JPH059273A - Copolyester and method for producing the same - Google Patents
Copolyester and method for producing the sameInfo
- Publication number
- JPH059273A JPH059273A JP16069791A JP16069791A JPH059273A JP H059273 A JPH059273 A JP H059273A JP 16069791 A JP16069791 A JP 16069791A JP 16069791 A JP16069791 A JP 16069791A JP H059273 A JPH059273 A JP H059273A
- Authority
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- Japan
- Prior art keywords
- formula
- copolyester
- molecular weight
- group
- general formula
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- Biological Depolymerization Polymers (AREA)
Abstract
(57)【要約】
【目的】生分解性ポリマーである共重合ポリエステルを
提供する。
【構成】下記構造単位〔I〕及び〔II〕からなり、
〔I〕/〔II〕=97/3〜3/97(モル比)であ
り、重量平均分子量が1万以上の共重合ポリエステル及
び該ポリエステルを下記一般式〔II〕及び〔IV〕で
表される化合物を重合することにより製造する方法
【化1】
(57) [Summary] [Object] To provide a copolyester which is a biodegradable polymer. [Structure] Consists of the following structural units [I] and [II],
[I] / [II] = 97/3 to 3/97 (molar ratio), a weight average molecular weight of 10,000 or more copolymerized polyester and the polyester are represented by the following general formulas [II] and [IV]. A method for producing the compound by polymerizing
Description
【0001】[0001]
【産業上の利用分野】本発明は環境問題対策用高分子材
料および医用高分子材料として期待されている生分解性
ポリマーである共重合ポリエステルおよびその製造法に
関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a copolyester which is a biodegradable polymer expected as a polymeric material for environmental problems and a medical polymeric material, and a method for producing the same.
【0002】[0002]
【従来の技術】環境問題対策用高分子材料および医用高
分子材料として生分解性ポリマーが検討されている。下
記式〔I〕および下記式〔II〕の構成単位からなる共
重合ポリエステルとして、乳酸およびマンデル酸を直接
的に共重合させることは知られている(H.Fuknz
aki Eur.Poly.J.26,1273(19
90) )。2. Description of the Related Art Biodegradable polymers have been investigated as polymeric materials for environmental problems and medical polymeric materials. It is known that lactic acid and mandelic acid are directly copolymerized as a copolymerized polyester composed of structural units of the following formula [I] and the following formula [II] (H. Fuknz
aki Eur. Poly. J. 26, 1273 (19
90)).
【0003】[0003]
【発明が解決しようとする課題】しかし上記製造法によ
る共重合ポリエステルの分子量は5,000以下であ
り、ドラッグデリバリーシステム(DDS)には利用で
きるが、環境問題対策用または医用高分子材料として広
く利用できない。これら用途として広く利用するため
に、より高分子量の重合体の製造法の開発が期待されて
いた。However, the copolymerized polyester produced by the above-mentioned production method has a molecular weight of 5,000 or less, and although it can be used in a drug delivery system (DDS), it is widely used as a polymer material for environmental protection or medical use. Not available. Development of a method for producing a polymer having a higher molecular weight has been expected to be widely used for these purposes.
【0004】[0004]
【課題を解決するための手段】そのため、上記2種の構
成単位を有する重合体の製造法を鋭意検討した結果、下
記一般式〔III〕および下記一般式〔IV〕で表され
る化合物を触媒の存在下で共重合することによって、よ
り容易に高分子量の重合体を製造できることがわかり、
本発明に到達した。すなわち、本発明の要旨は下記一般
式〔I〕の単位
−O−CHR−CO− 〔I〕
(式〔I〕中、Rは水素原子または炭素数1〜5のアル
キル基を示す)および下記一般式〔II〕の単位
−O−CHAr−CO− 〔II〕
(式〔II〕中、Arはフェニル基であり、アルキル、
アルコキシ、アセチル、アセトキシ、ハロゲン、ニトロ
またはフェニル基で置換されていてもよい。)を構成単
位とし、〔I〕/〔II〕のモル比率が97/3〜3/
97であり、重量平均分子量が10,000以上である
ことを特徴とする共重合ポリエステルおよびび一般式
〔III〕で表される化合物Therefore, as a result of diligent studies on a method for producing a polymer having the above-mentioned two kinds of constitutional units, the compound represented by the following general formula [III] and the following general formula [IV] was used as a catalyst. It was found that a high molecular weight polymer can be produced more easily by copolymerizing in the presence of
The present invention has been reached. That is, the gist of the present invention is a unit of the following general formula [I], —O—CHR—CO— [I] (in the formula [I], R represents a hydrogen atom or an alkyl group having 1 to 5 carbon atoms) and the following: Unit of the general formula [II] —O—CHAr—CO— [II] (In the formula [II], Ar is a phenyl group, alkyl,
It may be substituted with alkoxy, acetyl, acetoxy, halogen, nitro or phenyl groups. ) As a structural unit, and the molar ratio [I] / [II] is 97/3 to 3 /
97, and a weight average molecular weight of 10,000 or more, a copolyester and a compound represented by the general formula [III]
【0005】[0005]
【化3】 [Chemical 3]
【0006】(式〔III〕Rは式〔I〕と同じ)およ
び一般式〔IV〕で表される化合物(Formula [III] R is the same as formula [I]) and compounds represented by general formula [IV]
【0007】[0007]
【化4】 [Chemical 4]
【0008】(式〔IV〕中、Arは式〔II〕と同
じ)を触媒の存在下で重合することを特徴とする上記の
共重合ポリエステルの製造法に存する。(Wherein Ar is the same as in the formula [II] in the formula [IV]) is polymerized in the presence of a catalyst.
【0009】以下に本発明を詳細に説明する。本発明の
重合反応は触媒の存在下で行われるが、使用できる触媒
の具体例としてはスズ化合物、アルミニウム化合物、ア
ンチモン化合物、チタン化合物などが挙げられ、特にス
ズ化合物が好ましい。また重合反応は溶媒の存在下また
は不存在下で行われるが、溶媒を使用する場合は一般式
〔III〕、〔IV〕で表される化合物を溶解するもの
で、触媒を不活性化しないものならばいずれも使用可能
である。具体例としてはテトラヒドロフラン、クロロホ
ルム、オルトジクロルベンゼン、ジオキサンなどが挙げ
られる。The present invention will be described in detail below. The polymerization reaction of the present invention is carried out in the presence of a catalyst, and specific examples of the catalyst that can be used include tin compounds, aluminum compounds, antimony compounds and titanium compounds, and tin compounds are particularly preferable. The polymerization reaction is carried out in the presence or absence of a solvent. When a solvent is used, it dissolves the compound represented by the general formula [III] or [IV] and does not inactivate the catalyst. If so, both can be used. Specific examples include tetrahydrofuran, chloroform, orthodichlorobenzene, dioxane and the like.
【0010】共重合体の組成は式〔II〕の構成単位が
3〜97モル%、好ましくは3〜50モル%、より好ま
しくは5〜30モル%である。式〔II〕の構成単位が
多い場合には共重合体の生分解性が悪化するため好まし
くなく、式〔II〕の構成単位が少ない場合には共重合
体の機械的特性が低下するため好ましくない。The composition of the copolymer is such that the constitutional unit of the formula [II] is 3 to 97 mol%, preferably 3 to 50 mol%, more preferably 5 to 30 mol%. When the amount of the structural unit of the formula [II] is large, the biodegradability of the copolymer is deteriorated, which is not preferable. When the amount of the structural unit of the formula [II] is small, the mechanical properties of the copolymer are deteriorated. Absent.
【0011】重合温度は0〜300℃、好ましくは50
〜250℃である。一般式〔III〕で表される化合物
としてはラクチド、グリコリドの他にRがエチル基、イ
ソプロピル基、n−プロピル基、n−ブチル基などの化
合物が挙げられる。原料入手の容易さからラクチドが好
ましい。一般式〔IV〕で表わされる化合物としてはマ
ンデリドの他にAr基がp−トリル基、2,4−キシリ
ル基、p−メトキシフェニル基、2,5−ジクロロフェ
ニル基などの化合物が挙げられる。特にマンデリドが好
ましい。The polymerization temperature is 0 to 300 ° C., preferably 50.
~ 250 ° C. Examples of the compound represented by the general formula [III] include compounds in which R is an ethyl group, an isopropyl group, an n-propyl group, an n-butyl group, and the like in addition to lactide and glycolide. Lactide is preferred because of easy availability of raw materials. Examples of the compound represented by the general formula [IV] include compounds in which the Ar group is a p-tolyl group, a 2,4-xylyl group, a p-methoxyphenyl group, a 2,5-dichlorophenyl group, and the like in addition to mandelide. Mandelid is particularly preferred.
【0012】分子量は一般にポリマーを成型材料として
使用する場合には、重量平均分子量として、10,00
0以上好ましくは20,000以上、より好ましくは3
0,000以上の重合度のものが、初期の力学的性質か
ら要求される。一般式〔III〕および〔IV〕で表わ
される化合物を触媒の存在下で重合させる本発明の方法
により、重量平均分子量が10,000以上の一般式
〔I〕および式〔II〕を構成単位とする共重合ポリエ
ステルが容易に得られる。The molecular weight is generally 10,000 as a weight average molecular weight when a polymer is used as a molding material.
0 or more, preferably 20,000 or more, more preferably 3
A polymer having a degree of polymerization of 10,000 or more is required due to its initial mechanical properties. By the method of the present invention in which the compounds represented by the general formulas [III] and [IV] are polymerized in the presence of a catalyst, the general formula [I] and the formula [II] having a weight average molecular weight of 10,000 or more are regarded as constitutional units. A copolymerized polyester that can be easily obtained.
【0013】[0013]
【実施例】以下に実施例により、より具体的に説明する
が、本発明はその要旨を越えない限り以下の実施例に限
定されるものではない。
実施例1 マンデリトの合成
還流冷却器、Dean−Starkトラップをつけた5
00mlフラスコ中にベンゼン200ml、L−マンデ
ル酸23.7g(150ミリモル)、p−トルエンスル
ホン酸1.05g(5.4ミリモル)を加え還流した。
トラップに溜った水は随時取り除いた。60時間還流
後、懸濁液を熱時濾過し、濾物をジクロロメタンで洗浄
し、乾燥し、白色の粉末を得た。生成物及び原料のIR
およびNMRを図1および図2に示す。1H−NMRで
は6.85ppmにシングレットのCH、7.6ppm
にマルティプレットのC6H5の吸収があった。EXAMPLES The present invention will be described in more detail with reference to the following examples, but the present invention is not limited to the following examples as long as the gist thereof is not exceeded. Example 1 Mandelito's Synthetic Reflux Cooler, equipped with a Dean-Stark trap 5
200 ml of benzene, 23.7 g (150 mmol) of L-mandelic acid and 1.05 g (5.4 mmol) of p-toluenesulfonic acid were added to a 00 ml flask and refluxed.
The water accumulated in the trap was removed at any time. After refluxing for 60 hours, the suspension was filtered while hot, and the residue was washed with dichloromethane and dried to obtain a white powder. IR of products and raw materials
And NMR are shown in FIGS. 1 and 2. 1 H-NMR shows 6.85 ppm of singlet CH, 7.6 ppm
There was absorption of C 6 H 5 by Martipret.
【0014】実施例2 共重合ポリエステルの合成
マンデリド0.5g、l−ラクチド2.42gを加えて
窒素置換し、200℃に昇温して溶融後、オクチル酸ス
ズ0.753gを加えた。反応系を1mmHgに減圧
し、1.5時間同温度で加熱した。反応後生成物をクロ
ロホルム15mlに溶解し、エーテル200ml中に再
沈澱させた。得られた収量は2.4gで収率は83%で
あった。その後デカンテーションでエーテルを除き、乾
燥し粉末状の共重合体を得た。重クロロホルム中で測定
した1H−NMRを図3に示す。1.58ppmにダブ
レットのピークが、5.16ppmにカルテットのピー
クが、6.04ppmにブロードなピークが、7.42
ppmにブロードなマルチプレットのピークが見出され
た。共重合体の数平均分子量は18,000であり、重
量平均分子量は40,000であった。分子量はゲルパ
ーミエーションクロマトグラフィー(GPC)により求
めた。GPCは東ソー製HLC−802A型を用い、カ
ラムとしてTSKゲルG4000H8を、データプロセ
ッサーとしてTSK−CP8000を用いて行った。な
お、測定の検出器としてはRIディテクターを使用し
た。溶媒はテトラヒドロフランを使用し、38℃で測定
した。Example 2 Synthesis of Copolymerized Polyester 0.5 g of mandelide and 2.42 g of 1-lactide were added and the atmosphere was replaced with nitrogen. After heating to 200 ° C. and melting, 0.753 g of tin octylate was added. The reaction system was depressurized to 1 mmHg and heated at the same temperature for 1.5 hours. After the reaction, the product was dissolved in 15 ml of chloroform and reprecipitated in 200 ml of ether. The obtained amount was 2.4 g and the yield was 83%. After that, ether was removed by decantation and dried to obtain a powdery copolymer. 1 H-NMR measured in deuterated chloroform is shown in FIG. The doublet peak at 1.58 ppm, the quartet peak at 5.16 ppm, and the broad peak at 6.04 ppm are 7.42.
A broad multiplet peak was found at ppm. The number average molecular weight of the copolymer was 18,000 and the weight average molecular weight was 40,000. The molecular weight was determined by gel permeation chromatography (GPC). GPC was performed using Tosoh HLC-802A type, TSK gel G4000H8 was used as a column, and TSK-CP8000 was used as a data processor. An RI detector was used as a detector for measurement. Tetrahydrofuran was used as the solvent, and the temperature was measured at 38 ° C.
【0015】[0015]
【発明の効果】本発明の高分子量の共重合ポリエステル
は、従来の低分子量の共重合ポリエステルと違い、十分
な機械的特性があるために、広範囲の成型材料として利
用できる。更に本発明の製造法により、成型材料として
有用な高分子量の生分解性の共重合ポリエステルが容易
に製造できるようになった。EFFECT OF THE INVENTION The high molecular weight copolyester of the present invention, unlike the conventional low molecular weight copolyester, has sufficient mechanical properties and can be used as a wide range of molding materials. Further, according to the production method of the present invention, a high-molecular-weight biodegradable copolyester useful as a molding material can be easily produced.
【図1】実施例1における生成物および原料のIRスペ
クトル図FIG. 1 is an IR spectrum diagram of a product and a raw material in Example 1.
【図2】実施例1における生成物および原料1H−NM
Rスペクトル図FIG. 2 Product and raw material 1 H-NM in Example 1
R spectrum diagram
【図3】実施例2における生成物の1H−NMRスペク
トル図FIG. 3 is a 1 H-NMR spectrum diagram of the product in Example 2.
Claims (2)
キル基を示す)および下記式〔II〕の単位 −O−CHAr−CO− 〔II〕 (式〔II〕中、Arはフェニル基であり、アルキル、
アルコキシ、アセチル、アセトキシ、ハロゲン、ニトロ
またはフェニル基で置換されていてもよい。)を構成単
位とし、〔I〕/〔II〕のモル比率が97/3〜3/
97であり、重量平均分子量が10,000以上である
ことを特徴とする共重合ポリエステル。1. A unit of the following formula [I], —O—CHR—CO— [I] (in the formula [I], R represents a hydrogen atom or an alkyl group having 1 to 5 carbon atoms) and the following formula [II] ] -O-CHAr-CO- [II] (In formula [II], Ar is a phenyl group, alkyl,
It may be substituted with alkoxy, acetyl, acetoxy, halogen, nitro or phenyl groups. ) As a structural unit, and the molar ratio [I] / [II] is 97/3 to 3 /
97, and the weight average molecular weight is 10,000 or more, The copolyester characterized by the above-mentioned.
アルキル基を示す。)および一般式〔IV〕で表わされ
る化合物 【化2】 (式〔IV〕中、Arはフェニル基であり、アルキル、
アルコキシ、アセチル、アセトキシ、ハロゲン、ニトロ
またはフェニル基で置換されていてもよい。)を触媒の
存在下で重合することを特徴とする請求項1記載の共重
合ポリエステルの製造法。2. A compound represented by the general formula [III]: (In the formula [III], R represents a hydrogen atom or an alkyl group having 1 to 5 carbon atoms) and a compound represented by the general formula [IV]: (In the formula [IV], Ar is a phenyl group, alkyl,
It may be substituted with alkoxy, acetyl, acetoxy, halogen, nitro or phenyl groups. 2.) The method for producing a copolyester according to claim 1, wherein the polymerization is carried out in the presence of a catalyst.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16069791A JPH059273A (en) | 1991-07-01 | 1991-07-01 | Copolyester and method for producing the same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16069791A JPH059273A (en) | 1991-07-01 | 1991-07-01 | Copolyester and method for producing the same |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH059273A true JPH059273A (en) | 1993-01-19 |
Family
ID=15720518
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16069791A Pending JPH059273A (en) | 1991-07-01 | 1991-07-01 | Copolyester and method for producing the same |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH059273A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2001042333A3 (en) * | 1999-12-13 | 2001-12-06 | Univ Michigan State | Process for the preparation of polymers of dimeric cyclic esters |
JP2006225622A (en) * | 2005-02-20 | 2006-08-31 | Yoshiharu Kimura | Polymer and method for producing the same |
JP2009046552A (en) * | 2007-08-17 | 2009-03-05 | Kyoto Institute Of Technology | Composition and film |
-
1991
- 1991-07-01 JP JP16069791A patent/JPH059273A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2001042333A3 (en) * | 1999-12-13 | 2001-12-06 | Univ Michigan State | Process for the preparation of polymers of dimeric cyclic esters |
US6469133B2 (en) * | 1999-12-13 | 2002-10-22 | Board Of Trustees Of Michigan State University | Process for the preparation of polymers of dimeric cyclic esters |
JP2006225622A (en) * | 2005-02-20 | 2006-08-31 | Yoshiharu Kimura | Polymer and method for producing the same |
JP2009046552A (en) * | 2007-08-17 | 2009-03-05 | Kyoto Institute Of Technology | Composition and film |
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