは互いに異なるアルキル基であり。1 〇 61 In the formula, X and Y are different alkyl groups.

例えばメチル基、エチル基、n−プロピル基、イソプロ
ピル基、n−ブチル基、  5ec−ブチル基、を−ブ
チル基3 ネオペンチル基、  5ee−ペンチル基。
For example, methyl group, ethyl group, n-propyl group, isopropyl group, n-butyl group, 5ec-butyl group, -butyl group, neopentyl group, 5ee-pentyl group.

イソペンチル基などが例示できるが、さらにX。Examples include isopentyl group, and X.

Yの少くとも一方がかさ高い分枝アルキル基であること
を必須要件としている。このような非対称7マル酸ジエ
ステルとしてはアルキル基の種々の組合せが可能でおり
、例えばフマル酸メチルイソプロピルジエステル、フマ
ル酸メチルt −7’fルジエステル、フマル酸メチル
ネオペンチルジエステル、フマル酸エチルイソプロピル
ジエステル、7マル酸エチルt−ブチルジエステル、フ
マル酸エチルネオペンチルジエステル、フマル酸イソプ
ロピルt−ブチルジエステルなどがある。
It is an essential requirement that at least one of Y is a bulky branched alkyl group. Various combinations of alkyl groups are possible for such asymmetric 7-malate diesters, such as methyl isopropyl fumarate diester, methyl t-7'f diester fumarate, methyl neopentyl fumarate diester, ethyl isopropyl fumarate diester. , ethyl t-butyl 7-malate diester, ethyl neopentyl fumarate diester, isopropyl t-butyl fumarate, and the like.

本発明に用いられるフマル酸ジアルキルエステルは種々
の公知のエステル化法で合成することができる。たとえ
ば、フマル酸をまずアルコールでし エステル化2.さらに得られたフマル酸モノアルキルエ
ステルを他の分校アルコールK ヨー> テニスチル化
【7てフマル酸ジアルキルエステルを合成スる方法があ
る。他に、無水マレイン酸もしくはマレイン酸からエス
テル化および異性化反応によっても得ることができる。
The fumaric acid dialkyl ester used in the present invention can be synthesized by various known esterification methods. For example, fumaric acid is first esterified with alcohol.2. Furthermore, there is a method of synthesizing the fumaric acid dialkyl ester by subjecting the obtained fumaric acid monoalkyl ester to other branch alcohols. Alternatively, it can be obtained from maleic anhydride or maleic acid by esterification and isomerization reactions.

本発明に使用されるフマル酸ジエステルは、あらかじめ
蒸留等の方法で精製しておくことが好ましい。
The fumaric acid diester used in the present invention is preferably purified in advance by a method such as distillation.

本発明において、重合可能な不飽和二重結合を有する化
合物とフマル酸ジアルキルエステルの共重合は通常の方
法で実施されるが、例えば適当なラジカル重合開始剤の
存在下、溶媒中あるいは無溶媒下で大気圧、加圧下もし
くは減圧下で必要に応じて加熱することによって目的を
達せられる。
In the present invention, copolymerization of a compound having a polymerizable unsaturated double bond and a fumaric acid dialkyl ester is carried out by a conventional method, for example, in the presence of a suitable radical polymerization initiator, in a solvent or without a solvent. The purpose can be achieved by heating as necessary at atmospheric pressure, elevated pressure or reduced pressure.

その場合、反応系を不活性ガス、例えば窒素、ヘリウム
、アルゴン等で置換する方法も実施できる。
In that case, a method of replacing the reaction system with an inert gas such as nitrogen, helium, argon, etc. can also be implemented.

本発明に用いられるラジカル開始剤としては例えば種々
の有機過酸化物類、レドックス試薬、過ハロゲン化物類
酸素などがあり、他に熱、光、放射線等もあげられ、そ
れらの併用も可能である。
Radical initiators used in the present invention include, for example, various organic peroxides, redox reagents, perhalides, and oxygen, as well as heat, light, radiation, etc., and combinations thereof are also possible. .

溶媒を用いる場合は、ラジカル重合に用いるこ重合方法
としては、塊状重合、溶液重合、懸濁重合、乳化重合、
気相重合のいずれの方法でも実施可能である。いずれの
重合法を用いても、原料となる重合可能な不飽和二重結
合を有する化合物とフマル酸ジアルキルエステルとの混
合比を変えることによシ、生成共重合体中への官能基の
導入割合や位置を容易に調節することができる。
When using a solvent, the polymerization methods used for radical polymerization include bulk polymerization, solution polymerization, suspension polymerization, emulsion polymerization,
Any method of gas phase polymerization can be used. Regardless of which polymerization method is used, functional groups can be introduced into the resulting copolymer by changing the mixing ratio of the raw material compound having a polymerizable unsaturated double bond and fumaric acid dialkyl ester. Proportion and position can be easily adjusted.

本発明の合成法によれば、所定量の官能基を有する共重
合体を容易に得ることができ、得られた共重合体は、適
量の7マル酸ジアルキルエステルの付加により、対応す
る単独重合体本来の特性を低下させることなく望ましい
加工特性、例えば染□  色性、接着性、内部可ソ性、
静電防止性愈とが着。
According to the synthesis method of the present invention, a copolymer having a predetermined amount of functional groups can be easily obtained. Desirable processing properties such as dyeability, adhesion, internal solubility,
Comes with anti-static material.

しく改善される。さらに共重合体に導入されたエステル
基は、必!!々特性を付与するためにケン化。
improved. Furthermore, the ester group introduced into the copolymer is a must! ! Saponified to give various properties.

エステル置換、アミド化等の反応に供することができる
It can be subjected to reactions such as ester substitution and amidation.

以下に本発明の具体的か実施例を例示するが、これらは
本発明の範囲を制限するものでない。以9− 下チは重量係を示す。
Specific examples of the present invention are illustrated below, but these are not intended to limit the scope of the present invention. 9- The lower part indicates the weight.

実施例1−1 内容1tの攪拌機と温度計を付したオートクレーブ中に
所定量のフマル酸メチルt−ブチルジエステルを仕込み
、窒素で系を十分置換し1次いでエチレンガスで系を置
換した。その後、重合開始剤として純酸素1.00 c
oをガスシリンジでオートクレーブ中に導入し、さらに
エチレン280yを導入した。これを160°Cに保ち
、攪拌しながら6時間重合させた。反応終了後室温まで
冷却し、未反応エチレンガスを放出して、反応物を得た
Example 1-1 A predetermined amount of methyl t-butyl diester fumarate was charged into a 1 ton autoclave equipped with a stirrer and a thermometer, and the system was sufficiently purged with nitrogen and then replaced with ethylene gas. Then, 1.00 c of pure oxygen was added as a polymerization initiator.
o was introduced into the autoclave using a gas syringe, and ethylene 280y was further introduced. This was maintained at 160°C and polymerized for 6 hours while stirring. After the reaction was completed, the reaction mixture was cooled to room temperature and unreacted ethylene gas was released to obtain a reaction product.

得られた反応物を熱デカリンに溶解し、ヘキサン中に注
いで再沈澱させ口過分離してポリマ寸を得た。得られた
ポリマーの収率、フマル酸ジアルキルエステルの付加率
、分子量についての測定結果を表−1に示す。
The obtained reaction product was dissolved in hot decalin, poured into hexane, reprecipitated, and separated by filtration to obtain a polymer size. Table 1 shows the measurement results for the yield of the obtained polymer, the addition rate of fumaric acid dialkyl ester, and the molecular weight.

一1〇− 表−1 フマル酸メチル t−ブチルジエステルの付加率は元素
分析値から算出した。ポリマーの分子量はシュタウデイ
ンガーの極限粘度法によシ求めた。
110-Table-1 Methyl fumarate The addition rate of t-butyl diester was calculated from the elemental analysis values. The molecular weight of the polymer was determined by Staudinger's limiting viscosity method.

以下の実施例および比較例についても同様である。The same applies to the following Examples and Comparative Examples.

比較例−1 実施例体へにおいて、フマル酸メチルt−ブチルジエス
テルのかわりに、マレイン酸またはツマっだ。その結果
を表−2および表−3に示す。
Comparative Example 1 In the example, maleic acid or tsumarate was used instead of methyl t-butyl diester fumarate. The results are shown in Table-2 and Table-3.

表−2゜ 表−3 かなように、実施例のものは高い付加率を示すのに、マ
レイン酸はほとんど反応せず、またフマル酸ジメチルエ
ステルの付加率も著しく低いことがわかる。
As shown in Table 2 and Table 3, although the Examples showed a high addition rate, maleic acid hardly reacted and the addition rate of fumaric acid dimethyl ester was also extremely low.

実施−P2 あらかじめ蒸留精製したスチレン20yおよびフマル酸
メチルt−ブチルジエステルの所定量をパイレックスガ
ラス製重合用封管に仕込み、さらにベゾイルペルオキシ
ド(BPO)の所定量(2X 10 ”mol/l)を
添加し、常法に従い十分に窒素置換を行なって封管を溶
封した。この重合用封管な振とう式湯浴に入れ80゛C
±0.2°Cに保ち、6時間反応させた。重合終了後、
封管の内容物をメタノールで洗滌し、ベンゼン−塩酸性
メタノールで再沈澱させてポリマーを得た。得られたポ
リマーについての結果を表−4に示す。
Implementation-P2 A predetermined amount of styrene 20y and methyl t-butyl fumarate diester, which had been distilled and purified in advance, was charged into a sealed polymerization tube made of Pyrex glass, and a predetermined amount (2X 10” mol/l) of bezoyl peroxide (BPO) was added. The sealed tube was melt-sealed by thoroughly purging with nitrogen according to the usual method.The sealed tube for polymerization was placed in a shaking water bath at 80°C.
The mixture was kept at ±0.2°C and reacted for 6 hours. After polymerization,
The contents of the sealed tube were washed with methanol and reprecipitated with benzene-hydrochloric methanol to obtain a polymer. Table 4 shows the results for the obtained polymer.

表−4 比較例−2 実施−に2において、フマル酸メチルt−ブチルエステ
ルのかわりに、マレイン酸またはフマル酸ジメチルエス
テルを用いた以外はすべて実施例1−2と同様にして賞
金反応を行なりた。その結果を表−5および表−6に示
す。
Table 4 Comparative Example 2 The bounty reaction was carried out in the same manner as in Example 1-2 except that maleic acid or dimethyl fumarate was used instead of methyl t-butyl fumarate in Example 2. It became. The results are shown in Table-5 and Table-6.

13− 表−6 かなように、実施例のものは高い付加率を示すのに、マ
レイン酸はほとんど反応せずまたフマル酸ジメチルエス
テルの付加率も著しく低いことがわかる。
13-Table 6 As can be seen, although the examples showed a high addition rate, maleic acid hardly reacted and the addition rate of fumaric acid dimethyl ester was also extremely low.

実施例 1−3 実施例1−1で用いたものと同様のオートクレーブを用
い、そこにフマル酸メチルt−ブチルジエステルを所定
量と過酸化ラウロイル0.5ノを仕込み、系を一20°
Cに冷却、窒素置換した仮、塩化ビニル300Fを導入
した。これを60°Cに保ち攪拌しながら6時間重合さ
せた。反応終了後、水洗、口過してポリマーを得た。得
られたポリマーについての結果を表−7に示す。
Example 1-3 Using an autoclave similar to that used in Example 1-1, a predetermined amount of methyl t-butyl diester fumarate and 0.5 g of lauroyl peroxide were charged therein, and the system was heated to -20°.
Temporary vinyl chloride 300F, which had been cooled and replaced with nitrogen, was introduced into C. This was polymerized for 6 hours while maintaining the temperature at 60°C and stirring. After the reaction was completed, the polymer was washed with water and passed through the mouth to obtain a polymer. The results for the obtained polymer are shown in Table-7.

14− 表−7 実施例−1−4 攪拌機、温度針、冷却管を付した5 00 mlの4つ
ロフラスコに150−のジメチルホルムアミドと所定量
のフマル酸メチルt−ブチルジエステルおよびアクリロ
ニトリル120Fを混合導入し、系を窒素で十分置換し
た後、アゾビスイソブチロニトリル3重量%のジメチル
ホルムアミド溶液20−を添加し、60°Cに温度を保
ち6時間重合させた。反応終了後、未反応のアクリロニ
トリルをアスピレータ−で減圧除去し、得られたポリマ
ー溶液を大量の水中に加えてポリマーを沈澱させて生成
ポリマーを得た。得られたポリマーについての結果を表
−8に示す。
14- Table-7 Example-1-4 Mix 150-dimethylformamide, predetermined amounts of methyl t-butyl fumarate diester, and acrylonitrile 120F in a 500 ml four-bottle flask equipped with a stirrer, temperature needle, and cooling tube. After the system was sufficiently purged with nitrogen, a solution of 3% by weight of azobisisobutyronitrile in dimethylformamide (20%) was added, and the temperature was maintained at 60°C for polymerization for 6 hours. After the reaction was completed, unreacted acrylonitrile was removed under reduced pressure using an aspirator, and the resulting polymer solution was added to a large amount of water to precipitate the polymer to obtain a produced polymer. Table 8 shows the results for the obtained polymer.

表−8 実施例−1−5 実施例1−1で用いたものと同様のオートクレーブに7
マル酸メチルt−ブチルジエステル所定量と塩化ロジウ
ム2yドデシルベンゼンスルホン酸ナトリウム10ノ、
水400mgを加え冷却して200りのブタジェンを加
えた。次いで攪拌しなから80°Cで4時間重合を行な
い0重合終了後室温まで冷却し、未反応ブタジェンを除
去した後。
Table-8 Example-1-5 In an autoclave similar to that used in Example 1-1,
Predetermined amount of methyl t-butyl diester malate and 10 parts of rhodium chloride 2y sodium dodecylbenzenesulfonate,
400 mg of water was added, cooled, and 200 mg of butadiene was added. Next, polymerization was carried out at 80° C. for 4 hours without stirring, and after completion of zero polymerization, the mixture was cooled to room temperature and unreacted butadiene was removed.

内容物をメタノール中に加えて沈澱させることKより生
成ポリマーを得た。得られたポリマーについての結果を
表−9に示す。
The resulting polymer was obtained by adding the contents into methanol and precipitating it. Table 9 shows the results for the obtained polymer.

15− 表−9 ただし極限粘度は1トラリン溶媒下で測定、以下も同様
である。
15-Table-9 However, the intrinsic viscosity was measured in 1-traline solvent, and the same applies below.

実施例 1−6 実施例1−1で用いたものと同様のオートクレーブにホ
ルムアミド360 jE、  フマル酸メチルを一ブチ
ルジエステル所定量、スチレン25F、ブタジェン15
0りを仕込み、乳化剤としてラウリル硫酸ナトリウム1
05Fを用い、さらにドデシルメルカプタン1.5yを
加えその後、系を窒素で十分置換し、過硫酸カリウムI
Pを添加し、攪拌し表から50°Cで25時間反応させ
た。反応終了後未反応のブタジェンを除去し、生成ポリ
マーにポリマーに対し2重量%のフェニルβ−ナフチル
アミンを添加した後、25チ食塩水に注ぎポリマーを凝
固させ水洗、乾燥してポリマーを得た。
Example 1-6 In an autoclave similar to that used in Example 1-1, formamide 360 jE, methyl fumarate in a predetermined amount of monobutyl diester, styrene 25F, and butadiene 15
0 and sodium lauryl sulfate as an emulsifier.
Using 05F, 1.5y of dodecyl mercaptan was added, the system was sufficiently purged with nitrogen, and potassium persulfate I
P was added, stirred, and reacted at 50°C for 25 hours. After the reaction was completed, unreacted butadiene was removed, and phenyl β-naphthylamine was added to the resulting polymer in an amount of 2% by weight based on the polymer, followed by pouring into 25% brine to coagulate the polymer, washing with water, and drying to obtain a polymer.

17− 16− 生成ポリマーについての結果を表−ioに示す。17- 16- The results for the produced polymers are shown in Table-io.

表−10 実施例2−1〜2−6 実施例1−1〜1−6において、フマル酸メチルt−ブ
チルジエステルの代ルに7マル酸エチルネオペンチルジ
エステルを表−11のように用いた場合について、それ
ぞれに対応する同様の反応条件で重合させてポリマーを
得た。それらの結果を表−11に示す。
Table 10 Examples 2-1 to 2-6 In Examples 1-1 to 1-6, ethyl neopentyl 7-malate was used as a substitute for methyl t-butyl fumarate as shown in Table 11. In each case, polymers were obtained by polymerization under similar reaction conditions corresponding to each case. The results are shown in Table-11.

18− 表−11 実施例3−1〜3−6 実施例1−1〜1〜6にお、いて、フマル酸メチルt−
ブチルジエステルの代シにフマル酸イソプロピルt−ブ
チルジエステルを表12のように用いた場合について、
それぞれに対応する同様の反応条件で重合させてポリマ
ーを得た。それらの結果を表−12に示す。
18- Table-11 Examples 3-1 to 3-6 In Examples 1-1 to 1 to 6, methyl fumarate t-
When using isopropyl t-butyl fumarate as a substitute for butyl diester as shown in Table 12,
Polymers were obtained by polymerization under similar reaction conditions corresponding to each. The results are shown in Table-12.

表−12 特許出願人 日本油月−4未入会λ土Table-12 patent applicant Nihon Yugetsu-4 non-member λ soil

Claims (1)

【特許請求の範囲】[Claims] 重含可能な不飽和二重結合を有する化合物を重合させる
際に、少なくとも1個のかさ高い分枝アルキル基をもつ
非対称の7マル酸ジアルキルエステルを用いることを特
徴とする共重合体の合成法。
A method for synthesizing a copolymer, which comprises using an asymmetric 7-malate dialkyl ester having at least one bulky branched alkyl group when polymerizing a compound having an unsaturated double bond that can be superimposed. .
JP8330782A 1982-05-19 1982-05-19 Synthesis of novel copolymer Pending JPS58201814A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8330782A JPS58201814A (en) 1982-05-19 1982-05-19 Synthesis of novel copolymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8330782A JPS58201814A (en) 1982-05-19 1982-05-19 Synthesis of novel copolymer

Publications (1)

Publication Number Publication Date
JPS58201814A true JPS58201814A (en) 1983-11-24

Family

ID=13798755

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8330782A Pending JPS58201814A (en) 1982-05-19 1982-05-19 Synthesis of novel copolymer

Country Status (1)

Country Link
JP (1) JPS58201814A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2561538A1 (en) * 1984-03-26 1985-09-27 Nippon Oil Co Ltd MEMBRANE FOR THE SELECTIVE SEPARATION OF GAS
JPS6128513A (en) * 1984-07-19 1986-02-08 Nippon Oil & Fats Co Ltd Optical resin and its production
JPS62198759A (en) * 1986-02-26 1987-09-02 Mitsubishi Chem Ind Ltd Polymer for liquid separation
JPH05112614A (en) * 1992-04-22 1993-05-07 Nippon Oil & Fats Co Ltd Production of optical material
JPH05132522A (en) * 1992-04-22 1993-05-28 Nippon Oil & Fats Co Ltd Production of optical material
JP2012032784A (en) * 2010-07-06 2012-02-16 Tosoh Corp Fumaric acid diester-based resin for retardation film and retardation film comprising the same

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2561538A1 (en) * 1984-03-26 1985-09-27 Nippon Oil Co Ltd MEMBRANE FOR THE SELECTIVE SEPARATION OF GAS
JPS6128513A (en) * 1984-07-19 1986-02-08 Nippon Oil & Fats Co Ltd Optical resin and its production
JPS62198759A (en) * 1986-02-26 1987-09-02 Mitsubishi Chem Ind Ltd Polymer for liquid separation
JPH05112614A (en) * 1992-04-22 1993-05-07 Nippon Oil & Fats Co Ltd Production of optical material
JPH05132522A (en) * 1992-04-22 1993-05-28 Nippon Oil & Fats Co Ltd Production of optical material
JP2012032784A (en) * 2010-07-06 2012-02-16 Tosoh Corp Fumaric acid diester-based resin for retardation film and retardation film comprising the same
US9266988B2 (en) 2010-07-06 2016-02-23 Tosoh Corporation Fumaric acid diester based resin for retardation film and retardation film comprising the same

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