JP2002293833A - Copolymer of oligostyrene (meth)acrylate and methyl (meth)acrylate and its production method - Google Patents

Copolymer of oligostyrene (meth)acrylate and methyl (meth)acrylate and its production method

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Publication number
JP2002293833A
JP2002293833A JP2001095216A JP2001095216A JP2002293833A JP 2002293833 A JP2002293833 A JP 2002293833A JP 2001095216 A JP2001095216 A JP 2001095216A JP 2001095216 A JP2001095216 A JP 2001095216A JP 2002293833 A JP2002293833 A JP 2002293833A
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Japan
Prior art keywords
meth
acrylate
copolymer
oligostyrene
methyl
Prior art date
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Application number
JP2001095216A
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Japanese (ja)
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JP4787418B2 (en
Inventor
Takashi Sawaguchi
孝志 澤口
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Sawaguchi Takashi
Sanei Kogyo KK
Original Assignee
Sawaguchi Takashi
Sanei Kogyo KK
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Priority to JP2001095216A priority Critical patent/JP4787418B2/en
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  • Macromonomer-Based Addition Polymer (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a novel copolymer of an oligostyrene (meth)acrylate and a methyl (meth)acrylate. SOLUTION: The copolymerization of the oligostyrene (meth)acrylate and the methyl (meth)acrylate produces the novel copolymer.

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(メタ)アク
リル酸オリゴスチレン・エステルと(メタ)アクリル酸
メチルとの共重合体及びその製造方法に関する。
TECHNICAL FIELD The present invention relates to a novel copolymer of oligostyrene (meth) acrylate and methyl (meth) acrylate and a method for producing the same.

【0002】[0002]

【従来技術】従来から(メタ)アクリル酸メチルと(メ
タ)アクリル酸スチレン・エステルとの共重合体は知ら
れていたが、(メタ)アクリル酸オリゴスチレン・エス
テルとの共重合体については、全く知られていなかっ
た。
2. Description of the Related Art Conventionally, copolymers of methyl (meth) acrylate and styrene (meth) acrylate have been known. Not known at all.

【0003】[0003]

【発明が解決しようとする課題】本発明は、(メタ)ア
クリル酸オリゴスチレン・エステルと(メタ)アクリル
酸メチルとの新規な共重合体及びその製造方法を提供す
る。
SUMMARY OF THE INVENTION The present invention provides a novel copolymer of oligostyrene (meth) acrylate and methyl (meth) acrylate and a method for producing the same.

【0004】[0004]

【課題を解決するための手段】本発明は、本発明者が開
発した新規なモノマである、(メタ)アクリル酸オリゴ
スチレン・エステルを(メタ)アクリル酸メチルとのラ
ジカル重合させることにより、新規な(メタ)アクリル
酸オリゴスチレン・エステルと(メタ)アクリル酸メチ
ル共重合体が得られることを見出し本発明を完成した。
SUMMARY OF THE INVENTION The present invention provides a novel monomer, a novel monomer developed by the present inventor, by radical polymerization of (meth) acrylic acid oligostyrene ester with methyl (meth) acrylate. It has been found that a (meth) acrylic acid oligostyrene ester and a methyl (meth) acrylate copolymer can be obtained, and the present invention has been completed.

【0005】すなわち、本発明にかかる共重合体は、下
記一般式(1)と(2)で表される繰り返し構造単位から
なる数平均分子量1000〜500000の共重合体で
ある。
That is, the copolymer according to the present invention is a copolymer having a number average molecular weight of 1,000 to 500,000 and comprising a repeating structural unit represented by the following general formulas (1) and (2).

【化5】 式中、Rは水素またはメチル基を表わし、nは2〜10
の整数を表わす。
Embedded image In the formula, R represents hydrogen or a methyl group, and n represents 2 to 10
Represents an integer.

【化6】 式中、R1は水素またはメチル基を表わす。Embedded image In the formula, R 1 represents hydrogen or a methyl group.

【0006】また、本発明にかかる共重合体は前記一般
式(1)中のR、および(2)中のR1がメチル基であり、
nが2または3であることを特徴とする。
Further, the copolymer according to the present invention wherein R 1 is a methyl group R, and (2) of the general formula (1),
It is characterized in that n is 2 or 3.

【0007】さらに、本発明にかかる(メタ)アクリル
酸オリゴスチレン・エステルと(メタ)アクリル酸メチ
ルとの共重合体の製造方法は、下記一般式(3)
Further, a method of producing a copolymer of oligostyrene (meth) acrylate and methyl (meth) acrylate according to the present invention is represented by the following general formula (3):

【化7】 (式中、Rは水素またはメチル基を表わし、nは2〜1
0の整数を表わす)で表わされる(メタ)アクリル酸オリ
ゴスチレン・エステルと、
Embedded image (Wherein, R represents hydrogen or a methyl group, and n represents 2 to 1)
(Representing an integer of 0) (meth) acrylic acid oligostyrene ester represented by

【化8】 (式中、R1は水素またはメチル基を表わす)で表わさ
れる(メタ)アクリル酸メチルとを、有機溶媒中において
重合させることを特徴とする。
Embedded image (Wherein R 1 represents hydrogen or a methyl group), and is characterized by being polymerized in an organic solvent with methyl (meth) acrylate.

【0008】さらには、前記重合反応がラジカル重合で
あることを特徴とする。
Further, the present invention is characterized in that the polymerization reaction is radical polymerization.

【0009】[0009]

【発明の実施の形態】以下本発明を実施の形態に即して
詳細に説明する。(メタ)アクリル酸オリゴスチレン・エステルと(メ
タ)アクリル酸メチルとの共重合体 本発明にかかる共重合体は、その繰り返し構造単位が、
一般式(1)及び(2)で表されるものであることを特徴と
する。その分子量について特に制限はなく、以下に説明
する重合反応を制御することにより広い範囲で得ること
ができる。分子量(Mn、Mw)及び分子量分布(Mw
/Mn)はポリスチレンを標準としてゲルパーミエーシ
ョンクロマトグラフ(GPC)にて測定することができ
る。本発明において好ましい分子量は10000〜10
0000の範囲である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail with reference to embodiments. (Meth) acrylic acid oligostyrene ester
(T) Copolymer with methyl acrylate The copolymer according to the present invention has a repeating structural unit
It is characterized by being represented by the general formulas (1) and (2). The molecular weight is not particularly limited, and can be obtained in a wide range by controlling the polymerization reaction described below. Molecular weight (Mn, Mw) and molecular weight distribution (Mw
/ Mn) can be measured by gel permeation chromatography (GPC) using polystyrene as a standard. The preferred molecular weight in the present invention is 10,000 to 10
0000.

【0010】また、共重合体中の各繰り返し構造の存在
比(モル比)には特に制限はなく以下説明する製造方法
により広い範囲で得ることができる。本発明において
は、一般式(1)で表される繰り返し構造と一般式
(2)で表される繰り返し構造との比が、0.1:0.9
9〜0.99〜0.1の範囲であることが好ましく、さら
に1:99〜99:1の範囲であることが好ましい。
[0010] The abundance ratio (molar ratio) of each repeating structure in the copolymer is not particularly limited, and can be obtained in a wide range by the production method described below. In the present invention, the ratio of the repeating structure represented by the general formula (1) to the repeating structure represented by the general formula (2) is 0.1: 0.9.
It is preferably in the range of 9 to 0.99 to 0.1, and more preferably in the range of 1:99 to 99: 1.

【0011】表1及び表2には典型的な本発明の共重合
体について、仕込みメチルメタクリル酸(MMA)のモ
ル分率、得られる共重合体のMw、Mw/Mn、収率及
びMMA単位のモル分率がまとめられている。また、表
3にはA−SDを用いた場合、仕込みMMAのモル分
率、得られる共重合体中のMMA単位のモル分率がまと
められている。
Tables 1 and 2 show typical copolymers of the invention for the mole fraction of charged methyl methacrylic acid (MMA), Mw, Mw / Mn, yield and MMA units of the resulting copolymer. Are summarized. In addition, Table 3 summarizes the molar fraction of charged MMA and the molar fraction of MMA units in the obtained copolymer when A-SD is used.

【0012】[0012]

【表1】 [Table 1]

【0013】ここで、a)分子量はポリスチレンを標準と
してGPCで測定した。b)共重合体中のMMA単位のモ
ル分率は重クロロホルム中の1HNMRで求めた。重合
反応は、窒素置換したガラスアンプルを用いてベンゼン
中で、[モノマ濃度]=0.18mol/L、[AIB
N]=0.0036mol/L、60℃、3時間の条件
で行った。
Here, a) The molecular weight was measured by GPC using polystyrene as a standard. b) The molar fraction of MMA units in the copolymer was determined by 1 HNMR in deuterated chloroform. [Polymer concentration] = 0.18 mol / L, [AIB]
N] = 0.0036 mol / L, at 60 ° C. for 3 hours.

【0014】[0014]

【表2】 [Table 2]

【0015】ここで、a)分子量はポリスチレンを標準と
してGPCで測定した。b)MMA単位のモル分率は重ク
ロロホルム中の1H NMRで求めた。重合反応は、窒素
置換したガラスアンプルを用いてトルエン中で、[モノ
マ濃度]=1.87mol/L、[AIBN]=0.02
mol/L、60℃、3時間の条件で行った。
Here, a) the molecular weight was measured by GPC using polystyrene as a standard. b) The molar fraction of MMA units was determined by 1 H NMR in chloroform- d . In the polymerization reaction, [monomer concentration] = 1.87 mol / L, [AIBN] = 0.02 in toluene using a glass ampoule substituted with nitrogen.
The reaction was performed under the conditions of mol / L, 60 ° C. and 3 hours.

【0016】[0016]

【表3】 [Table 3]

【0017】ここで、MMA単位のモル分率は重クロロ
ホルム中の1H NMRで求めた。重合反応は、窒素置換
したガラスアンプルを用いてトルエン中で、[モノマ濃
度]=0.18mol/L、[AIBN]=0.003m
ol/L、60℃、3時間の条件で行った。
Here, the molar fraction of MMA units was determined by 1 H NMR in chloroform-d. In the polymerization reaction, [monomer concentration] = 0.18 mol / L, [AIBN] = 0.003 m in toluene using a glass ampoule substituted with nitrogen.
ol / L, 60 ° C., 3 hours.

【0018】さらに、本発明の共重合体の繰り返し構造
単位の結合様式については特に制限はなく完全なランダ
ム共重合体から完全なブロック共重合体まで含むが、好
ましくは部分的にブロック性を有するランダム共重合体
である。ブロック性は、例えば1H NMR、13C NM
Rのミクロ構造からランダム共重合体かブロック性を有
する共重合体かが推定できる。図1及び図2にはそれぞ
れ本発明の共重合体(MMAが70%モル組成、n=
2)と、ポリメタアクリル酸ジスチレン・エステル(P
M−SD)とポリメタアクリル酸メチル(PMMA)の
ブレンド物の1HNMRが示されている。明らかに本発
明の共重合体がブロック性であることがわかる。
Further, there is no particular limitation on the bonding mode of the repeating structural units of the copolymer of the present invention, and it includes from a completely random copolymer to a completely block copolymer, but preferably has a partially blockable property. It is a random copolymer. Blocking properties are, for example, 1 H NMR, 13 C NM
From the microstructure of R, it can be estimated whether the copolymer is a random copolymer or a block copolymer. FIGS. 1 and 2 show the copolymer of the present invention (MMA 70% molar composition, n =
2) and polystyrene distyrene methacrylate (P
1 H NMR of a blend of M-SD) and polymethyl methacrylate (PMMA) is shown. It is apparent that the copolymer of the present invention is blockable.

【0019】またブロック性の見積もりには、Fineman-
Ross法によるr値測定が可能である。具体的には、図3
に一例として仕込み量のMMAのモル分率と、共重合体
中のMMAのモル分率が示されているように前記r値は
1より大きく、ランダムというよりもブロック性が多い
ことがわかる。
In order to estimate the blocking property, Fineman-
R value measurement by the Ross method is possible. Specifically, FIG.
As an example, the r value is larger than 1 as shown by the mole fraction of MMA in the charged amount and the mole fraction of MMA in the copolymer, and it can be seen that the blockability is greater than random.

【0020】また、本発明の共重合体の熱特性の1つと
してDSC測定によるガラス転移温度(Tg)が挙げら
れる。図4にその一例が挙げられているように、共重合
体中の2つの繰り返し構造単位のモル比が1:1に近づ
くに従ってTgは低下し、1:1では約40℃にまで達
することがわかる。このTgの低下は、PMMAのTg
が約130℃であり、またポリメタアクリル酸ジスチレ
ン・エステル(PM−SD)のTgが約70℃であるこ
とから本発明の共重合体に特徴的である。
One of the thermal properties of the copolymer of the present invention is a glass transition temperature (Tg) measured by DSC. As an example is shown in FIG. 4, as the molar ratio of two repeating structural units in the copolymer approaches 1: 1, Tg decreases, and at 1: 1 it can reach about 40 ° C. Understand. This decrease in Tg is due to the Tg of PMMA.
Is about 130 ° C. and the Tg of polystyrene dimethacrylate (PM-SD) is about 70 ° C., which is characteristic of the copolymer of the present invention.

【0021】製造方法 本発明にかかる共重合体は、一般式(3)で表される(メ
タ)アクリル酸オリゴスチレン・エステルをモノマとし
て一般式(4)で表される(メタ)アクリル酸メチルとと
もに重合させることを特徴とする。ここで、(メタ)アク
リル酸オリゴスチレン・エステルの合成には特に制限は
ないが以下に説明する方法により容易に得ることができ
る。
Production Method The copolymer according to the present invention is a methyl (meth) acrylate represented by the general formula (4) using a monomer of the oligostyrene (meth) acrylate represented by the general formula (3) as a monomer. And polymerized together. Here, the synthesis of the (meth) acrylic acid oligostyrene ester is not particularly limited, but can be easily obtained by the method described below.

【0022】本発明者の開発した熱分解方法(Journal
of Polymer Science, Polym. Chem., 36, 209 (1998))
により、スチレンモノマ単位の繰り返し数が2〜10程
度の単分散性の片末端ビニリデン基含有オリゴスチレン
が得られる。単分散性の末端ビニリデン基含有オリゴス
チレンのビニリデン基を、常法により酸化することによ
り単分散性の末端ヒドロキシ基含有オリゴスチレンを得
ることができる。
The pyrolysis method developed by the present inventors (Journal
of Polymer Science, Polym. Chem., 36, 209 (1998))
As a result, a monodisperse oligostyrene containing one terminal vinylidene group having a repeating number of styrene monomer units of about 2 to 10 is obtained. Monodisperse oligostyrene having a terminal hydroxy group can be obtained by oxidizing the vinylidene group of the monodisperse oligostyrene having a terminal vinylidene group by a conventional method.

【0023】さらにここで得られる単分散性の末端ヒド
ロキシ基含有オリゴスチレンと、(メタ)アクリル酸また
は(メタ)アクリル酸塩化物とを常法により反応させる
ことにより一般式(3)で表わされる(メタ)アクリル酸
オリゴスチレン・エステルを容易に製造することができ
る。また、(メタ)アクリル酸メチルは市販品が好ましく
使用できる。
Further, the monodisperse oligostyrene having a terminal hydroxy group obtained here is reacted with (meth) acrylic acid or (meth) acrylic acid chloride by a conventional method to obtain a compound represented by the general formula (3). (Meth) acrylic acid oligostyrene ester can be easily produced. Commercially available methyl (meth) acrylate can be preferably used.

【0024】本発明の共重合体は、前記モノマを有機溶
媒、好ましくはベンゼン、トルエン、キシレンなどの芳
香族系溶媒中で重合させることにより、容易に製造する
ことができる。重合方法には特に制限はなく、ラジカル
重合、アニオン重合などのイオン重合、有機金属化合物
による重合などの公知の重合法を採用することができ
る。好ましくは、ラジカル重合またはアニオン重合を採
用する。
The copolymer of the present invention can be easily produced by polymerizing the monomer in an organic solvent, preferably an aromatic solvent such as benzene, toluene and xylene. The polymerization method is not particularly limited, and a known polymerization method such as ionic polymerization such as radical polymerization or anionic polymerization, or polymerization using an organometallic compound can be employed. Preferably, radical polymerization or anionic polymerization is employed.

【0025】たとえば、ラジカル開始剤としてアゾビス
イソブチロニトリル(AIBN)を用いたラジカル重合
の場合、室温〜80℃の温度で60分〜25時間反応さ
せることにより、反応溶媒不溶性の重合体を高収率で得
ることができる。
For example, in the case of radical polymerization using azobisisobutyronitrile (AIBN) as a radical initiator, the reaction solvent insoluble polymer is reacted at a temperature of room temperature to 80 ° C. for 60 minutes to 25 hours. It can be obtained in high yield.

【0026】[0026]

【実施例】実施例1 (メタ)アクリル酸オリゴスチレ
ン・エステルの製造 ポリスチレンの高度制御熱分解生成物から単離精製した
前記一般式中のnが2であるスチレンダイマーおよびn
が3であるスチレントリマーのそれぞれをヒドロホウ素
化した後、水酸化ナトリウム水溶液および過酸化水素を
用いて酸化し、末端ヒドロキシ基含有スチレンダイマー
(SD−OH)および末端ヒドロキシ基含有スチレント
リマー(ST−OH)を調製した。次いで、得られたS
D−OHまたはST−OHのトリメチルアミン/ジクロ
ロメタン溶液を、塩化メタクリロイルまたは塩化アクリ
ロイルのジクロロメタン溶液中に、−5℃で滴下し、得
られた反応生成物を、シリカゲル・カラムを用いクロロ
ホルム/ヘキサン=2/1混合溶媒により精製してメタ
クリル酸スチレンダイマー・エステル(M−SD)、メ
タクリル酸スチレントリマー・エステル(M−ST)、
アクリル酸スチレンダイマー・エステル(A−SD)お
よびアクリル酸スチレントリマー・エステル(A−S
T)を調製した。得られたM−SD、M−ST、A−S
DおよびA−STは、IRスペクトル、 1H−NMRス
ペクトルおよび13C−NMRスペクトルにより、いずれ
も前記一般式(2)の構造を有することが確認された。M
−SD、M−ST、A−SDおよびA−STの収率は、
いずれも約70重量%であった。
Embodiment 1Oligostyrene (meth) acrylate
Production of ester Isolated and purified from highly controlled pyrolysis products of polystyrene
A styrene dimer wherein n in the general formula is 2;
Each of the styrene trimers having
Sodium hydroxide solution and hydrogen peroxide
Styrene dimer containing terminal hydroxy group
(SD-OH) and Styrene Containing Terminal Hydroxy Group
A rimer (ST-OH) was prepared. Then, the obtained S
D-OH or ST-OH trimethylamine / dichloro
Methane solution or acryloyl chloride
To a solution of Royl in dichloromethane was added dropwise at -5 ° C.
Chloroform the reaction product obtained using a silica gel column.
Purified with a mixed solvent of form / hexane = 2/1 and meta
Styrene dimer ester (M-SD),
Styrene trimer ester (M-ST),
Acrylic acid styrene dimer ester (A-SD)
And styrene acrylate trimer ester (AS
T) was prepared. Obtained M-SD, M-ST, AS
D and A-ST are IR spectra, 1H-NMR
Vector and13According to the C-NMR spectrum,
Was also confirmed to have the structure of the general formula (2). M
The yields of -SD, M-ST, A-SD and A-ST are:
All were about 70% by weight.

【0027】実施例2 メタクリル酸スチレンダイマー
・エステル(M−SD)とメタクリル酸メチル(MM
A)との共重合 表1及び表2に示すように上記調製したM−SDとMM
Aとを種々の仕込み比で、ラジカル開始剤のアゾビスイ
ソブチロニトリル(AIBN)および反応溶媒のベンゼ
ンと共に重合管に仕込み、凍結、脱気、窒素置換を繰返
した後封管し、反応温度を60℃の条件に設定して重合
を開始させ、生成した重合体を再沈殿によるかまたは沈
殿物として回収した。反応条件および得られた重合体の
特性を表1、2に示した。
Example 2 Styrene methacrylate dimer
・ Ester (M-SD) and methyl methacrylate (MM
A) M-SD and MM prepared as shown in Tables 1 and 2
A was charged into a polymerization tube at various charging ratios together with azobisisobutyronitrile (AIBN) as a radical initiator and benzene as a reaction solvent, followed by repeated freezing, degassing, and nitrogen substitution, and then sealing the tube. Was set to 60 ° C. to initiate polymerization, and the produced polymer was recovered by reprecipitation or as a precipitate. The reaction conditions and the characteristics of the obtained polymer are shown in Tables 1 and 2.

【0028】実施例3 アクリル酸スチレンダイマー・
エステル(A−SD)とメタクリル酸メチル(MMA)
との共重合 上記調製したM−SDとMMAとを種々の仕込み比で、
ラジカル開始剤のアゾビスイソブチロニトリル(AIB
N)および反応溶媒のベンゼンと共に重合管に仕込み、
凍結、脱気、窒素置換を繰返した後封管し、反応温度を
60℃の条件に設定して重合を開始させ、生成した重合
体を再沈殿物として回収した。反応条件および得られた
重合体の特性を他の重合体とともに表3及び表4(DS
Cで求めたTgとGPCで求めた数平均分子量)にまと
めて示した。また、図5にはPMMA、PA−SD及び
MMAとA−SDとの共重合体(仕込み組成比MMA:
A−SD=8:2)の1HNMRスペクトルを示す。同
様に図6には、A−SDとMMAとのラジカル共重合に
おける共重合体の仕込み中のMMAのモル分率と、共重
合体中のMMA単位のモル分率のプロット(共重合組成
曲線)を示す。
Example 3 Styrene acrylate dimer
Ester (A-SD) and methyl methacrylate (MMA)
Copolymerization of M-SD and MMA prepared above at various charging ratios,
Radical initiator azobisisobutyronitrile (AIB)
N) and benzene as a reaction solvent were charged into a polymerization tube,
After repeated freezing, degassing, and nitrogen substitution, the tube was sealed, the reaction temperature was set to 60 ° C., and polymerization was started, and the produced polymer was recovered as a reprecipitate. The reaction conditions and the properties of the obtained polymer are shown together with other polymers in Tables 3 and 4 (DS
(Tg determined by C and number average molecular weight determined by GPC). FIG. 5 shows PMMA, PA-SD and a copolymer of MMA and A-SD (preparation composition ratio MMA:
The 1 HNMR spectrum of A-SD = 8: 2) is shown. Similarly, FIG. 6 is a plot of the mole fraction of MMA during the preparation of the copolymer in the radical copolymerization of A-SD and MMA, and the mole fraction of MMA units in the copolymer (copolymer composition curve). ).

【0029】[0029]

【表4】 [Table 4]

【0030】[0030]

【発明の効果】本発明は、(メタ)アクリル酸オリゴス
チレン・エステルと(メタ)アクリル酸メチルとの共重
合体により、新規な(メタ)アクリル酸オリゴスチレン
・エステルと(メタ)アクリル酸メチルとの共重合体を
得ることができる。
The present invention provides a novel oligostyrene (meth) acrylate and a methyl (meth) acrylate by using a copolymer of an oligostyrene (meth) acrylate and a methyl (meth) acrylate. Can be obtained.

【図面の簡単な説明】[Brief description of the drawings]

【図1】仕込み組成比MMA:M−SD=7:3の本発
明の共重合体の1HNMRスペクトル。
FIG. 1 is a 1 HNMR spectrum of a copolymer of the present invention having a charged composition ratio of MMA: M-SD = 7: 3.

【図2】PMMAとPM−SDのブレンド物の1HNM
Rスペクトル。
FIG. 2: 1 HNM of a blend of PMMA and PM-SD
R spectrum.

【図3】M−SDとMMAとのラジカル共重合における
共重合体の仕込み中のMMAのモル分率と、共重合体中
のMMA単位のモル分率のプロット(共重合組成曲線)
であり、(a)はベンゼン中、(b)はトルエン中で測定し
た。
FIG. 3 is a plot of the molar fraction of MMA during the preparation of the copolymer in the radical copolymerization of M-SD and MMA, and the molar fraction of MMA units in the copolymer (copolymer composition curve).
Where (a) was measured in benzene and (b) was measured in toluene.

【図4】MMAとM−SDとの共重合体のDSCデー
タ。
FIG. 4 is DSC data of a copolymer of MMA and M-SD.

【図5】PMMA、PA−SD及びMMAとA−SDと
の共重合体(仕込み組成比MMA:A−SD=8:2)
1HNMRスペクトル。
FIG. 5: PMMA, PA-SD and a copolymer of MMA and A-SD (prepared composition ratio MMA: A-SD = 8: 2)
1 HNMR spectrum of

【図6】A−SDとMMAとのラジカル共重合における
共重合体の仕込み中のMMAのモル分率と、共重合体中
のMMA単位のモル分率のプロット(共重合組成曲
線)。
FIG. 6 is a plot (copolymer composition curve) of the mole fraction of MMA during the preparation of the copolymer in the radical copolymerization of A-SD and MMA, and the mole fraction of MMA units in the copolymer.

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4J027 AA02 BA07 CB09 4J100 AL03Q AL08P BC43P CA04 DA01 DA04  ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 4J027 AA02 BA07 CB09 4J100 AL03Q AL08P BC43P CA04 DA01 DA04

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 下記一般式(1)と(2)で表される繰り返
し構造単位からなる数平均分子量1000〜50000
0の共重合体。 【化1】 式中、Rは水素またはメチル基を表わし、nは2〜10
の整数を表わす。 【化2】 式中、R1は水素またはメチル基を表わす。
1. A number average molecular weight of 1,000 to 50,000 comprising a repeating structural unit represented by the following general formulas (1) and (2):
0 copolymer. Embedded image In the formula, R represents hydrogen or a methyl group, and n represents 2 to 10
Represents an integer. Embedded image In the formula, R 1 represents hydrogen or a methyl group.
【請求項2】 一般式(1)中のR、および(2)中のR
1がメチル基であり、nが2または3である請求項1記
載の重合体。
2. R in the general formula (1) and R in (2)
The polymer according to claim 1, wherein 1 is a methyl group and n is 2 or 3.
【請求項3】 下記一般式(3) 【化3】 (式中、Rは水素またはメチル基を表わし、nは2〜1
0の整数を表わす)で表わされる(メタ)アクリル酸オ
リゴスチレン・エステルと、 【化4】 (式中、R1は水素またはメチル基を表わす)で表わさ
れる(メタ)アクリル酸メチルとを、有機溶媒中におい
て重合させることを特徴とする請求項1記載の(メタ)
アクリル酸オリゴスチレン・エステル重合体の製造方
法。
3. The following general formula (3): (Wherein, R represents hydrogen or a methyl group, and n represents 2 to 1)
(Meth) acrylic acid oligostyrene ester represented by the formula: (Meth) according to claim 1, wherein methyl (meth) acrylate represented by the formula (wherein R 1 represents hydrogen or a methyl group) is polymerized in an organic solvent.
A method for producing an oligostyrene acrylate / ester polymer.
【請求項4】 重合反応がラジカル重合である請求項3
記載の製造方法。
4. The method according to claim 3, wherein the polymerization reaction is a radical polymerization.
The manufacturing method as described.
JP2001095216A 2001-03-29 2001-03-29 Copolymer of (meth) acrylic acid oligostyrene ester and methyl (meth) acrylate and method for producing the same Expired - Fee Related JP4787418B2 (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004168805A (en) * 2002-11-18 2004-06-17 Takashi Sawaguchi Amphiphilic graft copolymer
CN116525935A (en) * 2023-07-04 2023-08-01 深圳市贝特瑞新能源技术研究院有限公司 Polymer electrolyte prepolymerization liquid, polymer electrolyte and electrochemical device

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JPH0728239A (en) * 1993-07-13 1995-01-31 Hitachi Chem Co Ltd Photosensitive resin composition and production of photosensitive element and resist pattern using the same
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JPH10338829A (en) * 1997-02-07 1998-12-22 Kao Corp Water-base ink for ink jet recording
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JPH01263108A (en) * 1988-04-13 1989-10-19 Ricoh Co Ltd Nonaqueous resin composition
JPH05214245A (en) * 1992-02-04 1993-08-24 Nippon Petrochem Co Ltd Thermoplastic resin composition
JPH0728239A (en) * 1993-07-13 1995-01-31 Hitachi Chem Co Ltd Photosensitive resin composition and production of photosensitive element and resist pattern using the same
JPH09291046A (en) * 1996-04-24 1997-11-11 Sanei Kogyo:Kk Synthesis of 2,4-diphenyl-1-butene or 2,4,6-triphenyl1-hexene in high yield and selectivity
JPH10338829A (en) * 1997-02-07 1998-12-22 Kao Corp Water-base ink for ink jet recording
JPH1161017A (en) * 1997-08-18 1999-03-05 Kao Corp Aqueous ink for ink jet recording
JP2002080532A (en) * 2000-09-06 2002-03-19 Takashi Sawaguchi Oligostyrene (meth)acrylate polymer and method for producing the same

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004168805A (en) * 2002-11-18 2004-06-17 Takashi Sawaguchi Amphiphilic graft copolymer
CN116525935A (en) * 2023-07-04 2023-08-01 深圳市贝特瑞新能源技术研究院有限公司 Polymer electrolyte prepolymerization liquid, polymer electrolyte and electrochemical device
CN116525935B (en) * 2023-07-04 2024-01-12 深圳市贝特瑞新能源技术研究院有限公司 Polymer electrolyte prepolymerization liquid, polymer electrolyte and electrochemical device

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