JP4288089B2 - (Meth) acrylic acid oligoolefin ester polymer and production method thereof - Google Patents

(Meth) acrylic acid oligoolefin ester polymer and production method thereof Download PDF

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JP4288089B2
JP4288089B2 JP2003072256A JP2003072256A JP4288089B2 JP 4288089 B2 JP4288089 B2 JP 4288089B2 JP 2003072256 A JP2003072256 A JP 2003072256A JP 2003072256 A JP2003072256 A JP 2003072256A JP 4288089 B2 JP4288089 B2 JP 4288089B2
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polymer
oligoolefin
meth
ester
acrylic acid
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JP2004277600A (en
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孝志 澤口
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San-Ei Kougyou Corp
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San-Ei Kougyou Corp
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Description

【0001】
【発明の属する技術分野】
本発明は、新規(メタ)アクリル酸オリゴオレフィン・エステル重合体およびその製造方法に関する。この重合体は、立体規則性に優れており光学活性体としての利用が期待される。
【0002】
Macromolecules, 22, 1546(1989)に、末端メタクリレート型の単分散性ポリスチレン・マクロモノマーのラジカル連鎖重合による生成ポリマーの重合度は、マクロモノマーの分子量と仕込み濃度に依存することが報告されている。この報告においては、スチレンモノマー単位の繰り返し数が10より大きいマクロモノマーが使用され、くし型構造を有するシンジオタクチックリッチのポリマーが得られている(非特許文献1参照)。
【0003】
ラジカル重合ハンドブック(エヌ・ティー・エス出版、234頁、(1999年))には、メタクリル酸エステルのラジカル重合において、得られるポリマーの立体規則性がエステル基の嵩高さにより変化し、たとえばトリフェニルメチル基や1−フェニルベンゾスペリル基のように比較的に平面的な広がりを持ったエステル基の場合、立体規則性の極めて優れたポリマーが得られることを記載している。
【0004】
本発明者等は、Journal of Polymer Science, Polym. Chem., 36, 209(1998)に、ポリスチレンを高度制御熱分解することにより、スチレンモノマー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高収率で得られることを報告した(非特許文献2参照)。
【0005】
【非特許文献1】
Macromolecules, 22, 1546(1989)
【非特許文献2】
Journal of Polymer Science, Polym. Chem., 36, 209(1998)
【0006】
【発明が解決しようとする課題】
上記片末端ビニリデン基含有オリゴオレフィンは、何らかの理由で未使用のまま廃棄され、漂着物などとして環境問題を提起している廃オレフィンを原料に製造することができ、また、末端ビニリデン基をヒドロキシ基、カルボキシ基、エポキシ基などの官能性基に変換することができる。しかしながら、現時点では、それらの有効な用途は見つかっていない。
【0007】
本発明は、ポリオレフィンの高度制御熱分解により得られる単分散性オリゴオレフィンの用途として、立体規則性(メタ)アクリル酸オリゴオレフィン・エステル重合体を提供することを目的とする。
【0008】
本発明は、一般式(1)
【化3】
(式中、Rは水素またはメチル基またはエチル基を表わし、R′は水素またはメチル基を表し、nは3〜20の整数を表わす)で表わされるモノマー単位を繰り返し単位とする(メタ)アクリル酸オリゴオレフィン・エステル重合体である。
【0009】
別の本発明は、一般式(2)
【化4】
(式中、R、R′およびnは前記定義したとおりの意味を表わす)で表わされる(メタ)アクリル酸オリゴオレフィン・エステルを、溶媒中において重合させることを特徴とする上記(メタ)アクリル酸オリゴオレフィン・エステル重合体の製造方法である。
【0010】
【発明の実施の形態】
本発明の(メタ)アクリル酸オリゴオレフィン・エステル重合体は、前記一般式(1)で表わされ、式中のオレフィン・モノマー単位の繰り返し数を表わすnが3〜20であるモノマー単位を繰り返し単位とする重合体である。たとえばメタクリル酸オリゴプロピレン・エステル重合体、メタクリル酸オリゴエチレン・エステル重合体、アクリル酸オリゴプロピレン・エステル重合体、アクリル酸オリゴエチレン・エステル重合体などの(メタ)アクリル酸オリゴオレフィン・エステル重合体である。
【0011】
これらの重合体は、たとえばメタクリル酸オリゴプロピレン・エステル重合体の場合、反応溶媒、たとえばベンゼン、トルエン、キシレンなどの芳香族有機溶媒に不溶性である。また、重合体のDSC測定では、常温で液体の重合体はガラス転移点(Tg)に相当する熱転移ピークは現れないが、反応溶媒に不溶性の重合体では、ガラス転移温度(Tg)に相当する明確な熱転移ピークを示す。
【0012】
本発明の重合体のこれらの特徴は、重合体が極めて高い立体規則性を有することを示している。
高い立体規則性を有する(メタ)アクリル酸エステル重合体はらせん構造をとることが知られているので、光学活性物質の分離担体としての利用が期待される。
【0013】
本発明の重合体は、前記一般式(2)で表わされる(メタ)アクリル酸オリゴオレフィン・エステルを、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。
【0014】
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。
【0015】
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。特に60℃より低い温度における反応では、反応初期から反応溶媒可溶性の重合体を経由することなくゲル状の反応溶媒不溶性重合体が得られる。
【0016】
本発明において、原料の前記一般式(2)で表わされる(メタ)アクリル酸オリゴオレフィン・エステルは、単分散性の末端ヒドロキシ基含有オリゴオレフィンと、(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容易に製造することができる。
【0017】
上記単分散性の末端ヒドロキシ基含有オリゴオレフィンは、単分散性の末端ビニリデン基含有オリゴオレフィンのビニリデン基を、常法により酸化することにより製造することができる。単分散性の末端ビニリデン基含有オリゴオレフィンは、The 2nd International Symposium on Feedstock Recycling of Plastics & Other Innovative Plastics Recycling Techniques , Ostend , Belgium(September 8-11 , 2002)Journal of Polymer Science, Polym. Chem., 36, 209(1998)等に記載した、ポリオレフィンの高度制御熱分解により高収率で製造することができる。
【0018】
【実施例】
実施例1
(メタ)アクリル酸オリゴプロピレン・エステルの製造
ポリプロピレンの高度制御熱分解生成物から再沈殿精製した前記一般式中のnが3〜20でi分子あたりに含まれる二重結合の平均数(ft)が1.1程度のオリゴプロピレン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オリゴプロピレン(PP−O−OH)を調製した。また、Sandor NemesらのPolymer Bulletin 29, 135-138(1992)に記載されている9−BBNを用いる手法によっても製造することができる。
【0019】
次いで、得られたPP−O−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、分取GPCを用い精製してメタクリル酸オリゴプロピレン・エステル(PP−O−MC)およびアクリル酸オリゴプロピレン・エステル(PP−O−AC)を調製した。
得られたPP−O−MCおよびPP−O−AC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。
PP−O−MCおよびPP−O−ACの収率は、いずれも約70重量%であった。
【0020】
実施例2
メタクリル酸オリゴプロピレン・エステル(PP−O−MC)の重合
上記調製したPP−O−MCを、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ナスフラスコに仕込み、凍結、脱気、窒素置換を繰返した後密封し、反応温度を80℃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。
【0021】
回収時には重合溶液は全てゲル状になっており、回収された重合体は全て反応溶媒に不溶性であった。
【0022】
無溶媒で得られた重合体はガラス転移温度(Tg)が41.8であったが、反応溶媒を加えることでガラス転移温度(Tg)が急激に上がり、さらに反応溶媒の増加に伴い上昇するという傾向が見られた。
反応条件および得られた重合体の特性を表1に示す。
【0023】
【表1】
【0024】
得られた重合体は全て接着性を示した。特に試料番号4の重合体はプラスチック(PS、PP、PE、PMMA等)、金属類、ガラス、素肌、衣類等あらゆる物に対して接着性を示した。
【発明の効果】
本発明は、上記実施例に示したように、高立体規則性の新規(メタ)アクリル酸オリゴオレフィン・エステル重合体を提供する。この重合体はリボン構造を有することから、光学活性物質の分離担体として利用することができる。
また、その製造原料として、廃ポリマーの高度制御熱分解によって得られるオリゴオレフィンを使用できるので、環境問題の解決に役立つ。
【図面の簡単な説明】
【図1】実施例1で合成されたPP−O−MCの1H−NMRスペクトルを示す。
【図2】実施例1で合成されたPP−O−ACの1H−NMRスペクトルを示す。
【図3】実施例2の場合におけるPP−O−MCの重合曲線を示す。
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a novel (meth) acrylic acid oligoolefin ester polymer and a method for producing the same. This polymer is excellent in stereoregularity and is expected to be used as an optically active substance.
[0002]
Macromolecules, 22, 1546 (1989) reports that the degree of polymerization of a polymer produced by radical chain polymerization of a terminal-dispersed monodisperse polystyrene-macromonomer depends on the molecular weight of the macromonomer and the charged concentration. In this report, a macromonomer having a repeating number of styrene monomer units larger than 10 is used, and a syndiotactic rich polymer having a comb structure is obtained (see Non-Patent Document 1).
[0003]
In the radical polymerization handbook (NTS Publishing, page 234, (1999)), the stereoregularity of the polymer obtained in radical polymerization of methacrylic acid ester varies depending on the bulk of the ester group. In the case of an ester group having a relatively planar spread such as a methyl group or 1-phenylbenzosperyl group, it is described that a polymer with extremely excellent stereoregularity can be obtained.
[0004]
The inventors of the present invention have reported in Journal of Polymer Science, Polym. Chem., 36, 209 (1998) that a monodispersed polymer having a repeating number of styrene monomer units of about 2 to 10 by highly controlled pyrolysis of polystyrene. It was reported that oligostyrene containing one-end vinylidene group was obtained in high yield (see Non-Patent Document 2).
[0005]
[Non-Patent Document 1]
Macromolecules, 22, 1546 (1989)
[Non-Patent Document 2]
Journal of Polymer Science, Polym. Chem., 36, 209 (1998)
[0006]
[Problems to be solved by the invention]
The above-mentioned one-end vinylidene group-containing oligoolefin can be produced from waste olefin that has been discarded for some reason and has caused environmental problems as an adhering material, etc. Can be converted into a functional group such as a carboxy group or an epoxy group. However, at present, their effective use has not been found.
[0007]
An object of the present invention is to provide a stereoregular (meth) acrylic oligoolefin ester polymer as a use of a monodisperse oligoolefin obtained by highly controlled pyrolysis of polyolefin.
[0008]
The present invention relates to a general formula (1)
[Chemical 3]
(Wherein R represents hydrogen, a methyl group or an ethyl group, R ′ represents hydrogen or a methyl group, and n represents an integer of 3 to 20). It is an acid oligoolefin ester polymer.
[0009]
Another aspect of the present invention is a compound of the general formula (2)
[Formula 4]
(Wherein R, R ′ and n represent the meanings as defined above), and the (meth) acrylic acid is polymerized in a solvent. This is a method for producing an oligoolefin ester polymer.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
The (meth) acrylic acid oligoolefin / ester polymer of the present invention is represented by the general formula (1), wherein n represents the number of repeating olefin / monomer units in the formula, and n is a repeating unit of 3-20. A polymer as a unit. For example, (meth) acrylic oligoolefin / ester polymers such as methacrylic acid oligopropylene / ester polymer, methacrylic acid oligoethylene / ester polymer, acrylic acid oligopropylene / ester polymer, acrylic acid oligoethylene / ester polymer, etc. is there.
[0011]
These polymers are insoluble in reaction solvents such as aromatic organic solvents such as benzene, toluene and xylene in the case of, for example, methacrylic acid oligopropylene ester polymers. Moreover, in the DSC measurement of the polymer, the thermal transition peak corresponding to the glass transition point (Tg) does not appear in the polymer that is liquid at normal temperature, but the polymer that is insoluble in the reaction solvent corresponds to the glass transition temperature (Tg). Show a distinct thermal transition peak.
[0012]
These characteristics of the polymer of the present invention indicate that the polymer has a very high stereoregularity.
Since a (meth) acrylic acid ester polymer having high stereoregularity is known to have a helical structure, it is expected to be used as a separation carrier for optically active substances.
[0013]
The polymer of the present invention is obtained by polymerizing the (meth) acrylic oligoolefin ester represented by the general formula (2) in an organic solvent, preferably an aromatic solvent such as benzene, toluene, xylene, etc. It can be manufactured easily.
[0014]
There is no restriction | limiting in particular in a polymerization method, Well-known polymerization methods, such as ion polymerization, such as radical polymerization and anion polymerization, and superposition | polymerization by an organometallic compound, are employable. Preferably, radical polymerization or anionic polymerization is employed.
[0015]
For example, in the case of radical polymerization using azobisisobutyronitrile (AIBN) as a radical initiator, a reaction solvent-insoluble polymer is obtained in a high yield by reacting at room temperature to 80 ° C. for 60 minutes to 25 hours. Can be obtained at In particular, in a reaction at a temperature lower than 60 ° C., a gel-like reaction solvent-insoluble polymer can be obtained without going through the reaction solvent-soluble polymer from the beginning of the reaction.
[0016]
In the present invention, the raw material (meth) acrylic acid oligoolefin ester represented by the general formula (2) is a monodispersed terminal hydroxy group-containing oligoolefin and (meth) acrylic acid or (meth) acrylic acid salt. It can be easily produced by reacting a product with a conventional method.
[0017]
The monodispersed terminal hydroxy group-containing oligoolefin can be produced by oxidizing the vinylidene group of the monodispersed terminal vinylidene group-containing oligoolefin by a conventional method. Terminal vinylidene group containing oligoolefin of monodispersity, The 2 nd International Symposium on Feedstock Recycling of Plastics & Other Innovative Plastics Recycling Techniques, Ostend, Belgium (September 8-11, 2002) Journal of Polymer Science, Polym. Chem., 36, 209 (1998) and the like, and can be produced in high yield by highly controlled pyrolysis of polyolefin.
[0018]
【Example】
Example 1
Production of (meth) acrylic acid oligopropylene ester Average of double bonds contained per i molecule, wherein n is 3 to 20 in the above general formula and purified by reprecipitation from a highly controlled pyrolysis product of polypropylene Oligopropylene having a number (ft) of about 1.1 was hydroborated and then oxidized with an aqueous sodium hydroxide solution and hydrogen peroxide to prepare terminal hydroxy group-containing oligopropylene (PP-O-OH). Further, it can also be produced by a technique using 9-BBN described in Polymer Bulletin 29, 135-138 (1992) of Sandor Nemes et al.
[0019]
Subsequently, the obtained trimethylamine / dichloromethane solution of PP-O—OH was added dropwise to a dichloromethane solution of methacryloyl chloride or acryloyl chloride at −5 ° C., and the obtained reaction product was purified using preparative GPC. A methacrylic acid oligopropylene ester (PP-O-MC) and an acrylic acid oligopropylene ester (PP-O-AC) were prepared.
The obtained PP-O-MC and PP-O-AC were all confirmed to have the structure of the general formula (2) by IR spectrum, 1 H-NMR spectrum and 13 C-NMR spectrum.
The yields of PP-O-MC and PP-O-AC were both about 70% by weight.
[0020]
Example 2
Polymerization of methacrylic acid oligopropylene ester (PP-O-MC) The above-prepared PP-O-MC together with a radical initiator azobisisobutyronitrile (AIBN) and a reaction solvent benzene is an eggplant flask. Then, after repeating freezing, degassing, and nitrogen substitution, the mixture was sealed, the reaction temperature was set to 80 ° C., and the polymerization was started. The resulting polymer was recovered by reprecipitation or as a precipitate.
[0021]
At the time of recovery, the polymerization solution was in a gel state, and all of the recovered polymer was insoluble in the reaction solvent.
[0022]
The polymer obtained without solvent had a glass transition temperature (Tg) of 41.8, but the glass transition temperature (Tg) was rapidly increased by adding the reaction solvent, and further increased with an increase in the reaction solvent. The tendency was seen.
Table 1 shows reaction conditions and characteristics of the obtained polymer.
[0023]
[Table 1]
[0024]
All the obtained polymers showed adhesiveness. In particular, the polymer of Sample No. 4 showed adhesion to plastics (PS, PP, PE, PMMA, etc.), metals, glass, bare skin, clothing and other objects.
【The invention's effect】
The present invention provides a novel (meth) acrylic acid oligoolefin ester polymer having high stereoregularity as shown in the above examples. Since this polymer has a ribbon structure, it can be used as a separation carrier for optically active substances.
Moreover, since the oligoolefin obtained by highly controlled pyrolysis of a waste polymer can be used as the manufacturing raw material, it helps to solve an environmental problem.
[Brief description of the drawings]
1 shows the 1 H-NMR spectrum of PP-O-MC synthesized in Example 1. FIG.
2 shows a 1 H-NMR spectrum of PP-O-AC synthesized in Example 1. FIG.
3 shows a polymerization curve of PP-O-MC in the case of Example 2. FIG.

Claims (2)

下記一般式(1)
(式中、Rはメチル基を表わし、R′は水素またはメチル基を表し、nは3〜20の整数を表わす)で表わされるモノマー単位を繰り返し単位とする(メタ)アクリル酸オリゴオレフィン・エステル重合体。
The following general formula (1)
(Wherein R represents a methyl group, R ′ represents hydrogen or a methyl group, and n represents an integer of 3 to 20) (meth) acrylic oligoolefin ester having a monomer unit as a repeating unit Polymer.
下記一般式(2)
(式中、Rはメチル基を表わし、R′は水素またはメチル基を表し、nは3〜20の整数を表わす)で表わされる(メタ)アクリル酸オリゴオレフィン・エステルを、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)アクリル酸オリゴオレフィン・エステル重合体の製造方法。
The following general formula (2)
(In the formula, R represents a methyl group, R 'represents hydrogen or a methyl group, and n represents an integer of 3 to 20), and a (meth) acrylic oligoolefin ester represented by polymerization is polymerized in an organic solvent. The method for producing a (meth) acrylic oligoolefin ester polymer according to claim 1, wherein:
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