JP2002138142A - Method of producing polyhydroxycarboxylic acid - Google Patents

Method of producing polyhydroxycarboxylic acid

Info

Publication number
JP2002138142A
JP2002138142A JP2000333399A JP2000333399A JP2002138142A JP 2002138142 A JP2002138142 A JP 2002138142A JP 2000333399 A JP2000333399 A JP 2000333399A JP 2000333399 A JP2000333399 A JP 2000333399A JP 2002138142 A JP2002138142 A JP 2002138142A
Authority
JP
Japan
Prior art keywords
acid
producing
polyhydroxycarboxylic
hydroxycarboxylic
mixture
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.)
Granted
Application number
JP2000333399A
Other languages
Japanese (ja)
Other versions
JP3745612B2 (en
Inventor
Nobuyuki Sakuta
信幸 作田
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.)
Nishikawa Rubber Co Ltd
Original Assignee
Nishikawa Rubber 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 Nishikawa Rubber Co Ltd filed Critical Nishikawa Rubber Co Ltd
Priority to JP2000333399A priority Critical patent/JP3745612B2/en
Publication of JP2002138142A publication Critical patent/JP2002138142A/en
Application granted granted Critical
Publication of JP3745612B2 publication Critical patent/JP3745612B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a method of producing a biodegradable polyhydroxycarboxylic acid using a polymerization catalyst for polymerizing a hydroxycarboxylic acid such as lactic acid which scarcely affects environment even when dumped in the natural surroundings without recollecting after use, and further even if remaining in the product, does not cause a reaction with a drug or a harmful reaction in the living body. SOLUTION: This method of producing a high molecular weight polylactic acid or a lactic acid-sugar copolymer comprises adding phosphoric acid aqueous solution as a polymerization catalyst to L-lactic acid or a mixture of L-lactic acid and corn starch, and heating with agitation under reduced pressure or in the presence of an organic solvent such as D-limonene.

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】本発明はヒドロキシカルボン
酸の単独重合体または共重合体であるポリヒドロキシカ
ルボン酸、とくに生分解性樹脂の製造方法に関するもの
である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a polyhydroxycarboxylic acid which is a homopolymer or a copolymer of a hydroxycarboxylic acid, in particular, a biodegradable resin.

【0002】[0002]

【従来の技術】従来、種々の樹脂成形物が農業・園芸用
資材(例えばポリ塩化ビニルフィルム)及び漁業用資材
(例えばポリエチレン繊維の漁網)として用いられてい
るが、これらの資材はいずれは廃棄されるものである。
したがって、廃棄されても環境を汚染することなく、時
間の経過とともに加水分解されるか又は土中の微生物に
より生分解される樹脂が要望されている。本発明者らは
先に、このような農業・園芸用資材、漁業用資材などに
利用でき、使用後に廃棄されても土中の微生物などによ
り二酸化炭素と水に分解されるポリヒドロキシカルボン
酸を容易に製造する方法を発明した。
2. Description of the Related Art Conventionally, various resin moldings have been used as agricultural and horticultural materials (for example, polyvinyl chloride film) and fishery materials (for example, fishing nets made of polyethylene fiber). Is what is done.
Therefore, there is a need for a resin that is hydrolyzed with time or biodegraded by microorganisms in the soil without polluting the environment even when discarded. The present inventors have previously made polyhydroxycarboxylic acids that can be used for such agricultural and horticultural materials, fishing materials, etc., and that are decomposed into carbon dioxide and water by microorganisms in the soil even if disposed after use. A method for easy manufacture has been invented.

【0003】[0003]

【発明が解決しようとする課題】ところで、ポリ乳酸に
代表されるポリヒドロキシカルボン酸は将来的に大きな
需要が見込まれる生分解性樹脂であるが、従来の製造方
法において使用される重合触媒は1,3−置換−1,
1,3,3−テトラオルガノジスタノキサン等の有機金
属化合物であり、使用後回収されずに自然環境中に廃棄
された場合、環境に及ぼす影響が大きいという問題点が
あった。
By the way, polyhydroxycarboxylic acid represented by polylactic acid is a biodegradable resin for which great demand is expected in the future, but the polymerization catalyst used in the conventional production method is one. , 3-substitution-1,
It is an organic metal compound such as 1,3,3-tetraorganodistanoxane, and has a problem in that when it is disposed of in a natural environment without being collected after use, it has a significant effect on the environment.

【0004】また、これまで知られているリン酸アルミ
ニウム、リン酸鉄、リン酸カルシウム等のリン酸金属塩
を触媒として用いたヒドロキシカルボン酸の重合は、金
属原子部分がヒドロキシカルボン酸に配位し、ヒドロキ
シカルボン酸の反応部位を活性化することにより進行す
るものである。
[0004] Further, in the polymerization of hydroxycarboxylic acid using a conventionally known metal phosphate such as aluminum phosphate, iron phosphate, calcium phosphate or the like as a catalyst, a metal atom part is coordinated to hydroxycarboxylic acid. It proceeds by activating the reactive site of hydroxycarboxylic acid.

【0005】したがってリン酸金属塩を触媒として合成
されるポリヒドロキシカルボン酸を医療用途、たとえば
薬のコーティング材料として使用する場合、樹脂内に金
属イオンが残留していると薬と金属イオンが錯体を形成
し、薬の効力を阻害してしまう可能性がある。このため
リン酸金属塩を触媒として合成されたポリヒドロキシカ
ルボン酸を未精製のままで医療用途に用いるのは好まし
くない。
Therefore, when a polyhydroxycarboxylic acid synthesized using a metal phosphate as a catalyst is used for medical purposes, for example, as a coating material for a drug, if the metal ion remains in the resin, the drug and the metal ion form a complex. Can form and interfere with the efficacy of the drug. For this reason, it is not preferable to use a polyhydroxycarboxylic acid synthesized using a metal phosphate as a catalyst for medical purposes without purification.

【0006】さらに、ヒドロキシカルボン酸の重合にお
いてリン酸エステルを使用することも報告されている。
しかしリン酸エステルは、触媒としてではなく、あくま
で熱安定剤および反応停止剤として使用されるものであ
る。熱安定剤としてのリン酸エステルは、ポリヒドロキ
シカルボン酸の成形加工時における熱分解反応を防止す
るために用いるものである。一方、反応停止剤としての
リン酸エステルは、重合反応をそれ以上進行させないた
めに用いるものである。ここで、リン酸エステルは触媒
(有機金属化合物、金属塩、金属酸化物など)と錯体を
形成し、触媒サイクルを停止する作用を有する。
[0006] Furthermore, the use of phosphoric esters in the polymerization of hydroxycarboxylic acids has also been reported.
However, the phosphoric acid ester is not used as a catalyst but as a heat stabilizer and a reaction terminator. Phosphoric acid esters as heat stabilizers are used to prevent a thermal decomposition reaction during molding of polyhydroxycarboxylic acid. On the other hand, a phosphate ester as a reaction terminator is used to prevent the polymerization reaction from proceeding further. Here, the phosphate ester forms a complex with a catalyst (such as an organometallic compound, a metal salt, or a metal oxide), and has an action of stopping the catalyst cycle.

【0007】さらにまた、K.Hiltunenらはポ
リヒドロキシカルボン酸を合成するのに用いる酸触媒と
して、硫酸が適していると報告している(Macrom
olecules,Vol.30,No.3,pp.3
73−379,1997)。しかしながら硫酸は、有機
化合物とはニトロ化、スルホン化等の反応を生じさせ
る。そしてこれらの反応が生体内で生じると生体に悪影
響を及ぼす可能性があるため、硫酸を触媒として合成さ
れたポリヒドロキシカルボン酸を医療用途において使用
するには硫酸を取り除かなければならない。
Further, K.K. Hiltunen et al. Report that sulfuric acid is a suitable acid catalyst for use in synthesizing polyhydroxycarboxylic acids (Macrom).
olecules, Vol. 30, no. 3, pp. 3
73-379, 1997). However, sulfuric acid causes reactions such as nitration and sulfonation with organic compounds. When these reactions occur in a living body, the living body may be adversely affected. Therefore, in order to use polyhydroxycarboxylic acid synthesized using sulfuric acid as a catalyst in medical applications, sulfuric acid must be removed.

【0008】本発明は、ヒドロキシカルボン酸またはヒ
ドロキシカルボン酸と糖類や金属酸化物との混合物の重
合触媒として、使用後回収されずに自然環境中に廃棄さ
れた場合においても環境にほとんど影響を及ぼすことが
なく、かつ生成物中に残留したとしても薬との反応や生
体内での有害な反応を生じることのない重合触媒を使用
するポリヒドロキシカルボン酸の製造方法を提供するこ
とを目的とするものである。
The present invention provides a catalyst for polymerization of a hydroxycarboxylic acid or a mixture of a hydroxycarboxylic acid and a saccharide or metal oxide, which has little effect on the environment even when it is disposed of in the natural environment without being recovered after use. It is an object of the present invention to provide a method for producing a polyhydroxycarboxylic acid using a polymerization catalyst which does not cause a reaction with a drug or a harmful reaction in a living body even if it remains in a product without causing the reaction. Things.

【0009】[0009]

【課題を解決するための手段】本発明者は鋭意検討した
結果、重合触媒としてリン酸誘導体を使用することによ
り上記の目的を達成することができることを見出し、本
発明を完成するに至った。
Means for Solving the Problems As a result of intensive studies, the present inventors have found that the above object can be achieved by using a phosphoric acid derivative as a polymerization catalyst, and have completed the present invention.

【0010】すなわち本発明のポリヒドロキシカルボン
酸の製造方法は、1種類以上のヒドロキシカルボン酸、
またはヒドロキシカルボン酸と糖類あるいは金属酸化物
との混合物中に、重合触媒としてリン酸誘導体を添加
し、減圧下に加熱攪拌するか、あるいは有機溶媒中で共
沸脱水重合を行うことを特徴とするものである。
That is, the method for producing a polyhydroxycarboxylic acid of the present invention comprises the steps of:
Or, in a mixture of a hydroxycarboxylic acid and a saccharide or a metal oxide, a phosphoric acid derivative is added as a polymerization catalyst, and the mixture is heated and stirred under reduced pressure, or is subjected to azeotropic dehydration polymerization in an organic solvent. Things.

【0011】[0011]

【発明の実施の形態】本発明においてヒドロキシカルボ
ン酸またはその混合物の重合反応に用いられる重合触媒
としてはリン酸誘導体が使用される。
DESCRIPTION OF THE PREFERRED EMBODIMENTS In the present invention, a phosphoric acid derivative is used as a polymerization catalyst used for a polymerization reaction of a hydroxycarboxylic acid or a mixture thereof.

【0012】リン酸誘導体としては、ブレンステッド酸
(すなわち水素イオンを放出しうる化学種)であって無
毒なものであればいずれを使用しても差し支えはなく、
たとえばリン酸、ピロリン酸、ポリリン酸、酢酸リン等
が挙げられるが、入手のしやすさと安価であることか
ら、リン酸を用いることが好ましい。本発明におけるヒ
ドロキシカルボン酸の重合反応は、リン酸誘導体から放
出される水素イオン(H+)の働きによりヒドロキシカ
ルボン酸同士で脱水し、エステル化が進行するものであ
り、リン酸金属塩を用いる従来技術とは反応機構が異な
っている。
As the phosphoric acid derivative, any Bronsted acid (ie, a chemical species capable of releasing hydrogen ions) which is non-toxic can be used.
For example, phosphoric acid, pyrophosphoric acid, polyphosphoric acid, phosphorus acetate and the like can be mentioned. However, phosphoric acid is preferably used because it is easily available and inexpensive. In the polymerization reaction of the hydroxycarboxylic acid in the present invention, the hydrogen ions (H + ) released from the phosphoric acid derivative cause the dehydration between the hydroxycarboxylic acids and esterification proceeds, and a metal phosphate is used. The reaction mechanism is different from the prior art.

【0013】またリン酸は無機の酸化物であり毒性が小
さいため、使用後回収されずに自然環境中に廃棄された
場合においても環境にほとんど影響を及ぼさない。さら
にリン酸は硫酸よりも弱酸であり、有機化合物とはニト
ロ化、スルホン化等の反応を起こさないから、生体内で
悪影響を及ぼす可能性はなく、しかもリン酸は食品添加
物として認可されており、使用後生体内に残されても生
体に及ぼす影響はきわめて小さい。
[0013] Further, since phosphoric acid is an inorganic oxide and has low toxicity, even if it is discarded in a natural environment without being recovered after use, it hardly affects the environment. Furthermore, phosphoric acid is a weaker acid than sulfuric acid and does not cause reactions such as nitration and sulfonation with organic compounds, so there is no possibility of adverse effects in vivo, and phosphoric acid is approved as a food additive. Therefore, even if it is left in the living body after use, the effect on the living body is extremely small.

【0014】なお亜リン酸について検討したところ、リ
ン酸が空気中で安定であるのに対し、亜リン酸は空気中
で不安定であるため重合反応を窒素ガス雰囲気下で行う
必要があり、また得られるポリヒドロキシカルボン酸の
重量平均分子量(Mw)は最大で11,000程度であ
る。
When phosphorous acid was examined, phosphoric acid was stable in air, whereas phosphorous acid was unstable in air, so that the polymerization reaction had to be carried out in a nitrogen gas atmosphere. The weight average molecular weight (Mw) of the obtained polyhydroxycarboxylic acid is at most about 11,000.

【0015】さらにリン酸誘導体は触媒活性が高い重合
触媒であるから、乳酸等のヒドロキシカルボン酸以外の
共重合成分として少なくとも一種以上の多糖類や金属酸
化物を用いることで、より高分子量のポリヒドロキシカ
ルボン酸が得られる。
Further, since the phosphoric acid derivative is a polymerization catalyst having high catalytic activity, by using at least one kind of polysaccharide or metal oxide as a copolymerization component other than hydroxycarboxylic acid such as lactic acid, a higher molecular weight polysaccharide can be obtained. A hydroxycarboxylic acid is obtained.

【0016】リン酸誘導体の置換基は水素または水酸基
が好ましい。またリン原子に脂肪族カルボン酸や芳香族
カルボン酸が直接結合していてもよい。またピロリン酸
やポリリン酸のように、いくつかのリン原子が酸素原子
を介してオリゴマーを形成していてもよい。
The substituent of the phosphoric acid derivative is preferably hydrogen or a hydroxyl group. An aliphatic carboxylic acid or an aromatic carboxylic acid may be directly bonded to the phosphorus atom. Some phosphorus atoms may form an oligomer via an oxygen atom like pyrophosphoric acid and polyphosphoric acid.

【0017】リン酸誘導体の添加量は、ヒドロキシカル
ボン酸100重量部に対し0.001〜1重量部が好ま
しい。0.001重量部未満であると顕著な触媒活性が
得られず、1重量部を超えると得られるポリヒドロキシ
カルボン酸の重量平均分子量が減少する。
The addition amount of the phosphoric acid derivative is preferably 0.001 to 1 part by weight based on 100 parts by weight of the hydroxycarboxylic acid. If the amount is less than 0.001 part by weight, remarkable catalytic activity cannot be obtained. If the amount exceeds 1 part by weight, the weight average molecular weight of the obtained polyhydroxycarboxylic acid decreases.

【0018】本発明に使用するヒドロキシカルボン酸
は、分子内に水酸基を有する脂肪族カルボン酸が好まし
く、不整炭素を有する場合はD体、L体、ラセミ体のい
ずれでもよい。また2種以上のヒドロキシカルボン酸を
併用してもよい。このようなヒドロキシカルボン酸の具
体例として、乳酸、グリコール酸、酒石酸、クエン酸、
リンゴ酸などを挙げることができ、これらを単独でまた
は混合物として用いることが好ましい。
The hydroxycarboxylic acid used in the present invention is preferably an aliphatic carboxylic acid having a hydroxyl group in the molecule. When it has an asymmetric carbon, it may be any of D-form, L-form and racemic-form. Two or more hydroxycarboxylic acids may be used in combination. Specific examples of such hydroxycarboxylic acids include lactic acid, glycolic acid, tartaric acid, citric acid,
Malic acid and the like can be mentioned, and these are preferably used alone or as a mixture.

【0019】本発明の共重合成分として使用する糖類と
しては天然物のものが好ましく、D−グルコース、D−
フルクトース、D−マンノース、D−ガラクトースなど
の単糖類、麦芽糖、砂糖(ショ糖)などの少糖(オリゴ
糖)類、澱粉、特にコーンスターチ、サツマイモ澱粉、
小麦澱粉などの多糖類、あるいはこれらの混合物を挙げ
ることができる。
The saccharide used as a copolymer component of the present invention is preferably a natural product, such as D-glucose or D-glucose.
Monosaccharides such as fructose, D-mannose and D-galactose; oligosaccharides (oligosaccharides) such as maltose and sugar (sucrose); starch, particularly corn starch and sweet potato starch;
Examples thereof include polysaccharides such as wheat starch, and mixtures thereof.

【0020】本発明に使用する有機溶媒は、水より沸点
が高くかつ水と相溶化しないものであればいずれでもよ
いが、天然物であって樹脂中に残存しても環境や人体に
悪影響の少ないD−リモネンが好ましい。
The organic solvent used in the present invention may be any organic solvent that has a higher boiling point than water and is not compatible with water. However, even if it is a natural product and remains in the resin, it has no adverse effect on the environment or the human body. Less D-limonene is preferred.

【0021】[0021]

【実施例】以下、実施例および比較例により、本発明を
さらに詳しく説明する。 (実施例1)90%L−乳酸1mol(100g)と8
5%リン酸水溶液0.05w%(50mg)を500m
lの反応器に入れ、190℃で30時間減圧下に加熱攪
拌した。得られたポリ乳酸の重量平均分子量(Mw)を
測定したところ、19,000であった。
The present invention will be described below in more detail with reference to Examples and Comparative Examples. (Example 1) 1 mol (100 g) of 90% L-lactic acid and 8
5% phosphoric acid aqueous solution 0.05w% (50mg) 500m
and stirred under heating at 190 ° C. for 30 hours under reduced pressure. When the weight average molecular weight (Mw) of the obtained polylactic acid was measured, it was 19,000.

【0022】なお、得られた樹脂の重量平均分子量はゲ
ルパーミエーションクロマトグラフィー(GPC)を用
いて測定した。流出溶媒はクロロホルムを使用し、温度
40℃で、流量は1.0ml/minである。GPC装
置は日本ミリポアリミテッド株式会社製高圧ポンプ(高
速液体クロマトグラフ用510型)と、昭和電工株式会
社製示差屈折率検出器(ShodexRI−71)およ
び同社製カラム(GPC K802.5およびGPC
K806M)である。また分子量はポリスチレンを標準
試料とし、換算した値である。
The weight average molecular weight of the obtained resin was measured by using gel permeation chromatography (GPC). The solvent used was chloroform, and the temperature was 40 ° C. and the flow rate was 1.0 ml / min. The GPC device is a high pressure pump (Model 510 for high-performance liquid chromatography) manufactured by Nippon Millipore Limited, a differential refractive index detector (Showex RI-71) manufactured by Showa Denko KK, and columns (GPC K802.5 and GPC) manufactured by the company.
K806M). The molecular weight is a value obtained by converting polystyrene as a standard sample.

【0023】(実施例2)90%L−乳酸1mol(1
00g)と85%リン酸水溶液0.1w%(100m
g)を500mlの反応器に入れ、190℃で30時間
減圧下に加熱攪拌した。得られたポリ乳酸の重量平均分
子量は38,000であった。
(Example 2) 1 mol of 90% L-lactic acid (1 mol
00g) and 0.1% by weight of 85% phosphoric acid aqueous solution (100 m
g) was placed in a 500 ml reactor, and heated and stirred under reduced pressure at 190 ° C. for 30 hours. The weight average molecular weight of the obtained polylactic acid was 38,000.

【0024】(実施例3)90%L−乳酸1mol(1
00g)と85%リン酸水溶液0.2w%(200m
g)を500mlの反応器に入れ、190℃で30時間
減圧下に加熱攪拌した。得られたポリ乳酸の重量平均分
子量は29,000であった。
Example 3 1 mol of 90% L-lactic acid (1 mol
00g) and 0.2% by weight of an 85% phosphoric acid aqueous solution (200 m
g) was placed in a 500 ml reactor, and heated and stirred under reduced pressure at 190 ° C. for 30 hours. The weight average molecular weight of the obtained polylactic acid was 29,000.

【0025】(実施例4)90%L−乳酸1mol(1
00g)とコーンスターチ100mgと85%リン酸水
溶液0.1w%(100mg)を500mlの反応器に
入れ、190℃で30時間減圧下に加熱攪拌した。得ら
れた乳酸−糖共重合体の重量平均分子量は51,000
であった。
Example 4 1 mol of 90% L-lactic acid (1 mol
00g), 100 mg of corn starch and 0.1 w% (100 mg) of an 85% phosphoric acid aqueous solution were placed in a 500 ml reactor, and heated and stirred under reduced pressure at 190 ° C. for 30 hours. The weight average molecular weight of the obtained lactic acid-sugar copolymer is 51,000.
Met.

【0026】(実施例5)90%L−乳酸1mol(1
00g)とコーンスターチ200mgと85%リン酸水
溶液0.1w%(100mg)を500mlの反応器に
入れ、190℃で30時間減圧下に加熱攪拌した。得ら
れた乳酸−糖共重合体の重量平均分子量は58,000
であった。
Example 5 1 mol of 90% L-lactic acid (1 mol
00g), 200 mg of corn starch and 0.1 w% (100 mg) of an 85% phosphoric acid aqueous solution were put into a 500 ml reactor, and heated and stirred under reduced pressure at 190 ° C. for 30 hours. The weight average molecular weight of the obtained lactic acid-sugar copolymer is 58,000.
Met.

【0027】(比較例)90%L−乳酸1mol(10
0g)を500mlの反応器に入れ、190℃で30時
間減圧下に加熱攪拌した。得られたポリ乳酸の重量平均
分子量は11,000であった。
Comparative Example 1 mol of 90% L-lactic acid (10 mol
0 g) was placed in a 500 ml reactor and heated and stirred at 190 ° C. for 30 hours under reduced pressure. The weight average molecular weight of the obtained polylactic acid was 11,000.

【0028】[0028]

【発明の効果】以上説明したように本発明によれば、ヒ
ドロキシカルボン酸またはヒドロキシカルボン酸と糖類
や金属酸化物との混合物の重合触媒としてリン酸誘導体
を用いることにより、使用後回収されずに自然環境中に
廃棄された場合においても環境にほとんど影響を及ぼさ
ない。
As described above, according to the present invention, by using a phosphoric acid derivative as a polymerization catalyst for a hydroxycarboxylic acid or a mixture of a hydroxycarboxylic acid and a saccharide or a metal oxide, it is not recovered after use. Even if disposed of in the natural environment, it has little effect on the environment.

【0029】また得られた樹脂は、通常の触媒を用いて
合成された樹脂と同様の用途に使用されるほか、生体内
や生体に直接接触する医療用樹脂成形品などに好適に使
用することができる。
The obtained resin is used not only for the same purpose as the resin synthesized using an ordinary catalyst, but also for medical resin molded articles which come into direct contact with the living body. Can be.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】1種類のヒドロキシカルボン酸、2種類以
上のヒドロキシカルボン酸の混合物、ヒドロキシカルボ
ン酸と糖類の混合物、またはヒドロキシカルボン酸と金
属酸化物の混合物中に、重合触媒としてリン酸誘導体を
添加し、減圧下に加熱攪拌するか、あるいは有機溶媒中
で共沸脱水重合を行うことを特徴とするポリヒドロキシ
カルボン酸の製造方法。
1. A phosphoric acid derivative as a polymerization catalyst in one kind of hydroxycarboxylic acid, a mixture of two or more kinds of hydroxycarboxylic acids, a mixture of hydroxycarboxylic acids and saccharides, or a mixture of hydroxycarboxylic acids and metal oxides. A method for producing a polyhydroxycarboxylic acid, comprising adding and stirring under heating under reduced pressure, or performing azeotropic dehydration polymerization in an organic solvent.
【請求項2】リン酸誘導体がリン酸、ピロリン酸、ポリ
リン酸、酢酸リンからなる群から選択される一種以上の
リン酸誘導体であることを特徴とする請求項1に記載の
ポリヒドロキシカルボン酸の製造方法。
2. The polyhydroxycarboxylic acid according to claim 1, wherein the phosphoric acid derivative is at least one phosphoric acid derivative selected from the group consisting of phosphoric acid, pyrophosphoric acid, polyphosphoric acid and phosphorus acetate. Manufacturing method.
【請求項3】ヒドロキシカルボン酸が乳酸、グリコール
酸、酒石酸、クエン酸、リンゴ酸、あるいはこれらの混
合物であることを特徴とする請求項1に記載のポリヒド
ロキシカルボン酸の製造方法。
3. The method for producing a polyhydroxycarboxylic acid according to claim 1, wherein the hydroxycarboxylic acid is lactic acid, glycolic acid, tartaric acid, citric acid, malic acid, or a mixture thereof.
【請求項4】糖類が多糖類であることを特徴とする請求
項1に記載のポリヒドロキシカルボン酸の製造方法。
4. The method for producing a polyhydroxycarboxylic acid according to claim 1, wherein the saccharide is a polysaccharide.
【請求項5】有機溶媒がD−リモネンであることを特徴
とする請求項1に記載のポリヒドロキシカルボン酸の製
造方法。
5. The method for producing polyhydroxycarboxylic acid according to claim 1, wherein the organic solvent is D-limonene.
JP2000333399A 2000-10-31 2000-10-31 Process for producing polyhydroxycarboxylic acid Expired - Fee Related JP3745612B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000333399A JP3745612B2 (en) 2000-10-31 2000-10-31 Process for producing polyhydroxycarboxylic acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000333399A JP3745612B2 (en) 2000-10-31 2000-10-31 Process for producing polyhydroxycarboxylic acid

Publications (2)

Publication Number Publication Date
JP2002138142A true JP2002138142A (en) 2002-05-14
JP3745612B2 JP3745612B2 (en) 2006-02-15

Family

ID=18809489

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000333399A Expired - Fee Related JP3745612B2 (en) 2000-10-31 2000-10-31 Process for producing polyhydroxycarboxylic acid

Country Status (1)

Country Link
JP (1) JP3745612B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007063516A (en) * 2005-09-02 2007-03-15 Hiroshima Univ Resin composition
WO2007145195A1 (en) 2006-06-15 2007-12-21 National University Corporation Kyoto Institute Of Technology Organic acid catalyst for polylactic acid synthesis
CN100415797C (en) * 2006-08-24 2008-09-03 中国民航大学 Micropore foamed polymer capable of biodegradable and its preparation method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007063516A (en) * 2005-09-02 2007-03-15 Hiroshima Univ Resin composition
WO2007145195A1 (en) 2006-06-15 2007-12-21 National University Corporation Kyoto Institute Of Technology Organic acid catalyst for polylactic acid synthesis
CN100415797C (en) * 2006-08-24 2008-09-03 中国民航大学 Micropore foamed polymer capable of biodegradable and its preparation method

Also Published As

Publication number Publication date
JP3745612B2 (en) 2006-02-15

Similar Documents

Publication Publication Date Title
JP5485151B2 (en) Polymer hydrogel and preparation method thereof
Liu et al. Gelatin-based hydrogels with β-cyclodextrin as a dual functional component for enhanced drug loading and controlled release
JP4584146B2 (en) Molded product containing α-1,4-glucan and / or modified product thereof and method for producing the same
CA2339166C (en) Dextran-maleic acid monoesters and hydrogels based thereon
JPH0796181A (en) Superabsorbent, process for preparation thereof and hygienicgoods having the same
JP7128368B2 (en) Cellulose acetate and cellulose acetate composition
WO2002006507A1 (en) Biodegradable articles obtained from enzymatically synthesized amylose
JP4321007B2 (en) Polysaccharide complex and method for producing the same
WO1994003499A1 (en) Auto-cross-linked gellan gum
CN103442742A (en) Biodegradable particle, vascular embolization material and method for producing biodegradable particles
JP2002138142A (en) Method of producing polyhydroxycarboxylic acid
JPH03503905A (en) Cross-linked hyaluronic acid gel, its use and its production method
JPH1160928A (en) Polyhydroxycarboxylic acid resin composition and its production
US5844068A (en) Process for the preparation of polyhydroxycarboxylic acid copolymer resin
JP3086851B2 (en) Method for producing polyhydroxycarboxylic acid resin
Sen et al. A novel polymeric biomaterial based on carboxymethylstarch and its application in controlled drug release
CN107412151B (en) Phytohemagglutinin-polysaccharide hydrogel capable of intelligently regulating and controlling insulin release as well as preparation and application thereof
JP5110046B2 (en) Polysaccharide complex and method for producing the same
JP2003522823A (en) Biodegradable disposable syringe
JP2002241403A (en) Lactide-modified starch derivative and process for preparation thereof
JP2003176353A (en) Polylysine and method for producing the same
JPH10237106A (en) Production of acylated chitin and chitosan, and molded products thereof
JPH0467945B2 (en)
KR940009418B1 (en) Process for preparation of polyester with biodegradation
JPH01156341A (en) Production of polyion complex gel

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20050506

A871 Explanation of circumstances concerning accelerated examination

Free format text: JAPANESE INTERMEDIATE CODE: A871

Effective date: 20050506

A975 Report on accelerated examination

Free format text: JAPANESE INTERMEDIATE CODE: A971005

Effective date: 20050524

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20050601

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20050719

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20050831

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20051020

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20051116

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20051117

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

LAPS Cancellation because of no payment of annual fees