JPH07316273A - Acid-terminal-blocked polylactic acid - Google Patents

Acid-terminal-blocked polylactic acid

Info

Publication number
JPH07316273A
JPH07316273A JP10979194A JP10979194A JPH07316273A JP H07316273 A JPH07316273 A JP H07316273A JP 10979194 A JP10979194 A JP 10979194A JP 10979194 A JP10979194 A JP 10979194A JP H07316273 A JPH07316273 A JP H07316273A
Authority
JP
Japan
Prior art keywords
acid
polylactic acid
hydrolysis resistance
polymer
terminal
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
JP10979194A
Other languages
Japanese (ja)
Other versions
JP3367577B2 (en
Inventor
Kunio Kimura
邦生 木村
Keiichi Uno
敬一 宇野
Tomohiro Aoyama
知裕 青山
Takeshi Ito
武 伊藤
Minako Yuuchi
美奈子 有地
Seishi Hotta
清史 堀田
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.)
Toyobo Co Ltd
Original Assignee
Toyobo 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 Toyobo Co Ltd filed Critical Toyobo Co Ltd
Priority to JP10979194A priority Critical patent/JP3367577B2/en
Priority to US08/285,552 priority patent/US5618911A/en
Priority to CN03108626.8A priority patent/CN1216882C/en
Priority to CN94115768A priority patent/CN1051095C/en
Publication of JPH07316273A publication Critical patent/JPH07316273A/en
Priority to US08/734,474 priority patent/US5714618A/en
Priority to CN99117996.XA priority patent/CN1129595C/en
Application granted granted Critical
Publication of JP3367577B2 publication Critical patent/JP3367577B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To obtain a polylactic acid resin having such a high hydrolysis resistance that it can stably exist in water or a humid atmosphere. CONSTITUTION:A polylactic acid whose acid terminals are substantially blocked and which is represented by the formula. In the formula, x is H or a hydrocarbon group; Y is a 1-50 C monovalent or polyvalent aliphatic hydrocarbon group; n is a positive integer of 10 or greater; and 1 is a positive integer of 1 or greater.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、酸末端が実質的に封鎖
されており、耐加水分解性に優れていることを特徴とす
るポリ乳酸に関する。更には、酸及び水酸両末端基が封
鎖されており、高温下での安定性にも優れていることを
特徴とするポリ乳酸に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to polylactic acid which is substantially capped with an acid terminal and is excellent in hydrolysis resistance. Further, the present invention relates to polylactic acid, which has both acid and hydroxyl terminal groups blocked and is excellent in stability at high temperatures.

【0002】[0002]

【従来の技術】近年、プラスチック廃棄物が引き起こす
環境破壊問題から、酵素や微生物で分解される生分解性
を有するプラスチックの開発研究が盛んに行なわれてお
り、その中でも、脂肪族ポリエステルが注目されてい
る。生分解性ポリエステルとしては、ポリ[(R)−3
−ヒドロキシブチレート]、ポリカプロラクトン、或い
はエチレングリコール、1、4−ブタンジオール等のグ
リコールとコハク酸、アジピン酸等のカルボン酸より成
るポリエステルが知られている。ポリ[(R)−3−ヒ
ドロキシブチレート]系ポリエステルは主に微生物合成
により生産されるために高価である。又、他のポリエス
テルは其の融点が低く、用途が拡大し難いと言った問題
がある。
2. Description of the Related Art In recent years, due to the problem of environmental destruction caused by plastic waste, research and development of biodegradable plastics that are decomposed by enzymes and microorganisms have been actively conducted, and among them, aliphatic polyesters have attracted attention. ing. As the biodegradable polyester, poly [(R) -3
-Hydroxybutyrate], polycaprolactone, or a polyester comprising a glycol such as ethylene glycol or 1,4-butanediol and a carboxylic acid such as succinic acid or adipic acid is known. Poly [(R) -3-hydroxybutyrate] -based polyester is expensive because it is mainly produced by microbial synthesis. In addition, other polyesters have a low melting point, which makes it difficult to expand their applications.

【0003】ポリ乳酸系樹脂は、良好な生分解性を有し
ており、手術用縫合糸や注射薬用マイクロカプセル等の
生体吸収材料として利用されている。また、近年、プラ
スチック廃棄物が引き起こす諸問題が社会的関心事とな
っており、其の解決策の一つとして酵素や微生物により
分解が期待される生分解性プラスチックとしても注目さ
れ、研究開発が進められている。ポリ乳酸樹脂は、熱的
性質、力学的性質、また、生分解性等の諸特性に優れ、
更には、分解後の残査が殆どないといった完全分解性で
あることや分解物の安全性が確立されているといった数
々の特筆すべき特徴を有し、その利用が非常に期待され
ている。
Polylactic acid resins have good biodegradability and are used as bioabsorbable materials such as surgical sutures and microcapsules for injections. In recent years, various problems caused by plastic waste have become a social concern, and as one of the solutions, attention has been paid to biodegradable plastics that are expected to be decomposed by enzymes and microorganisms, and R & D It is being advanced. Polylactic acid resin is excellent in various properties such as thermal properties, mechanical properties, and biodegradability,
Furthermore, it has a number of remarkable features such as complete degradability such that there is almost no residue after decomposition, and the safety of the decomposed product has been established, and its use is highly expected.

【0004】しかしながら、水中或いは湿度下での安定
性が充分ではなく大きな問題となっている。この様な耐
加水分解性の低さは、ポリ乳酸樹脂を生分解性プラスチ
ックとして利用する上で著しく不利であり、汎用用途へ
の展開が阻害されているのが現状である。加えて、ポリ
乳酸は溶融時の安定性が低く、溶融成形時に分子量の低
下を起こす。これは、成形品の物性の低下を引き起こす
ことは勿論、成形安定性の低下をも引き起こす。
However, the stability in water or in humidity is not sufficient, which is a big problem. Such low hydrolysis resistance is extremely disadvantageous in using the polylactic acid resin as a biodegradable plastic, and the development of general-purpose applications is currently hindered. In addition, polylactic acid has low stability when melted and causes a decrease in molecular weight during melt molding. This not only causes deterioration of the physical properties of the molded product, but also causes deterioration of molding stability.

【0005】[0005]

【発明が解決しようとする課題】上記の如く耐加水分解
性に優れ、更には溶融時安定性をも兼ね備えたポリ乳酸
が切望されているにもかかわらず、其の様なポリ乳酸は
未だ得られていない。かかる理由により、本発明は、水
中或いは湿度雰囲気下で安定に存在し得る良好な耐加水
分解性を有するポリ乳酸樹脂を提供し、更には、溶融時
安定性をも兼ね備えたポリ乳酸を提供することを目的と
する。
Although polylactic acid having excellent hydrolysis resistance and stability upon melting as described above has been earnestly desired, such polylactic acid has not been obtained yet. Has not been done. For this reason, the present invention provides a polylactic acid resin having good hydrolysis resistance that can stably exist in water or in a humidity atmosphere, and further provides polylactic acid that also has stability when melted. The purpose is to

【0006】[0006]

【課題を解決するための手段】そこで本研究者らは、良
好な耐加水分解性を有するポリ乳酸系樹脂を得るべく鋭
意検討を重ねた結果、酸末端と加水分解性に相関がある
ことを見いだし、遂に本発明を完成するに到った。即ち
本発明は、下記一般式(I)で表される酸末端が実質的
に封鎖されていることを特徴とするポリ乳酸に関するも
のである。
[Means for Solving the Problems] Therefore, as a result of intensive studies to obtain a polylactic acid-based resin having good hydrolysis resistance, the present inventors have found that there is a correlation between the acid terminal and the hydrolyzability. After finding out, the present invention was finally completed. That is, the present invention relates to polylactic acid characterized in that the acid terminal represented by the following general formula (I) is substantially blocked.

【0007】[0007]

【化2】 (式中、Xは水素原子又は炭化水素基、Yは炭素数1以
上50以下の1価以上の多価脂肪族炭化水素基、そして
nは10以上、lは1以上の正の整数を示す。)
[Chemical 2] (In the formula, X represents a hydrogen atom or a hydrocarbon group, Y represents a monovalent or more polyvalent aliphatic hydrocarbon group having 1 to 50 carbon atoms, and n represents a positive integer of 10 or more and 1 or more. .)

【0008】ポリ乳酸の耐加水分解性は、その酸末端基
数と相関があり、酸末端基数が増大するに従って、耐加
水分解性は低下する傾向にある。よって、高分子量のポ
リ乳酸に比べ低分子量のポリ乳酸は著しく耐加水分解性
が低い。ポリマーの分子量に依らず其の耐加水分解性を
向上させるには、酸末端基を封鎖してやることが重要で
ある。酸末端基の封鎖が不充分であれば目的とする良好
な耐加水分解性は発現しない。少なくとも、全酸末端基
数の50%以上は封鎖することが必要である。更には、
80%以上封鎖することが好ましい。
The hydrolysis resistance of polylactic acid has a correlation with the number of acid terminal groups, and as the number of acid terminal groups increases, the hydrolysis resistance tends to decrease. Therefore, low-molecular-weight polylactic acid has significantly lower hydrolysis resistance than high-molecular-weight polylactic acid. In order to improve the hydrolysis resistance of the polymer regardless of its molecular weight, it is important to block the acid end group. If the acid terminal group is not sufficiently blocked, the desired good hydrolysis resistance will not be exhibited. It is necessary to block at least 50% of the total number of acid terminal groups. Furthermore,
It is preferable to block by 80% or more.

【0009】本発明で言うところのポリ乳酸とは、L-乳
酸、D-乳酸いずれの乳酸単位の縮合体、又、それらの混
合縮合体を言う。ラクチド法で製造する場合には、L-ラ
クチド、D-ラクチド、DL-ラクチド、メソ−ラクチドの
何れを用いても良い。
The polylactic acid referred to in the present invention means a condensate of lactic acid units such as L-lactic acid and D-lactic acid, or a mixed condensate thereof. When it is produced by the lactide method, any of L-lactide, D-lactide, DL-lactide and meso-lactide may be used.

【0010】上述の如くに酸末端を封鎖するには、炭素
数1以上50以下の飽和及び/又は不飽和の1価以上の
多価脂肪族アルコールを共存させて、ラクチド或いは乳
酸を重合し製造を行なえばよい。用いる脂肪族アルコー
ルは、具体的にはメタノール、エタノール、プロパノー
ル、イソプロパノール、ブタノール、ペンタノール、ノ
ナノール、デカノール、ラウリルアルコール、ミリスチ
ルアルコール、セチルアルコール、ステアリルアルコー
ル、乳酸メチル、乳酸エチル、乳酸ブチル等のモノアル
コール、エチレングリコール、プロパンジオール、ブタ
ンジオール、ヘキサメチレングリコール、ノナンジオー
ル、テトラメチレングリコール等のジアルコール、グリ
セロール、ソルビトール、キシリトール、リビトール、
エリスリトール等の多価値アルコールを挙げることが出
来るがこれらに限定されるものではない。
In order to block the acid terminal as described above, a lactide or lactic acid is polymerized in the presence of a saturated and / or unsaturated monohydric or higher polyhydric aliphatic alcohol having 1 to 50 carbon atoms to produce it. Should be done. Specific examples of the aliphatic alcohol used include methanol, ethanol, propanol, isopropanol, butanol, pentanol, nonanol, decanol, lauryl alcohol, myristyl alcohol, cetyl alcohol, stearyl alcohol, methyl lactate, ethyl lactate, and butyl lactate. Dialcohols such as alcohol, ethylene glycol, propanediol, butanediol, hexamethylene glycol, nonanediol, tetramethylene glycol, glycerol, sorbitol, xylitol, ribitol,
Examples thereof include polyhydric alcohols such as erythritol, but are not limited thereto.

【0011】これらのアルコールは1種又は複数併用す
ることも可能である。特に、デカノール、ラウリルアル
コール、ミリスチルアルコール、セチルアルコール、ス
テアリルアルコール等の長鎖のアルコールが好適であ
る。用いるアルコールの沸点が重合温度より低いばあい
には、加圧下で反応を行なう必要がある。用いるアルコ
ールの量は、目的により異なるが、多すぎると分子量が
上がりにくく低分子量化合物が多量になるので好ましく
ない。全モノマーに対して0.001〜1モル%の割合
で用いられる。
These alcohols can be used alone or in combination of two or more. In particular, long-chain alcohols such as decanol, lauryl alcohol, myristyl alcohol, cetyl alcohol, and stearyl alcohol are suitable. When the boiling point of the alcohol used is lower than the polymerization temperature, it is necessary to carry out the reaction under pressure. The amount of alcohol used varies depending on the purpose, but if it is too large, the molecular weight is difficult to increase, and the amount of low molecular weight compounds increases, which is not preferable. It is used in a proportion of 0.001 to 1 mol% based on all monomers.

【0012】また、更に溶融安定性を向上させるには、
水酸基末端を炭化水素基で封鎖すればよく、好ましくは
式(I)中のXの70%以上、更に好ましくは80%以
上が炭素数2以上50以下のアシル基で封鎖する必要が
ある。この様な水酸基末端封鎖したポリ乳酸を製造する
場合は、炭素数2以上50以下の飽和及び/又は不飽和
脂肪族酸を用いて行なう。ラクチド法で製造する場合
は、これらの脂肪族酸を共存させて開環重合反応を行な
えばよいし、また、ポリマーを重合した後に脂肪族酸無
水物で処理し末端を封鎖することも出来る。
Further, in order to further improve the melt stability,
The end of the hydroxyl group may be blocked with a hydrocarbon group, preferably 70% or more, and more preferably 80% or more of X in the formula (I) should be blocked with an acyl group having 2 to 50 carbon atoms. When producing such a polylactic acid having a hydroxyl group end blocked, a saturated and / or unsaturated aliphatic acid having 2 to 50 carbon atoms is used. In the case of production by the lactide method, the ring-opening polymerization reaction may be carried out in the presence of these aliphatic acids, or the polymer may be polymerized and then treated with an aliphatic acid anhydride to block the ends.

【0013】用いる脂肪族酸は、具体的には、酢酸、プ
ロピオン酸、酪酸、吉草酸、カプロン酸、カプリン酸、
ペラルゴン酸、ラウリン酸、ミリスチン酸、パルミチン
酸、ステアリン酸、アラギジン酸、ベヘン酸、リノール
酸、オレイン酸、コハク酸、アジピン酸、スベリン酸、
アゼライン酸、セバシン酸、ウンデカン二酸、ダイマー
酸、フマル酸等を挙げることが出来るがこれらに限定さ
れるものではない。また、これらの酸無水物を加えても
差し支えない。
Specific examples of the aliphatic acid used include acetic acid, propionic acid, butyric acid, valeric acid, caproic acid, capric acid,
Pelargonic acid, lauric acid, myristic acid, palmitic acid, stearic acid, aragic acid, behenic acid, linoleic acid, oleic acid, succinic acid, adipic acid, suberic acid,
Examples thereof include azelaic acid, sebacic acid, undecanedioic acid, dimer acid, fumaric acid, etc., but are not limited thereto. Further, it is possible to add these acid anhydrides.

【0014】これらの脂肪族酸は1種又は複数併用する
ことも可能である。特に、ステアリン酸、パルミチン
酸、ミリスチン酸、リノール酸、オレイン酸は着香料、
乳化剤、ビタミン強化剤、また、フマル酸、コハク酸、
アジピン酸は調味料、酸味料若しくはそれらの原料とし
て食品添加物にも挙げられており、安全性が確立されて
いるので好ましい。更に好ましくは、製パン用助剤とし
て用いられるステアリン酸カルシウムの原料であるステ
アリン酸が挙げられる。用いる脂肪族酸の沸点が重合温
度より低いばあいには、加圧下で反応を行なう必要があ
る。用いる脂肪族酸の量は、目的により異なるが、多す
ぎると分子量が上がりにくく低分子量化合物が多量にな
るので好ましくない。全モノマーに対して0.001〜
1モル%の割合で用いられる。
These aliphatic acids can be used alone or in combination of two or more. In particular, stearic acid, palmitic acid, myristic acid, linoleic acid, oleic acid are flavoring agents,
Emulsifier, vitamin enhancer, fumaric acid, succinic acid,
Adipic acid is also mentioned as a seasoning, an acidulant, or a food additive as a raw material thereof, and is preferable because safety is established. More preferably, stearic acid, which is a raw material of calcium stearate used as an auxiliary agent for bread making, can be mentioned. When the boiling point of the aliphatic acid used is lower than the polymerization temperature, it is necessary to carry out the reaction under pressure. The amount of the aliphatic acid used varies depending on the purpose, but if it is too large, the molecular weight is difficult to increase and the amount of the low molecular weight compound increases, which is not preferable. 0.001 to all monomers
It is used in a proportion of 1 mol%.

【0015】また、本発明のポリ乳酸は第2成分等を共
重合させてもよく、生分解性を有する成分が好ましい。
具体的には、炭素数1以上20以下のアルキレン基から
なるオキシ酸成分であり、ラクチド法でポリマーを製造
する場合は対応するラクトンを共存させればよい。共重
合成分を例示すると、β−ブチロラクトン、γ−ブチロ
ラクトン、ε−カプロラクトン、プロピオラクトン、δ
−バレロラクトン、4−バレロラクトン、グリコリド等
を挙げることが出来るが、これらに限定されるものでは
ない。
The polylactic acid of the present invention may be copolymerized with a second component and the like, and a component having biodegradability is preferable.
Specifically, it is an oxyacid component composed of an alkylene group having 1 to 20 carbon atoms, and when a polymer is produced by the lactide method, a corresponding lactone may be allowed to coexist. Examples of the copolymerization component include β-butyrolactone, γ-butyrolactone, ε-caprolactone, propiolactone and δ.
-Valerolactone, 4-valerolactone, glycolide, etc. can be mentioned, but not limited thereto.

【0016】本発明のポリ乳酸系樹脂を製造する際には
一般に触媒が用いられるが、これらには公知の触媒が用
いられる。ラクチド法で製造される場合には、具体的に
は錫、アンチモン、亜鉛、チタン、鉄、アルミニウム化
合物を例示することが出来るが、これらに限定されるも
のではない。この中では特に錫系触媒、アルミニウム系
触媒が好ましく、オクチル酸錫、アルミニウムアセチル
アセトナートが特に好適である。
A catalyst is generally used when producing the polylactic acid resin of the present invention, and a known catalyst is used for these. When it is produced by the lactide method, specific examples thereof include tin, antimony, zinc, titanium, iron and aluminum compounds, but the invention is not limited thereto. Among these, tin-based catalysts and aluminum-based catalysts are particularly preferable, and tin octylate and aluminum acetylacetonate are particularly preferable.

【0017】本発明のポリ乳酸系樹脂は、必要に応じて
顔料、酸化防止剤、劣化防止剤、可塑剤、艶消剤、帯電
防止剤、紫外線吸収剤等の添加剤を加えても一向に差し
支えない。添加する場合は、低分子量化合物を減少させ
たのちに加える方がポリマー中に残存する量から好まし
い。
The polylactic acid resin of the present invention may be added with additives such as pigments, antioxidants, deterioration inhibitors, plasticizers, matting agents, antistatic agents, and ultraviolet absorbers, if necessary. Absent. When it is added, it is preferable to reduce the amount of the low molecular weight compound and then add the low molecular weight compound from the viewpoint of the amount remaining in the polymer.

【0018】本発明のポリ乳酸系樹脂は、溶融・溶液状
態から繊維、フィルム、シート、また、各種成形品に成
形加工することが可能であり、従来の物み比べて良好な
耐加水分解性を有するために広い範囲に亘り利用出来
る。具体的には、繊維や不織布では釣り糸、漁網、植木
の根巻き用不織布、育苗床用不織布、マルチング材、防
草シートの農園芸用不織布等、フィルムやシートでは包
装用フィルム、農園芸用マルチフィルム、ショッピング
バック、ごみ袋、テープ類、肥料袋、分離膜等、成形品
では飲料や化粧品類のボトル、ディスポーザブルカッ
プ、トレイ、ナイフ、フォーク、スプーン等の容食器
類、農園芸用植木鉢、育苗床、掘出し不用のパイプ、仮
止め材等の建材が挙げられる。
The polylactic acid-based resin of the present invention can be molded into fibers, films, sheets and various molded products from a molten / solution state, and has better hydrolysis resistance than conventional products. Therefore, it can be used over a wide range. Specifically, for fibers and non-woven fabrics, fishing lines, fishing nets, non-woven fabrics for plant roots, non-woven fabrics for nursery beds, mulching materials, agricultural and horticultural non-woven fabrics for weed-proof sheets, etc. , Shopping bags, garbage bags, tapes, fertilizer bags, separation membranes, etc., for molded products such as beverages and cosmetics bottles, disposable cups, trays, knives, forks, spoons and other tableware, agricultural and garden garden pots, nursery beds Building materials such as pipes that are not dug up and temporary fixing materials.

【0019】[0019]

【実施例】本発明を更に具体的に説明するために以下に
実施例を述べるが、本発明はこれらに限定されるもので
はない。尚、実施例における特性値は以下の方法によっ
て測定した。 還元比粘度(ηSP/C) ポリマー0.5gをクロロホルム100mlに溶解し、
25℃で測定した。 耐加水分解性試験 3.50cm×1.75cm×500μmのシート状試験片
を90℃,pH7.0のリン酸緩衝液中に12時間浸漬
し、浸漬前後の重量および還元比粘度を測定した。得ら
れた結果より、下記式によって、重量保持率(WR)及
び粘度保持率(VR)を算出した。
EXAMPLES Examples will be described below to more specifically describe the present invention, but the present invention is not limited thereto. The characteristic values in the examples were measured by the following methods. Reduced specific viscosity (η SP / C) Dissolve 0.5 g of polymer in 100 ml of chloroform,
It was measured at 25 ° C. Hydrolysis resistance test A sheet-shaped test piece of 3.50 cm x 1.75 cm x 500 µm was immersed in a phosphate buffer of 90 ° C and pH 7.0 for 12 hours, and the weight and reduced specific viscosity before and after the immersion were measured. From the obtained results, the weight retention rate (WR) and the viscosity retention rate (VR) were calculated by the following formulas.

【0020】[0020]

【数1】 [Equation 1]

【0021】[0021]

【数2】 溶融安定性試験 ポリマーを絶乾した後に窒素雰囲気下200℃で1時間
撹拌し、還元比粘度変化を測定した。得られた結果よ
り、下記式によって、溶融時粘度保持率(VMR)を算
出した。
[Equation 2] Melt Stability Test After the polymer was completely dried, the polymer was stirred at 200 ° C. for 1 hour in a nitrogen atmosphere, and the change in reduced specific viscosity was measured. From the obtained results, the viscosity retention during melting (VMR) was calculated by the following formula.

【0022】[0022]

【数3】 [Equation 3]

【0023】実施例1 L-ラクチド20.0g、1−デカノール32mg及びオ
クチル酸第1錫6mgのトルエン溶液を撹拌装置、窒素
導入管を備えた重合管に入れ、2時間減圧乾燥したのち
窒素気流下に200℃に加熱し、開環重合した。1時間
で反応を終了したのちポリマーを取り出した。得られた
ポリマーの還元比粘度は1.67dL/gであった。耐
加水分解性は表1に示した様に良好であった。また、V
MRは75%であった。
Example 1 A toluene solution of 20.0 g of L-lactide, 32 mg of 1-decanol and 6 mg of stannous octylate was placed in a polymerization tube equipped with a stirrer and a nitrogen inlet tube, dried under reduced pressure for 2 hours, and then a nitrogen stream was passed. It was heated to 200 ° C. below and ring-opening polymerization was performed. After the reaction was completed in 1 hour, the polymer was taken out. The reduced specific viscosity of the obtained polymer was 1.67 dL / g. The hydrolysis resistance was good as shown in Table 1. Also, V
The MR was 75%.

【0024】実施例2 L-ラクチド20.0g、ステアリン酸58mg、1−デ
カノール32mg及びオクチル酸第1錫6mgのトルエ
ン溶液を撹拌装置、窒素導入管を備えた重合管に入れ、
2時間減圧乾燥したのち窒素気流下に200℃に加熱
し、開環重合した。1時間で反応を終了したのちポリマ
ーを取り出した。得られたポリマーの還元比粘度は1.
26dl/gであった。耐加水分解性は表1に示した様
に良好であった。また、VMRが91%であり、溶融安
定性も良好であった。
Example 2 A toluene solution of 20.0 g of L-lactide, 58 mg of stearic acid, 32 mg of 1-decanol and 6 mg of stannous octylate was placed in a polymerization tube equipped with a stirrer and a nitrogen introducing tube,
After drying under reduced pressure for 2 hours, it was heated to 200 ° C. under a nitrogen stream to carry out ring-opening polymerization. After the reaction was completed in 1 hour, the polymer was taken out. The reduced specific viscosity of the obtained polymer was 1.
It was 26 dl / g. The hydrolysis resistance was good as shown in Table 1. The VMR was 91%, and the melt stability was good.

【0025】実施例3 L-ラクチド17.0g、ステアリン酸114mg、ε−
カプロラクトン3.0g、1−デカノール32mg及び
オクチル酸第1錫6mgのトルエン溶液を撹拌装置、窒
素導入管を備えた重合管に入れ、2時間減圧乾燥したの
ち窒素気流下に200℃に加熱し、開環重合した。1.
5時間で反応を終了したのちポリマーを取り出した。得
られたポリマーの還元比粘度は1.01dl/gであっ
た。耐加水分解性は表1に示した様に良好であった。ま
た、VMRが89%であり、溶融安定性も良好であっ
た。
Example 3 17.0 g of L-lactide, 114 mg of stearic acid, ε-
A toluene solution of 3.0 g of caprolactone, 32 mg of 1-decanol and 6 mg of stannous octylate was placed in a polymerization tube equipped with a stirrer and a nitrogen introducing tube, dried under reduced pressure for 2 hours, and then heated to 200 ° C. under a nitrogen stream, Ring-opening polymerization was performed. 1.
After the reaction was completed in 5 hours, the polymer was taken out. The polymer obtained had a reduced specific viscosity of 1.01 dl / g. The hydrolysis resistance was good as shown in Table 1. The VMR was 89%, and the melt stability was good.

【0026】実施例4、5 表1示した組成以外は、実施例1と同様に行いポリマー
を得た。耐加水分解性評価結果を表1に示した。
Examples 4 and 5 Polymers were obtained in the same manner as in Example 1 except for the composition shown in Table 1. The results of the hydrolysis resistance evaluation are shown in Table 1.

【0027】比較例1 L-ラクチド20.0g及びオクチル酸第1錫6mgのト
ルエン溶液を撹拌装置、窒素導入管を備えた重合管に入
れ、2時間減圧乾燥したのち窒素気流下に200℃に加
熱し、開環重合した。1時間で反応を終了したのちポリ
マーを取り出した。得られたポリマーの還元比粘度は
2.19dl/gであった。耐加水分解性は表1に示し
た様に不良であった。また、VMRha0%であった。
Comparative Example 1 A toluene solution of 20.0 g of L-lactide and 6 mg of stannous octylate was placed in a polymerization tube equipped with a stirrer and a nitrogen introducing tube, dried under reduced pressure for 2 hours, and then heated to 200 ° C. under a nitrogen stream. It was heated and subjected to ring-opening polymerization. After the reaction was completed in 1 hour, the polymer was taken out. The reduced specific viscosity of the obtained polymer was 2.19 dl / g. The hydrolysis resistance was poor as shown in Table 1. The VMRha was 0%.

【0028】比較例2 L-ラクチド20.0g、ステアリン酸114mg及びオ
クチル酸第1錫6mgのトルエン溶液を撹拌装置、窒素
導入管を備えた重合管に入れ、2時間減圧乾燥したのち
窒素気流下に200℃に加熱し、開環重合した。1時間
で反応を終了したのちポリマーを取り出した。得られた
ポリマーの還元比粘度は1.88dl/gであった。耐
加水分解性評価結果を表1に示した。また、VMRは8
7%であった。
Comparative Example 2 A toluene solution of 20.0 g of L-lactide, 114 mg of stearic acid and 6 mg of stannous octylate was placed in a polymerization tube equipped with a stirrer and a nitrogen introducing tube, dried under reduced pressure for 2 hours, and then under a nitrogen stream. Then, the mixture was heated to 200 ° C. to carry out ring-opening polymerization. After the reaction was completed in 1 hour, the polymer was taken out. The reduced specific viscosity of the obtained polymer was 1.88 dl / g. The results of the hydrolysis resistance evaluation are shown in Table 1. Also, VMR is 8
It was 7%.

【0029】[0029]

【表1】 [Table 1]

【0030】[0030]

【発明の効果】以上の実施例からも明らかな様に、本発
明におけるポリ乳酸系樹脂は良好な耐加水分解性を有し
ており、従来からの問題点であった水中或いは湿度下で
の安定性が著しく改良されている。また、更には溶融時
の安定性をも向上させることが出来、よって、広範な用
途が期待できる。本発明のポリマーは産業界また環境問
題の解決に寄与するところが非常に大きい。
As is clear from the above examples, the polylactic acid-based resin of the present invention has good hydrolysis resistance, so that the polylactic acid-based resin of the present invention has a problem in the prior art such as water or humidity. The stability is significantly improved. Further, the stability at the time of melting can be further improved, so that a wide range of applications can be expected. The polymer of the present invention greatly contributes to solving industrial and environmental problems.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 伊藤 武 滋賀県大津市堅田二丁目1番1号 東洋紡 績株式会社総合研究所内 (72)発明者 有地 美奈子 滋賀県大津市堅田二丁目1番1号 東洋紡 績株式会社総合研究所内 (72)発明者 堀田 清史 滋賀県大津市堅田二丁目1番1号 東洋紡 績株式会社総合研究所内 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Takeshi Ito 2-1-1 Katata, Otsu City, Shiga Toyobo Co., Ltd. (72) Inventor Minako Arichi 2-1-1 Katata, Otsu City, Shiga Prefecture No. Toyobo Co., Ltd. Research Institute (72) Inventor Kiyoshi Hotta 2-1-1 Katata, Otsu City, Shiga Prefecture Toyobo Co., Ltd. Research Institute

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 下記一般式(I)で表される酸末端が実
質的に封鎖されていることを特徴とする酸末端封鎖ポリ
乳酸。 【化1】 (式中、Xは水素原子又は炭化水素基、Yは炭素数1以
上50以下の1価以上の多価脂肪族炭化水素基、そして
nは10以上、lは1以上の正の整数を示す。)
1. An acid end-capped polylactic acid characterized in that the acid end represented by the following general formula (I) is substantially capped. [Chemical 1] (In the formula, X represents a hydrogen atom or a hydrocarbon group, Y represents a monovalent or more polyvalent aliphatic hydrocarbon group having 1 to 50 carbon atoms, and n represents a positive integer of 10 or more and 1 or more. .)
【請求項2】 上記一般式(I)で表されるXの70%
以上が炭素数2以上50以下のアシル基であることを特
徴とする請求項1記載の酸末端封鎖ポリ乳酸。
2. 70% of X represented by the general formula (I)
The acid end-capped polylactic acid according to claim 1, wherein the above is an acyl group having 2 to 50 carbon atoms.
JP10979194A 1993-08-19 1994-05-24 Acid-blocked polylactic acid Expired - Lifetime JP3367577B2 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP10979194A JP3367577B2 (en) 1994-05-24 1994-05-24 Acid-blocked polylactic acid
US08/285,552 US5618911A (en) 1993-08-19 1994-08-03 Polymer containing lactic acid as its constituting unit and method for producing the same
CN03108626.8A CN1216882C (en) 1993-08-19 1994-08-04 Process for purifying lactide formed through ring-opening polymerization
CN94115768A CN1051095C (en) 1993-08-19 1994-08-04 Polymer containing lactic acid as its constituting unit and method for producing the same
US08/734,474 US5714618A (en) 1993-08-19 1997-01-09 Polymer containing lactic acid as its constituting unit and method for producing the same
CN99117996.XA CN1129595C (en) 1993-08-19 1999-08-20 Process for preparing cyclodiester used to produce polymer containing structural unit of lactic acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10979194A JP3367577B2 (en) 1994-05-24 1994-05-24 Acid-blocked polylactic acid

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP2002267142A Division JP2003137983A (en) 2002-09-12 2002-09-12 Polylactic acid

Publications (2)

Publication Number Publication Date
JPH07316273A true JPH07316273A (en) 1995-12-05
JP3367577B2 JP3367577B2 (en) 2003-01-14

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ID=14519318

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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0959218A (en) * 1995-08-25 1997-03-04 Shimadzu Corp L-lactic acid oligomer derivative
JP2002030208A (en) * 2000-07-14 2002-01-31 Toray Ind Inc Polylactic acid resin composition and molded article
JP2004526043A (en) * 2001-05-07 2004-08-26 コーネル・リサーチ・ファンデーション・インコーポレイテッド Biodegradable copolymer attached to segments with multiple functional groups
US7129190B2 (en) 2004-02-12 2006-10-31 Nisshinbo Industries, Inc. Fiber article comprising a biodegradable plastic
JP2009024058A (en) * 2007-07-18 2009-02-05 Biobase Kk Polylactic acid resin composition and additive for polylactic acid resin
WO2009119336A1 (en) 2008-03-25 2009-10-01 東レ株式会社 Polylactic acid composition, and film comprising the same
US7687054B2 (en) 1997-02-07 2010-03-30 3M Innovative Properties Company Biocompatible compounds for sustained release pharmaceutical drug delivery systems
WO2013133542A1 (en) * 2012-03-09 2013-09-12 경상대학교 산학협력단 Method for controlling degradation of biodegradable polyester and degradation-controlled biodegradable polyester
KR101501683B1 (en) * 2012-03-23 2015-03-11 주식회사 엘지화학 Preparation method of polylactide resin having low acidity, and polylactide resin prepared therefrom
WO2017170423A1 (en) * 2016-03-29 2017-10-05 国立大学法人北海道大学 Alcohol-terminated polyester and polyester production method

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0959218A (en) * 1995-08-25 1997-03-04 Shimadzu Corp L-lactic acid oligomer derivative
US7687054B2 (en) 1997-02-07 2010-03-30 3M Innovative Properties Company Biocompatible compounds for sustained release pharmaceutical drug delivery systems
JP2002030208A (en) * 2000-07-14 2002-01-31 Toray Ind Inc Polylactic acid resin composition and molded article
JP2004526043A (en) * 2001-05-07 2004-08-26 コーネル・リサーチ・ファンデーション・インコーポレイテッド Biodegradable copolymer attached to segments with multiple functional groups
US7129190B2 (en) 2004-02-12 2006-10-31 Nisshinbo Industries, Inc. Fiber article comprising a biodegradable plastic
JP2009024058A (en) * 2007-07-18 2009-02-05 Biobase Kk Polylactic acid resin composition and additive for polylactic acid resin
WO2009119336A1 (en) 2008-03-25 2009-10-01 東レ株式会社 Polylactic acid composition, and film comprising the same
US8575254B2 (en) 2008-03-25 2013-11-05 Toray Industries, Inc. Polylactic acid-based composition and film formed thereof
WO2013133542A1 (en) * 2012-03-09 2013-09-12 경상대학교 산학협력단 Method for controlling degradation of biodegradable polyester and degradation-controlled biodegradable polyester
KR101397853B1 (en) * 2012-03-09 2014-05-20 경상대학교산학협력단 Method for Controlling Degradation of Biodegradable Polyester and Degradation-Controlled Biodegradable Polyester
KR101501683B1 (en) * 2012-03-23 2015-03-11 주식회사 엘지화학 Preparation method of polylactide resin having low acidity, and polylactide resin prepared therefrom
WO2017170423A1 (en) * 2016-03-29 2017-10-05 国立大学法人北海道大学 Alcohol-terminated polyester and polyester production method
JPWO2017170423A1 (en) * 2016-03-29 2019-02-07 国立大学法人北海道大学 Alcohol-terminated polyester and method for producing polyester

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