JPH0570574A - Production of aliphatic polyester - Google Patents

Production of aliphatic polyester

Info

Publication number
JPH0570574A
JPH0570574A JP23023291A JP23023291A JPH0570574A JP H0570574 A JPH0570574 A JP H0570574A JP 23023291 A JP23023291 A JP 23023291A JP 23023291 A JP23023291 A JP 23023291A JP H0570574 A JPH0570574 A JP H0570574A
Authority
JP
Japan
Prior art keywords
acid
polyester
aliphatic polyester
catalyst
weight
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
JP23023291A
Other languages
Japanese (ja)
Other versions
JP3046660B2 (en
Inventor
Eiichiro Takiyama
栄一郎 滝山
Shigekatsu Seki
重勝 関
Tadayuki Hosogane
忠幸 細金
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.)
Resonac Holdings Corp
Original Assignee
Showa Highpolymer 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 Showa Highpolymer Co Ltd filed Critical Showa Highpolymer Co Ltd
Priority to JP3230232A priority Critical patent/JP3046660B2/en
Publication of JPH0570574A publication Critical patent/JPH0570574A/en
Application granted granted Critical
Publication of JP3046660B2 publication Critical patent/JP3046660B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Polyesters Or Polycarbonates (AREA)

Abstract

PURPOSE:To produce an aliph. polyester having a high m.p. and strengths sufficient for practical use with an extremely small amt. of a catalyst used. CONSTITUTION:An aliph. polyester having a softening point of at least 70 deg.C and a number-average mol. wt. of at leant 10,000 is produced by esterifying 1,4-butanediol with a dicarboxyic acid component consisting of 50-100mol% succinic acid and 50-0mol% dicarboxylic acid selected from the group consisting of adipic, sebacic, and lauric acids and eliminating the glycol maleules in the presence thence of 0.0001-0.1 pt.wt. (based on 100 pts.wt. the polyester) titanium (oxy) acetylacetonate as a catalyst.

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、実用上十分な強度を有
し且つ融点が高く、用いる触媒が非常に少ない脂肪族ポ
リエステルを製造するための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 an aliphatic polyester having a practically sufficient strength, a high melting point, and a very small amount of catalyst.

【0002】[0002]

【従来の技術および課題】脂肪族飽和ポリエステルは融
点が低く、たとえ数平均分子量が10,000以上の高分子領
域にあった場合でも、飽和芳香族構造を含むポリエステ
ル、例えばポリエチレンテレフタレートのように実用上
十分な機械的物性を示さないため、今迄実用性がないも
のとされていた。実際、フィルム形成性がある場合で
も、製造されたフィルムは、引裂き強度や引張強度が要
求される性能に及ばず、実用に耐えるものではなかっ
た。これらの中でも、1,4−ブタンジオールをグリコー
ル成分とする脂肪族ポリエステルは、比較的強度があ
り、とくにコハク酸をジカルボン酸として用いた脂肪族
ポリエステルは、融点も110〜115℃と高く、特異
的である。但し、数平均分子量が十分に高くない場合
は、やや硬く、もろい傾向も認められ、フレキシビリテ
ィを付与する場合には、アジピン酸、セバシン酸、ドデ
カン酸といったメチレン結合の多いジカルボン酸の併用
が望ましい。従来、数平均分子量10,000以上の高分子量
ポリエステルを製造するためには、例えばポリエチレン
テレフタレートの場合では、テレフタル酸1モル当たり
0.001〜0.1モル%のアンチモン、亜鉛、チタン、鉛、マ
ンガン、ゲルマニウム、ジルコニウム等の重金属の有
機、無機の化合物が、脱グリコール反応の触媒に用いら
れている。また、リチウム化合物を併用することも知ら
れている。前記触媒の量は、一般にポリエチレンテレフ
タレート100重量部当たりに換算すると、0.1〜1
重量部となり、これ以下の触媒量では高分子量ポリエス
テルを得ることが難しいとされていた。しかし、実用
上、取扱い、またはゴミとして排出されるような場合、
安全性の面からは、前記触媒は極力、少量で使用するこ
とが望まれる。本発明は、上記のような従来の課題を解
決し、実用上十分な強度を有し且つ融点も高く、何より
も使用する触媒量を非常に少量とすることのできる脂肪
族ポリエステルの製造方法を提供することを目的とする
ものである。
BACKGROUND OF THE INVENTION Aliphatic saturated polyesters have a low melting point, and even if they have a number average molecular weight of 10,000 or more in a high molecular weight region, polyesters containing a saturated aromatic structure, such as polyethylene terephthalate, are practically sufficient. Until now, it has been considered impractical because it does not exhibit such mechanical properties. In fact, even if the film has a film-forming property, the produced film did not reach the performance required for the tear strength and the tensile strength and was not practically usable. Among them, the aliphatic polyester containing 1,4-butanediol as a glycol component has relatively high strength, and particularly the aliphatic polyester using succinic acid as a dicarboxylic acid has a high melting point of 110 to 115 ° C. Target. However, when the number average molecular weight is not sufficiently high, a slightly hard and fragile tendency is also recognized, and in the case of imparting flexibility, it is desirable to use a combination of dicarboxylic acids having many methylene bonds such as adipic acid, sebacic acid, and dodecanoic acid. .. Conventionally, in order to produce a high-molecular-weight polyester having a number-average molecular weight of 10,000 or more, for example, in the case of polyethylene terephthalate, per 1 mol of terephthalic acid
Organic and inorganic compounds of 0.001 to 0.1 mol% of heavy metals such as antimony, zinc, titanium, lead, manganese, germanium and zirconium are used as catalysts for the deglycolization reaction. It is also known to use a lithium compound in combination. Generally, the amount of the catalyst is 0.1 to 1 in terms of 100 parts by weight of polyethylene terephthalate.
It has been considered to be difficult to obtain a high molecular weight polyester with a catalyst amount of less than this. However, in practical use, if it is handled or discharged as garbage,
From the viewpoint of safety, it is desirable to use the catalyst in a small amount as much as possible. The present invention solves the above-mentioned conventional problems, has a practically sufficient strength and a high melting point, and above all, a method for producing an aliphatic polyester which can use a very small amount of a catalyst. It is intended to be provided.

【0003】[0003]

【課題を解決するための手段】本発明者らは鋭意検討の
結果、上記のような課題を解決することができた。すな
わち本発明は、1,4−ブタンジオールと、50〜100
モル%のコハク酸および50〜0モル%のアジピン酸、
セバシン酸およびドデカン酸から選ばれた少なくとも一
種のジカルボン酸とをエステル化し、次いで脱グリコー
ル反応させて融点70℃以上且つ数平均分子量10,000以
上の脂肪族ポリエステルを製造するに際して、該脂肪族
ポリエステル100重量部に対し、触媒として0.0001〜
0.1重量部のチタン(オキシ)アセチルアセトネートを
用いることを特徴とする、脂肪族ポリエステルの製造方
法を提供するものである。
As a result of earnest studies, the present inventors were able to solve the above problems. That is, the present invention comprises 1,4-butanediol and 50-100
Mol% succinic acid and 50-0 mol% adipic acid,
When at least one dicarboxylic acid selected from sebacic acid and dodecanoic acid is esterified, and then deglycolized, an aliphatic polyester having a melting point of 70 ° C. or higher and a number average molecular weight of 10,000 or higher is produced. As a catalyst, 0.0001 ~
The present invention provides a method for producing an aliphatic polyester, which comprises using 0.1 part by weight of titanium (oxy) acetylacetonate.

【0004】以下に、本発明をさらに詳細に説明する。
なお、特記しない限り、数平均分子量を単に分子量と表
す。本発明者らは、1,4−ブタンジオールとコハク酸、
並びに必要に応じてアジピン酸、セバシン酸またはドデ
カン酸を併用して、分子量10,000以上の脂肪族ポリエス
テルを合成するに際して、極力少量で有効な触媒につい
て検討した結果、あるチタン系触媒が、生成ポリエステ
ル100重量部に対して0.1重量部以下という少量で
も有効であることを見出し、本発明を完成することがで
きた。
The present invention will be described in more detail below.
Unless otherwise specified, the number average molecular weight is simply referred to as the molecular weight. The present inventors have found that 1,4-butanediol and succinic acid,
In addition, when adipic acid, sebacic acid or dodecanoic acid is used in combination, if necessary, when synthesizing an aliphatic polyester having a molecular weight of 10,000 or more, a catalyst effective as small as possible was examined. It was found that even a small amount of 0.1 parts by weight or less with respect to parts by weight was effective, and the present invention could be completed.

【0005】1,4−ブタンジオールとコハク酸、並びに
必要に応じてアジピン酸、セバシン酸またはドデカン酸
とからなる飽和ポリエステルの製造は、公知技術で行う
ことができる。この飽和ポリエステルを製造する際のエ
ステル化反応および脱グリコール反応条件は、従来から
用いられる適切な条件を設定することができ、とくに制
限されない。1,4−ブタンジオールの使用量は、コハク
酸またはコハク酸とアジピン酸、セバシン酸およびドデ
カン酸から選ばれた少なくとも一種のジカルボン酸との
混合酸100モル%に対し、実質的に等モルであるが、
一般にはエステル化中の溜出があることから、5〜20
モル%過剰に用いることが行われる。1,4−ブタンジオ
ールと併用する酸は、コハク酸のみも使用することがで
きる。これとは別に、コハク酸と、アジピン酸、セバシ
ン酸およびドデカン酸から選ばれた少なくとも一種のジ
カルボン酸(酸無水物も含む)系の混合酸におけるそれ
ぞれの成分の好適な混合割合は、通常、コハク酸が50
モル%以上、好ましくは60モル%以上、アジピン酸等
のジカルボン酸が50モル%以下、好ましくは40モル
%以下がよい。コハク酸と併用する前記ジカルボン酸が
50モル%を超えると、得られる飽和ポリエステルの融
点が70℃以下となり、実用上好ましくない。
The production of a saturated polyester composed of 1,4-butanediol and succinic acid, and optionally adipic acid, sebacic acid or dodecanoic acid can be carried out by a known technique. The esterification reaction and deglycolization reaction conditions for producing this saturated polyester can be set to appropriate conditions conventionally used, and are not particularly limited. The amount of 1,4-butanediol used is substantially equimolar to 100 mol% of succinic acid or a mixed acid of succinic acid and at least one dicarboxylic acid selected from adipic acid, sebacic acid and dodecanoic acid. But
Generally, there is a distillate during esterification, so 5-20
Use in molar excess is performed. As the acid used in combination with 1,4-butanediol, only succinic acid can be used. Apart from this, a suitable mixing ratio of each component in succinic acid and at least one dicarboxylic acid (including acid anhydride) -based mixed acid selected from adipic acid, sebacic acid and dodecanoic acid is usually 50 succinic acid
The amount of the dicarboxylic acid such as adipic acid is 50 mol% or less, preferably 40 mol% or less. When the amount of the dicarboxylic acid used in combination with succinic acid exceeds 50 mol%, the melting point of the obtained saturated polyester becomes 70 ° C. or lower, which is not preferable in practice.

【0006】本発明に用いられる触媒は、構造式The catalyst used in the present invention has a structural formula

【0007】[0007]

【化1】 [Chemical 1]

【0008】で示されるチタン(オキシ)アセチルアセ
トネートである。この触媒の使用量は、1,4−ブタンジ
オールとコハク酸、並びに必要に応じてアジピン酸、セ
バシン酸またはドデカン酸とを反応させて得られた飽和
ポリエステル100重量部に対し、0.0001〜0.1重量
部、好ましくは0.001重量部〜0.05重量部がよい。使
用量が0.0001重量部未満では、触媒の作用が弱くなり、
目的とする分子量を得ることが困難となる。また、0.
1重量部を超える使用量としても、その作用は大きく変
わることがない。チタン化合物以外の触媒では、前記使
用範囲内では高分子量ポリエステルを合成できるものは
見出せなかった。上記のように製造した脂肪族ポリエス
テルは、実用上十分な強度およびフレキシビリティを有
し、さらに融点も高いので各種用途に合わせて、各種の
成形方法を利用できる。例えばこれを用いてフィルムを
形成する場合は、公知のフィルム形成方法を利用でき、
とくに制限されない。また、成形時に、その用途に応じ
て各種の成形助剤、例えばフィラー(無機、有機)、着
色剤、補強材、ワックス類、熱可塑性ポリマー、オリゴ
マー等を併用することもできる。
It is titanium (oxy) acetylacetonate represented by: The amount of this catalyst to be used is 0.0001 to 0.001 with respect to 100 parts by weight of a saturated polyester obtained by reacting 1,4-butanediol with succinic acid, and optionally with adipic acid, sebacic acid or dodecanoic acid. 1 part by weight, preferably 0.001 part by weight to 0.05 part by weight. If the amount used is less than 0.0001 parts by weight, the action of the catalyst becomes weak,
It becomes difficult to obtain the target molecular weight. Also, 0.
Even if the amount used exceeds 1 part by weight, the action does not change significantly. With respect to catalysts other than titanium compounds, no catalyst capable of synthesizing a high molecular weight polyester was found within the above range of use. The aliphatic polyester produced as described above has practically sufficient strength and flexibility, and also has a high melting point, so various molding methods can be used according to various applications. For example, when forming a film using this, a known film forming method can be used,
There is no particular limitation. Further, at the time of molding, various molding aids such as fillers (inorganic or organic), colorants, reinforcing materials, waxes, thermoplastic polymers, oligomers and the like can be used in combination depending on the application.

【0009】[0009]

【実施例】以下、実施例によって本発明を説明する。実施例 1 撹拌機、分溜コンデンサー、温度計、ガス導入管を備え
た1l容セパラブルフラスコに、1,4−ブタンジオール2
50g、コハク酸290g、チタン(オキシ)アセチル
アセトネート0.05g(約0.01phr)を仕込み、2
10〜220℃、窒素気流中でエステル化して酸価を
9.6とした後、最終的には0.5Torrまで減圧し、21
5〜220℃で8時間脱グリコール反応を行い、分子量
16,100の飽和ポリエステル(A)(Shodex GPC SYSTEM
-11、昭和電工社製を用いたGPC分析の結果)が得ら
れた。室温まで冷却すると、白色ワックス状の結晶とな
り、融点は113℃であった。これとは別に、チタン
(オキシ)アセチルアセトネートを使用しないで同一条
件で反応させた場合は、得られた脂肪族ポリエステルの
分子量は5,800であり、大きな差が認められた。
EXAMPLES The present invention will be described below with reference to examples. Example 1 A 1-liter separable flask equipped with a stirrer, a fractionating condenser, a thermometer, and a gas introduction tube was charged with 1,4-butanediol 2
Charge 50 g, succinic acid 290 g, and titanium (oxy) acetylacetonate 0.05 g (about 0.01 phr).
After esterification in a nitrogen stream at 10 to 220 ° C to an acid value of 9.6, the pressure was finally reduced to 0.5 Torr, and
Deglycol reaction at 5 ~ 220 ℃ for 8 hours, molecular weight
16,100 saturated polyester (A) (Shodex GPC SYSTEM
-11, the result of GPC analysis using Showa Denko) was obtained. When cooled to room temperature, it became white waxy crystals and had a melting point of 113 ° C. Separately, when the reaction was carried out under the same conditions without using titanium (oxy) acetylacetonate, the obtained aliphatic polyester had a molecular weight of 5,800, showing a large difference.

【0010】実施例 2 撹拌機、分溜コンデンサー、温度計、ガス導入管を備え
た1l容セパラブルフラスコに、1,4−ブタンジオール2
50g、コハク酸232g、アジピン酸58g、チタン
(オキシ)アセチルアセトネート0.02g(約0.004ph
r)を仕込み、窒素気流中210〜215℃でエステル
化して酸価を6.7とした後、最終的には0.5Torrまで
減圧し、210〜215℃で12時間脱グリコールを行
い、分子量16,900の飽和ポリエステル(B)が得られ
た。室温まで冷却すると、わずかに黄褐色を帯びた白色
ワックス状となった。融点は約95℃であった。これと
は別に、チタン(オキシ)アセチルアセトネートを使用
しないで同一条件で反応させた場合は、得られた脂肪族
ポリエステルの分子量は6,600でり、大きな差が認めら
れた。
Example 2 In a 1-liter separable flask equipped with a stirrer, a fractionating condenser, a thermometer, and a gas inlet tube, 1,4-butanediol 2 was added.
50g, succinic acid 232g, adipic acid 58g, titanium (oxy) acetylacetonate 0.02g (about 0.004ph
r) was charged, and the acid value was adjusted to 6.7 by esterification in a nitrogen stream at 210 to 215 ° C, and finally the pressure was reduced to 0.5 Torr and deglycollation was performed at 210 to 215 ° C for 12 hours to obtain a molecular weight. 16,900 saturated polyesters (B) were obtained. When cooled to room temperature, it became a white wax with a slight tan color. The melting point was about 95 ° C. Separately, when the reaction was performed under the same conditions without using titanium (oxy) acetylacetonate, the obtained aliphatic polyester had a molecular weight of 6,600, showing a large difference.

【0011】実施例 3 撹拌機、分溜コンデンサー、温度計、ガス導入管を備え
た2l容セパラブルフラスコに、1,4−ブタンジオール4
95g、コハク酸406g、ドテカン酸339g、チタ
ン(オキシ)アセチルアセトネート0.025g(約0.002ph
r)を仕込み、窒素気流中210〜215℃でエステル
化して酸価を7.9とした後、最終的には0.5Torrまで
減圧し、210〜215℃で10時間脱グリコール反応
を行った。得られた飽和ポリエステル(C)の分子量は
15,900、融点は約80℃、室温まで冷却すると白色ワッ
クス状となった。
Example 3 A 4-liter separable flask equipped with a stirrer, a fractionating condenser, a thermometer, and a gas introduction tube was charged with 1,4-butanediol 4
95 g, succinic acid 406 g, dotecanoic acid 339 g, titanium (oxy) acetylacetonate 0.025 g (about 0.002 ph
r) was charged, and the acid value was adjusted to 7.9 by esterification in a nitrogen stream at 210 to 215 ° C., and finally the pressure was reduced to 0.5 Torr and a deglycolization reaction was performed at 210 to 215 ° C. for 10 hours. .. The molecular weight of the obtained saturated polyester (C) is
The melting point was 15,900 and the melting point was about 80 ° C. When cooled to room temperature, it became a white wax.

【0012】[0012]

【発明の効果】本発明によって、実用上十分な強度を有
し且つ融点も高く、さらに使用する触媒量を非常に少量
とすることのできる脂肪族ポリエステルの製造方法が提
供される。
The present invention provides a process for producing an aliphatic polyester which has practically sufficient strength, has a high melting point, and can use a very small amount of catalyst.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 1,4−ブタンジオールと、50〜100
モル%のコハク酸および50〜0モル%のアジピン酸、
セバシン酸およびドデカン酸から選ばれた少なくとも一
種のジカルボン酸とをエステル化し、次いで脱グリコー
ル反応させて融点70℃以上且つ数平均分子量10,000以
上の脂肪族ポリエステルを製造するに際して、 該脂肪族ポリエステル100重量部に対し、触媒として
0.0001〜0.1重量部のチタン(オキシ)アセチルアセト
ネートを用いることを特徴とする、脂肪族ポリエステル
の製造方法。
1. 1,4-butanediol and 50 to 100
Mol% succinic acid and 50-0 mol% adipic acid,
When at least one dicarboxylic acid selected from sebacic acid and dodecanoic acid is esterified and then deglycolized to produce an aliphatic polyester having a melting point of 70 ° C. or more and a number average molecular weight of 10,000 or more, 100 parts by weight of the aliphatic polyester is used. As a catalyst for
A method for producing an aliphatic polyester, which comprises using 0.0001 to 0.1 part by weight of titanium (oxy) acetylacetonate.
JP3230232A 1991-09-10 1991-09-10 Method for producing aliphatic polyester Expired - Fee Related JP3046660B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3230232A JP3046660B2 (en) 1991-09-10 1991-09-10 Method for producing aliphatic polyester

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3230232A JP3046660B2 (en) 1991-09-10 1991-09-10 Method for producing aliphatic polyester

Publications (2)

Publication Number Publication Date
JPH0570574A true JPH0570574A (en) 1993-03-23
JP3046660B2 JP3046660B2 (en) 2000-05-29

Family

ID=16904610

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3230232A Expired - Fee Related JP3046660B2 (en) 1991-09-10 1991-09-10 Method for producing aliphatic polyester

Country Status (1)

Country Link
JP (1) JP3046660B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004108792A3 (en) * 2003-04-10 2005-03-24 Vinod Chintamani Malshe Novel biodegradable aliphatic polyesters and pharmaceutical compositions and applications thereof
US20130078431A1 (en) * 2011-09-28 2013-03-28 Casio Computer Co., Ltd. Composition for label base, method for producing label base, and label

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004108792A3 (en) * 2003-04-10 2005-03-24 Vinod Chintamani Malshe Novel biodegradable aliphatic polyesters and pharmaceutical compositions and applications thereof
US20130078431A1 (en) * 2011-09-28 2013-03-28 Casio Computer Co., Ltd. Composition for label base, method for producing label base, and label

Also Published As

Publication number Publication date
JP3046660B2 (en) 2000-05-29

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