JPH11322835A - Catalyst for polymerizing polar vinyl monomer and production of polymer from the monomer - Google Patents

Catalyst for polymerizing polar vinyl monomer and production of polymer from the monomer

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Publication number
JPH11322835A
JPH11322835A JP13548598A JP13548598A JPH11322835A JP H11322835 A JPH11322835 A JP H11322835A JP 13548598 A JP13548598 A JP 13548598A JP 13548598 A JP13548598 A JP 13548598A JP H11322835 A JPH11322835 A JP H11322835A
Authority
JP
Japan
Prior art keywords
polymer
catalyst
polymerization
polar vinyl
vinyl monomer
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
JP13548598A
Other languages
Japanese (ja)
Inventor
Kenji Tsuchihara
健治 土原
Masanao Kawabe
正直 川辺
Kazuo Soga
和雄 曽我
Michihiko Asai
道彦 浅井
Yasuzo Suzuki
靖三 鈴木
Satoru Miyazawa
哲 宮沢
Masahide Murata
昌英 村田
Toshio Kase
俊男 加瀬
Hiroyuki Ozaki
裕之 尾崎
Yoshifumi Fukui
祥文 福井
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.)
KAGAKU GIJUTSU SENRYAKU SUISHI
KAGAKU GIJUTSU SENRYAKU SUISHIN KIKO
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
KAGAKU GIJUTSU SENRYAKU SUISHI
KAGAKU GIJUTSU SENRYAKU SUISHIN KIKO
Agency of Industrial Science and Technology
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 KAGAKU GIJUTSU SENRYAKU SUISHI, KAGAKU GIJUTSU SENRYAKU SUISHIN KIKO, Agency of Industrial Science and Technology filed Critical KAGAKU GIJUTSU SENRYAKU SUISHI
Priority to JP13548598A priority Critical patent/JPH11322835A/en
Publication of JPH11322835A publication Critical patent/JPH11322835A/en
Pending legal-status Critical Current

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  • Polymerization Catalysts (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain the subject catalyst for polymerization comprising a cobalt complex with coordinated phosphine ligand, capable of polymerizing many kinds of monomers and having a high catalytic activity. SOLUTION: This catalyst for polymerization comprises a cobalt complex with three coordinated phosphine ligands, pref. a complex of the formula, CH3 C (CH2 PPh2 )3 CoH(BH3 ) and is suitable for obtaining a polar polymer through homopolymerization of acrylonitrile or methacrylonitrile. The polar vinyl polymer is pref. obtained by polymerizing a polar vinyl monomer in a solventless state or in such an inert solvent as to be liquid while polymerization (e.g. opentane, hexane, etc.), at 0-80 deg.C for 0.5-100. The quantity consumed of the catalyst is 1×10<-4> -1×10<-2> mol, in terms of cobalt complex, per 1 mol polar vinyl monomer. The polymer is obtained in a yield <=60% and has a number average molecular weight of 1,000-1,000,000.

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、極性ビニルモノマ
ー重合用触媒及び極性ビニルポリマーの製造方法に関す
る。
The present invention relates to a catalyst for polymerizing a polar vinyl monomer and a method for producing a polar vinyl polymer.

【0002】[0002]

【従来の技術】ポリアクリロニトリル、ポリメタクリル
酸メチル等の極性基を側鎖に有するビニルポリマーは、
非極性ビニルポリマーと比較してさまざまな機能を有す
ることが知られている。これらのポリマーにさらに高い
機能を付与するためには、生成ポリマーの一次構造のよ
り厳密な制御が不可欠であると考えられる。従来、これ
らのポリマーは主としてラジカル重合法により合成され
ているが、この重合法を用いる場合成長種はフリーな
ラジカルであるため他の重合法と比較してその反応性が
高くコントロールが難しいため、生成ポリマーの一次構
造、すなわち立体構造や分子量等の制御、あるいは厳密
なブロックポリマーの生成や末端基の制御は困難で、現
在までのところ新たな機能性の付与には至っていない。
2. Description of the Related Art Vinyl polymers having a polar group in a side chain such as polyacrylonitrile and polymethyl methacrylate are:
It is known to have various functions compared to non-polar vinyl polymers. In order to impart higher functions to these polymers, it is considered that strict control of the primary structure of the resulting polymer is essential. Conventionally, these polymers are mainly synthesized by a radical polymerization method, but when using this polymerization method, since the growing species is a free radical, its reactivity is higher than other polymerization methods and it is difficult to control. However, it is difficult to control the primary structure of the resulting polymer, that is, the three-dimensional structure and molecular weight, or to strictly control the formation of the block polymer and the terminal groups, and so far no new functionality has been imparted.

【0003】これに対し、有機金属錯体触媒による重合
では、金属が常に成長種の近傍に存在するため、その中
心金属、配位子等の組み合わせを選択することにより、
成長種の反応性やモノマーの挿入方向をコントロールす
ることが比較的容易に行えるため、上記のような機能性
の付与にはより適した重合法であると考えられる。すで
にエチレン、プロピレン、スチレン等の非極性ビニルモ
ノマーについては、このような考え方に基づき有機金属
錯体触媒を用いた立体規則性重合やリビング重合が可能
となり、ブロックポリマーや末端基の制御等による高い
機能性の付与が行われている。
On the other hand, in polymerization using an organometallic complex catalyst, a metal is always present in the vicinity of a growing species. Therefore, by selecting a combination of the central metal, a ligand and the like,
Since it is relatively easy to control the reactivity of the growing species and the direction of insertion of the monomer, it is considered that the polymerization method is more suitable for imparting the above-described functionality. For non-polar vinyl monomers such as ethylene, propylene, and styrene, stereoregular polymerization and living polymerization using organometallic complex catalysts have become possible based on this concept, and high functionality is achieved by controlling block polymers and terminal groups. The sex has been given.

【0004】極性基を有するビニルモノマーの有機金属
錯体触媒による重合については、極性基がしばしば触媒
毒となるため、対応する非極性ビニルモノマーの重合に
比べて著しく困難であり、その報告例は限られている。
現在まで知られている有機金属錯体触媒による極性ビニ
ルモノマーの単独重合を例示すると、(a)鉄、コバル
ト、ルテニウム錯体触媒による種々の極性ビニルモノマ
ーの重合(ジャーナル・オブ・ポリマー・サイエンス・
ポリマー・レビュウズ.,13,161(197
8))、(b)希土類錯体触媒によるメタクリル酸エス
テルの重合(ジャーナル・オブ・アメリカン・ケミカル
・ソサイエティ.,114,4908(1992))、
The polymerization of a vinyl monomer having a polar group with an organometallic complex catalyst is significantly more difficult than the polymerization of the corresponding non-polar vinyl monomer because the polar group often acts as a catalyst poison. Have been.
Examples of the homopolymerization of polar vinyl monomers with organometallic complex catalysts known to date include (a) polymerization of various polar vinyl monomers with iron, cobalt and ruthenium complex catalysts (Journal of Polymer Science.
Polymer Review. , 13, 161 (197
8)), (b) Polymerization of methacrylic acid ester with rare earth complex catalyst (Journal of American Chemical Society, 114, 4908 (1992)),

【0005】(c)希土類錯体触媒による極性ビニルモ
ノマーの重合(マクロモレキュールズ.,29,801
4(1996))、(d)ジルコノセン錯体とホウ素化
合物からなる触媒によるメタクリル酸エステルの重合
(マクロモレキュールズ.,28,3067(199
5))等が挙げられる。しかしながら、これらの錯体に
よる重合は、ほとんどがメタクリル酸エステル類のもの
であり、アクリロニトリルの重合例は少なく、重合速度
に関しても遅いものがほとんどである。また有効なモノ
マーの種類が比較的限られているものが多い。
(C) Polymerization of polar vinyl monomer by rare earth complex catalyst (Macromolecules., 29, 801)
4 (1996)), (d) Polymerization of methacrylic acid esters with a catalyst comprising a zirconocene complex and a boron compound (Macromolecules., 28, 3067 (199)
5)) and the like. However, most of the polymerization by these complexes is based on methacrylic esters, and there are few polymerization examples of acrylonitrile, and the polymerization rate is almost low. In many cases, the types of effective monomers are relatively limited.

【0006】[0006]

【発明が解決しようとする課題】本発明は、アクリロニ
トリル、メタクリル酸エステル等極性基を側鎖に有する
極性ビニルモノマー、およびスチレンなどの芳香族基を
側鎖に有するビニルモノマーなど多くの種類のモノマー
の重合が可能でかつ高い触媒活性を有する重合触媒及び
これらのビニルポリマーの製造方法を提供することをそ
の課題とする。
SUMMARY OF THE INVENTION The present invention is directed to a wide variety of monomers such as a polar vinyl monomer having a polar group such as acrylonitrile and methacrylate in a side chain and a vinyl monomer having an aromatic group such as styrene in a side chain. It is an object of the present invention to provide a polymerization catalyst capable of polymerizing a polymer and having a high catalytic activity, and a method for producing these vinyl polymers.

【0007】[0007]

【課題を解決するための手段】本発明者らは、前記課題
を解決すべく鋭意研究を行った結果、3座配位ホスフィ
ン配位子を含むコバルト錯体を用いるとアクリロニトリ
ル、メタクリロニトリル、アクリル酸メチル、メタクリ
ル酸メチル等の極性基を有するビニルモノマーやスチレ
ン等の芳香族基を側鎖に有するビニルモノマーなど広範
囲のモノマーから高重合度のポリマーが得られることを
見出して本発明を完成するに至った。
Means for Solving the Problems The inventors of the present invention have conducted intensive studies to solve the above-mentioned problems. As a result, when a cobalt complex containing a tridentate phosphine ligand is used, acrylonitrile, methacrylonitrile, acrylic The present invention is completed by finding that a polymer having a high degree of polymerization can be obtained from a wide range of monomers such as a vinyl monomer having a polar group such as methyl acrylate and methyl methacrylate and a vinyl monomer having an aromatic group such as styrene in a side chain. Reached.

【0008】すなわち、本発明は、3座配位ホスフィン
配位子を含むコバルト錯体からなることを特徴とする極
性ビニルモノマー重合用触媒である。また、本発明は、
上記極性ビニルモノマー重合用触媒の存在下、極性ビニ
ルモノマーを重合させることを特徴とする極性ビニルポ
リマーの製造方法である。
That is, the present invention is a catalyst for polymerizing a polar vinyl monomer, comprising a cobalt complex containing a tridentate phosphine ligand. Also, the present invention
A method for producing a polar vinyl polymer, comprising polymerizing a polar vinyl monomer in the presence of the catalyst for polymerizing a polar vinyl monomer.

【0009】[0009]

【発明の実施の形態】以下、本発明の実施の形態につい
て説明する。本発明の極性ビニルモノマー重合用触媒で
ある3座配位ホスフィン配位子を含有するコバルト錯体
とは、下記の一般式で表わされるものが例示出来る。 X(Cn2nY)3CoH(BH3) [式中、XはCH3C又はNを、YはPR12(R1:脂肪
族基又は芳香族基)又はP(0R2)2(R2:脂肪族基
又は芳香族基)を示し、nは1≦n≦3] これらのコバルト錯体の具体例としては、N(CH2
Ph23CoH(BH3),CH3C(CH2PPh23Co
H(BH3),CH3C(CH2P(C2523CoH
(BH3),CH3C(CH2P(OC2523CoH
(BH3),CH3C(CH2P(OPh)23CoH(B
3)等が挙げられる。これらの内で特に好ましいコバ
ルト錯体としては、CH3C(CH2PPh23CoH(B
3)(式中、Phはフェニル基である)で表されるもの
である。
Embodiments of the present invention will be described below. Examples of the cobalt complex containing a tridentate phosphine ligand which is a catalyst for polymerizing a polar vinyl monomer of the present invention include those represented by the following general formula. X (C n H 2n Y) 3 CoH (BH 3 ) wherein X is CH 3 C or N, and Y is PR 12 (R 1: aliphatic group or aromatic group) or P (0R 2 ) 2 (R 2 : Aliphatic group or aromatic group, and n is 1 ≦ n ≦ 3] Specific examples of these cobalt complexes include N (CH 2 P
Ph 2 ) 3 CoH (BH 3 ), CH 3 C (CH 2 PPh 2 ) 3 Co
H (BH 3 ), CH 3 C (CH 2 P (C 2 H 5 ) 2 ) 3 CoH
(BH 3 ), CH 3 C (CH 2 P (OC 2 H 5 ) 2 ) 3 CoH
(BH 3 ), CH 3 C (CH 2 P (OPh) 2 ) 3 CoH (B
H 3 ). Of these, particularly preferred cobalt complexes include CH 3 C (CH 2 PPh 2 ) 3 CoH (B
H 3 ), wherein Ph is a phenyl group.

【0010】本発明で適用可能な極性ビニルモノマー
は、シアノ基、カルボキシル基、アルコキシカルボニル
基、フェニル基等の極性基を側鎖に有するビニルモノマ
ーである。このようなものとしては、アクリロニトリ
ル、メタクリロニトリル、メタクリル酸エステル、アク
リル酸エステル、スチレン等があげられる。本発明の重
合用触媒は、特にアクリロニトリル、メタクリル酸メチ
ルを単独重合してそれらの極性ポリマーを製造するのに
適している。
The polar vinyl monomer applicable in the present invention is a vinyl monomer having a polar group such as a cyano group, a carboxyl group, an alkoxycarbonyl group, and a phenyl group in a side chain. Such materials include acrylonitrile, methacrylonitrile, methacrylate, acrylate, styrene and the like. The polymerization catalyst of the present invention is particularly suitable for homopolymerizing acrylonitrile and methyl methacrylate to produce their polar polymers.

【0011】本発明により極性ビニルポリマーを得るに
は、前記重合触媒の存在下、極性ビニルモノマーを重合
させる。この場合の重合反応は、無溶媒、あるいは重合
反応に対して不活性で重合時に液体である溶媒中で行う
のが望ましい。この場合の重合溶媒としては、ペンタ
ン、ヘキサン、ヘプタン等の飽和脂肪族炭化水素、シク
ロヘキサン、シクロヘプタン等の飽和環式炭化水素、ベ
ンゼン、トルエン等の芳香族炭化水素、N,N−ジメチ
ルホフムアミド(DMF)等の含窒素溶媒等が挙げられ
る。
In order to obtain a polar vinyl polymer according to the present invention, a polar vinyl monomer is polymerized in the presence of the polymerization catalyst. In this case, the polymerization reaction is desirably performed without a solvent or in a solvent that is inert to the polymerization reaction and is liquid at the time of polymerization. Examples of the polymerization solvent in this case include saturated aliphatic hydrocarbons such as pentane, hexane and heptane, saturated cyclic hydrocarbons such as cyclohexane and cycloheptane, aromatic hydrocarbons such as benzene and toluene, and N, N-dimethylhofm. Examples include a nitrogen-containing solvent such as amide (DMF).

【0012】前記極性ビニルモノマーを単独重合させる
際の触媒使用量は一概に規定できないが、例えば、極性
ビニルモノマー1モル当たり、Co錯体が1×10-4
ル〜1×10-2モルの割合である。また前記重合は、通
常0〜80℃で0.5〜100時間の範囲で行われる。
得られるポリマーの収率は、重合温度、重合時間、触媒
量、溶媒の種類及びその量等により変化するが、概ね6
0%以下である。さらにまた、得られるポリマーの数平
均分子量は、やはり重合条件等に依存するが、約100
0〜約1000000である。
The amount of the catalyst used for homopolymerizing the polar vinyl monomer cannot be specified unconditionally. For example, the ratio of the Co complex is 1 × 10 -4 mol to 1 × 10 -2 mol per mol of the polar vinyl monomer. It is. The polymerization is usually carried out at 0 to 80 ° C. for 0.5 to 100 hours.
The yield of the obtained polymer varies depending on the polymerization temperature, the polymerization time, the amount of the catalyst, the type and amount of the solvent, and the like.
0% or less. Furthermore, the number average molecular weight of the obtained polymer also depends on the polymerization conditions, etc.
0 to about 1,000,000.

【0013】[0013]

【実施例】以下、本発明を、実施例により具体的に説明
する。なお、重合体の分子量測定は、GPCを用い、展
開溶媒はN,N−ジメチルホルムアミド(DMF)、カ
ラム温度は40℃とした。測定された分子量は、ポリス
チレン換算である。
The present invention will be described below in more detail with reference to examples. The molecular weight of the polymer was measured using GPC, the developing solvent was N, N-dimethylformamide (DMF), and the column temperature was 40 ° C. The measured molecular weight is in terms of polystyrene.

【0014】実施例1 窒素ガスで十分に置換した20mLのフラスコに、DM
F3mL、アクリロニトリル3mL、7.5ミリモルの
CH3C(CH2PPh23CoH(BH3)を入れ、室温
で15分攪拌した。反応液を塩酸酸性メタノールに注ぎ
ポリマーを析出させ、これを乾燥したところ、仕込みモ
ノマーに対し49%のポリマーが得られた。生成したポ
リマーをGPC分析したところ、数平均分子量(Mn)
は520000であった。
Example 1 A 20 mL flask sufficiently purged with nitrogen gas was charged with DM.
3 mL of F, 3 mL of acrylonitrile, and 7.5 mmol of CH 3 C (CH 2 PPh 2 ) 3 CoH (BH 3 ) were added, and the mixture was stirred at room temperature for 15 minutes. The reaction solution was poured into hydrochloric acid-methanol to precipitate a polymer, and the polymer was dried. As a result, 49% of the polymer relative to the charged monomers was obtained. GPC analysis of the produced polymer showed a number average molecular weight (Mn).
Was 520000.

【0015】実施例2 実施例1と同様に、アクリロニトリルを室温で3分重合
したところ収率32%でポリマーが得られた。生成した
ポリマーをGPC分析したところ、数平均分子量(M
n)は500000であった。
Example 2 In the same manner as in Example 1, acrylonitrile was polymerized at room temperature for 3 minutes to obtain a polymer with a yield of 32%. GPC analysis of the resulting polymer revealed a number average molecular weight (M
n) was 500,000.

【0016】実施例3 実施例1と同様に、メタクリル酸メチルを室温で24時
間重合したところ収率23%でポリマーが得られた。生
成したポリマーをGPC分析したところ、数平均分子量
(Mn)は43000であった。
Example 3 In the same manner as in Example 1, when methyl methacrylate was polymerized at room temperature for 24 hours, a polymer was obtained with a yield of 23%. GPC analysis of the resulting polymer showed a number average molecular weight (Mn) of 43,000.

【0017】実施例4 実施例1と同様に、メタクリロニトリルを室温で3時間
重合したところ収率12%でポリマーが得られた。生成
したポリマーをGPC分析したところ、数平均分子量
(Mn)は35000であった。
Example 4 In the same manner as in Example 1, methacrylonitrile was polymerized at room temperature for 3 hours to obtain a polymer in a yield of 12%. GPC analysis of the resulting polymer showed a number average molecular weight (Mn) of 35,000.

【0018】実施例5 実施例1と同様に,スチレンを室温で24時間重合した
ところ収率15%でポリマーが得られた。生成したポリ
マーをGPC分析したところ、数平均分子量(Mn)は
15000であった。
Example 5 As in Example 1, styrene was polymerized at room temperature for 24 hours to obtain a polymer in a yield of 15%. GPC analysis of the resulting polymer showed a number average molecular weight (Mn) of 15,000.

【0019】各実施例の結果から明らかなように、本発
明の重合用触媒である3座配位ホスフィン配位子を含有
するコバルト錯体のCH3C(CH2PPh23CoH(B
3)は、これをアクリロニトリルやメタクリル酸エス
テル等の多くの種類の極性ビニルモノマーの重合に用い
ると、容易にポリマーを生成する。特にアクリロニトリ
ルの重合において非常に短時間に高分子量を有するポリ
マーを高い収率で生成する。
As is clear from the results of the examples, the cobalt complex containing a tridentate phosphine ligand, CH 3 C (CH 2 PPh 2 ) 3 CoH (B
H 3 ) readily produces polymers when used in the polymerization of many types of polar vinyl monomers, such as acrylonitrile and methacrylate. Particularly in the polymerization of acrylonitrile, a polymer having a high molecular weight is produced in a very short time in a high yield.

【0020】[0020]

【発明の効果】本発明の触媒は種々の極性ビニルモノマ
ーの重合に利用可能であり、且つ、良好な収率で極性ビ
ニルポリマーを得ることができる。
Industrial Applicability The catalyst of the present invention can be used for polymerization of various polar vinyl monomers, and a polar vinyl polymer can be obtained in a good yield.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 川辺 正直 茨城県つくば市竹園二丁目6番2−203号 (72)発明者 曽我 和雄 石川県能美郡辰口町緑が丘九丁目6番11号 (72)発明者 浅井 道彦 茨城県つくば市並木三丁目711 (72)発明者 鈴木 靖三 茨城県つくば市吾妻二丁目805−808号 (72)発明者 宮沢 哲 茨城県つくば市松代四丁目403−103号 (72)発明者 村田 昌英 東京都文教区水道二丁目3番15−504号 (72)発明者 加瀬 俊男 茨城県つくば市松代5−2−2 (72)発明者 尾崎 裕之 茨城県つくば市小野川四丁目6−202号 (72)発明者 福井 祥文 茨城県つくば市二の宮四丁目6番3−507 号 ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Masanao Kawabe 2-6-1203 Takezono, Tsukuba-shi, Ibaraki Prefecture (72) Inventor Kazuo Soga 9-6-1, Midorigaoka, Tatsunokuchi-cho, Nomi-gun, Ishikawa Prefecture (72) Inventor Michihiko Asai 3-711 Namiki, Tsukuba, Ibaraki Prefecture (72) Inventor Yasuzou Suzuki 2-805-808, Azuma, Tsukuba, Ibaraki (72) Inventor Tetsu Miyazawa 4-403, 103-103 Matsushiro, Matsushiro, Tsukuba, Ibaraki Prefecture ( 72) Inventor: Masahide Murata, 2-3-15-1, Suido, Bunkyo-ku, Tokyo (72) Inventor: Toshio Kase 5-2-2, Matsushiro, Tsukuba-shi, Ibaraki (72) Inventor: Hiroyuki Ozaki 4-chome Onogawa, Tsukuba-shi, Ibaraki No. 6-202 (72) Inventor Yoshifumi Fukui 4-6-1 Ninomiya 4-507, Tsukuba, Ibaraki Prefecture

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 3座配位ホスフィン配位子を含むコバル
ト錯体からなることを特徴とする極性ビニルモノマー重
合用触媒。
1. A catalyst for polymerizing a polar vinyl monomer, comprising a cobalt complex containing a tridentate phosphine ligand.
【請求項2】 コバルト錯体が、下記化学式 CH3C(CH2PPh23CoH(BH3) で表されるものである請求項1に記載の極性ビニルモノ
マー重合用触媒。
2. The catalyst for polymerizing a polar vinyl monomer according to claim 1, wherein the cobalt complex is represented by the following chemical formula: CH 3 C (CH 2 PPh 2 ) 3 CoH (BH 3 ).
【請求項3】 請求項1又は2に記載の重合用触媒の存
在下、極性ビニルモノマーを重合させることを特徴とす
る極性ビニルポリマーの製造方法。
3. A method for producing a polar vinyl polymer, comprising polymerizing a polar vinyl monomer in the presence of the polymerization catalyst according to claim 1 or 2.
JP13548598A 1998-05-18 1998-05-18 Catalyst for polymerizing polar vinyl monomer and production of polymer from the monomer Pending JPH11322835A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13548598A JPH11322835A (en) 1998-05-18 1998-05-18 Catalyst for polymerizing polar vinyl monomer and production of polymer from the monomer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13548598A JPH11322835A (en) 1998-05-18 1998-05-18 Catalyst for polymerizing polar vinyl monomer and production of polymer from the monomer

Publications (1)

Publication Number Publication Date
JPH11322835A true JPH11322835A (en) 1999-11-26

Family

ID=15152834

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13548598A Pending JPH11322835A (en) 1998-05-18 1998-05-18 Catalyst for polymerizing polar vinyl monomer and production of polymer from the monomer

Country Status (1)

Country Link
JP (1) JPH11322835A (en)

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