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JPH06181784A - Production of copolyester - Google Patents

Production of copolyester

Info

Publication number
JPH06181784A
JPH06181784A JP4315246A JP31524692A JPH06181784A JP H06181784 A JPH06181784 A JP H06181784A JP 4315246 A JP4315246 A JP 4315246A JP 31524692 A JP31524692 A JP 31524692A JP H06181784 A JPH06181784 A JP H06181784A
Authority
JP
Japan
Prior art keywords
alcaligenes
copolymer
units
butyrolactone
carbon source
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.)
Pending
Application number
JP4315246A
Other languages
Japanese (ja)
Inventor
Yoshiharu Doi
義治 土肥
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.)
Mitsubishi Kasei Corp
Original Assignee
Mitsubishi Kasei Corp
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 Mitsubishi Kasei Corp filed Critical Mitsubishi Kasei Corp
Priority to JP4315246A priority Critical patent/JPH06181784A/en
Publication of JPH06181784A publication Critical patent/JPH06181784A/en
Pending legal-status Critical Current

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  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Biological Depolymerization Polymers (AREA)

Abstract

PURPOSE:To obtain a copolyester having adequate mechanical strength, biocompatibility and biodegradability, useful as e.g. a medical material, by culture of a kind of Alcaligenes bacteria using, as carbon source, a combination of sucrose, gamma-butyrolactone, 4-hydroxybutyric acid and a specific glycol. CONSTITUTION:A medium comprising (A) as carbon source, a combination of sucrose, gamma-butyrolactone, 4-hydroxybutyric acid and an alkylene glycol of formula HO(CH2)nOH (n is an even number of 4-12) and (B) as nitrogen source, an inorganic nitrogen compound such as ammonia, ammonium salt or nitrate, or an organic nitrogen compound such as urea, casein or peptone, is inoculated with a kind of Alcaligenes bacteria [e.g. Alcaligenes latas (ATCC 29713)] to conduct shaking culture at 30 deg.C for 48hr, and the resultant microbes are separated and dried, and then subjected to extraction with hot chloroform, thus affording the objective copolyester made up of 97-80mol% of 3-hydroxybutyrate unit and 3-20mol% of 4-hydroxybutyrate unit.

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3−ヒドロキシブチレー
ト単位(以下3HB単位と記す)と4−ヒドロキシブチ
レート単位(以下4HB単位と記す)からなるポリエス
テル共重合体の製造方法に関する。詳しくは生産性の改
善された生分解性ポリエステル共重合体の製造方法に関
する。
FIELD OF THE INVENTION The present invention relates to a method for producing a polyester copolymer comprising 3-hydroxybutyrate units (hereinafter referred to as 3HB units) and 4-hydroxybutyrate units (hereinafter referred to as 4HB units). More specifically, it relates to a method for producing a biodegradable polyester copolymer having improved productivity.

【0002】[0002]

【従来の技術】ポリ−3−ヒドロキシブチレート(以下
PHBと記す)は、エネルギー貯蔵物質として数多くの
微生物の菌体内に蓄積され、優れた生物分解性と生体適
合性を示す熱可塑性高分子であることから、環境を保全
するクリーンプラスチックとして注目され、手術糸や骨
折固定用材等の医用材料および医薬や農薬を徐々に放出
する徐放性システム等の多方面への応用が長年にわたり
期待されてきた。特に近年、合成プラスチックが環境汚
染や資源循環の観点から深刻な社会問題となるに到り、
PHBおよびその共重合体は石油に依存しないバイオポ
リマーとして注目されている。しかしながら、PHBは
耐衝撃性に劣るという物性上の問題があった。
2. Description of the Related Art Poly-3-hydroxybutyrate (hereinafter referred to as PHB) is a thermoplastic polymer that accumulates in the cells of many microorganisms as an energy storage substance and exhibits excellent biodegradability and biocompatibility. Therefore, it has attracted attention as a clean plastic that preserves the environment, and it has been expected for many years to be applied to various fields such as medical materials such as surgical threads and materials for fixing bone fractures, and sustained-release systems that gradually release drugs and pesticides. It was Particularly in recent years, synthetic plastics have become a serious social problem from the viewpoint of environmental pollution and resource recycling,
PHB and its copolymers are attracting attention as petroleum-independent biopolymers. However, PHB has a problem in physical properties that it is inferior in impact resistance.

【0003】近時、3HB単位および3−ヒドロキシバ
リレート単位(以下3HV単位と記す)を含有する共重
合体およびその製造法について、研究開発がなされ、た
とえば特開昭57−150393号、特開昭59−22
0192号に記載されている。しかしながら、3HV単
位含有率の高い共重合体は耐熱性に劣っていた。すなわ
ち、共重合体の3HV単位が0から33モル%まで増大
するとこの増大に伴って融解温度(Tm)が185℃か
ら85℃まで急激に低下することが知られていた(T.
L.Bluhm et al Macromolecu
les,19,2871(1986)。
Recently, a copolymer containing 3HB units and 3-hydroxyvalerate units (hereinafter referred to as 3HV units) and a method for producing the same have been researched and developed, for example, JP-A-57-150393. Sho 59-22
No. 0192. However, the copolymer having a high 3HV unit content was inferior in heat resistance. That is, it was known that when the 3HV unit of the copolymer increased from 0 to 33 mol%, the melting temperature (Tm) rapidly decreased from 185 ° C. to 85 ° C. with this increase (T.
L. Bluhm et al Macromolecule
les, 19, 2871 (1986).

【0004】一方、3HB単位および4HB単位を含有
する共重合体およびその製造法についても、研究開発が
なされ、たとえば特開平1−48821,1−2227
88,1−304891,2−27992に記載されて
いる。かかる共重合体は4HB単位の含有率が高い場合
でも高い融点を有し、耐衝撃性が改良されることから工
業的な価値が高い。
On the other hand, research and development have also been carried out on copolymers containing 3HB units and 4HB units and methods for producing the same, for example, Japanese Patent Laid-Open No. 48821, 1-22227.
88, 1-304891, 279292. Such a copolymer has a high melting point even when the content of 4HB units is high, and since the impact resistance is improved, it has a high industrial value.

【0005】しかし上記3HB単位および4HB単位を
含有する共重合体の製造方法は、炭素源としてフルクト
ースを使用する方法、あるいはγ−ブチロラクトン、4
−ヒドロキシ酪酸、又はHO(CH2 n OH(nは4
〜12の偶数)で表わされる化合物を使用する方法しか
報告されていない。そのため工業的規模で生産するには
生産性および原料のコスト面に問題があった。
However, the method for producing a copolymer containing the above 3HB units and 4HB units is a method using fructose as a carbon source, or γ-butyrolactone, 4
- hydroxybutyric acid, or HO (CH 2) n OH ( n is 4
Only a method using a compound represented by (even number of -12) has been reported. Therefore, there is a problem in productivity and cost of raw materials for production on an industrial scale.

【0006】[0006]

【本発明が解決しようとする課題】本発明の目的は安価
な原料を主体として使用した生産性の優れた3HB単位
および4HB単位からなる共重合体の製造方法を提供す
ることである。
SUMMARY OF THE INVENTION An object of the present invention is to provide a method for producing a copolymer comprising 3HB units and 4HB units, which is mainly composed of inexpensive raw materials and has excellent productivity.

【0007】[0007]

【課題を解決するための手段】本発明者らは3HB単位
および4HB単位からなる共重合体を工業的に有利に生
産できる方法について鋭意検討した結果、アルカリゲネ
ス属菌、特にアルカリゲネス ラタスの存在下に、特定
の炭素源をショ糖と組み合せて使用することにより特定
の3HB単位および4HB単位からなる共重合体が効率
よく生産できること、また、γ−ブチロラクトン等の高
価な炭素源を高効率で4HB単位として共重合体中に導
入できることを見出し、本発明に到達した。
Means for Solving the Problems The inventors of the present invention have made earnest studies on a method capable of industrially producing a copolymer consisting of 3HB units and 4HB units. As a result, in the presence of Alcaligenes spp., Particularly Alcaligenes rattus. , A copolymer comprising a specific 3HB unit and a specific 4HB unit can be efficiently produced by using a specific carbon source in combination with sucrose, and an expensive carbon source such as γ-butyrolactone is highly efficiently used in a 4HB unit. As a result, they have found that they can be introduced into a copolymer, and have reached the present invention.

【0008】即ち本発明の要旨は、3−ヒドロキシブチ
レート単位97〜80モル%および4−ヒドロキシブチ
レート単位3〜20モル%からなるポリエステル共重合
体を、アルカリゲネス属菌の存在下に製造する方法にお
いて、炭素源としてショ糖およびγ−ブチロラクトン、
4−ヒドロキシ酪酸、HO(CH2 n OH(nは4〜
12の偶数)で表わされる化合物から選ばれた少なくと
も1つとを併用することを特徴とするポリエステル共重
合体の製造方法に存する。
That is, the gist of the present invention is to produce a polyester copolymer comprising 97 to 80 mol% of 3-hydroxybutyrate units and 3 to 20 mol% of 4-hydroxybutyrate units in the presence of Alcaligenes. In the method, sucrose and γ-butyrolactone as carbon sources,
4-hydroxybutyric acid, HO (CH 2 ) n OH (n is 4 to
The present invention also relates to a method for producing a polyester copolymer, characterized in that it is used in combination with at least one selected from compounds represented by the even number 12).

【0009】以下、本発明を詳細に説明する。本発明の
ポリエステル共重合体は、3HB単位97〜80モル%
および4HB単位3〜20%からなる。ここで、3HB
単位および4HB単位は各々次式で表される構成単位で
ある。
The present invention will be described in detail below. The polyester copolymer of the present invention contains 3 to 80 mol% of HB units.
And 4HB units 3-20%. Where 3HB
The unit and the 4HB unit are constituent units represented by the following formulas, respectively.

【0010】[0010]

【化1】 3HB単位; −OCH(CH3 )CH2 CO− 4HB単位; −OCH2 CH2 CH2 CO−## STR1 ## 3HB units; -OCH (CH 3) CH 2 CO- 4HB units; -OCH 2 CH 2 CH 2 CO-

【0011】本発明で使用される微生物については、P
HB生産能を有するアルカリゲネス属であれば、特に限
定されないが、例えばアルカリゲネス フェカリス(A
lcaligenes faecalic)、アルカリ
ゲネス ルーランディィ(Alcaligenes r
uhlandii)、アルカリゲネス ラタス(Alc
aligenes ratus)、アルカリゲネス ユ
ウトロフス(Alcaligenes eutroph
s)等であり、これらの菌種に属する菌株の代表例とし
てアルカリゲネス フェカリスATCC8750、アル
カリゲネス ルーランディィATCC15749、アル
カリゲネス ラタスATCC29712、ATCC29
713:アルカリゲネス ユウトロフスH−16ATC
C17699等が挙げられる。これらのうち、アルカリ
ゲネス ラタスATCC29712、ATCC2971
3が生産性の面で特に好ましい。
Regarding the microorganisms used in the present invention, P
There is no particular limitation as long as it is an Alcaligenes genus capable of producing HB. For example, Alcaligenes faecalis (A
lcaligenes faecalic, Alcaligenes r
uhlandii), Alcaligenes ratus (Alc
aligenes ratus, Alcaligenes eutroph
s) etc., and representative examples of strains belonging to these strains are Alcaligenes faecalis ATCC 8750, Alcaligenes rulandi ATCC15749, Alcaligenes ratus ATCC 29712, ATCC29.
713: Alcaligenes Yutrofus H-16ATC
C17699 etc. are mentioned. Of these, Alcaligenes ratus ATCC29712, ATCC2971
3 is particularly preferable in terms of productivity.

【0012】アルカリゲネス属に属するこれらの微生物
の菌学的性質は、例えば、“BERGEY’S MAN
UAL OF DETERMINATIVE BACT
ERIOLOGY:Eighth Editionや、
アルカリゲネス ユウトロフスH−16の菌学的性質
は、例えば“J.Gen.Microobiol.,
15、185〜192(1979)に記載されている。
The mycological properties of these microorganisms belonging to the genus Alcaligenes are described, for example, in "BERGEY'S MAN".
UAL OF DETERMINATIVE BACT
ERILOGY: Eight Edition,
The mycological properties of Alcaligenes eutrophus H-16 are described, for example, in “J. Gen. Microbiol., 1
15 , 185-192 (1979).

【0013】本発明の培養法は、微生物を増殖させる通
常の培養法が適用される。例えば、前段培養(菌体の増
殖)と後段培養(窒素源の制限下における共重合体の生
成)とからなる二段回分培養、あるいは、菌体の増殖と
共重合体の生成を同時に行う一段回分培養が可能であ
る。更には、窒素源や炭素源を滴下しながら菌体の増殖
と共重合体の生成を行う連続培養も行うことができる。
As the culture method of the present invention, a usual culture method for growing a microorganism is applied. For example, a two-stage batch culture consisting of a pre-stage culture (proliferation of cells) and a post-stage culture (production of a copolymer under the restriction of a nitrogen source), or a single stage in which cell growth and copolymer production are performed simultaneously Batch culture is possible. Furthermore, continuous culture can be carried out in which a bacterial cell is grown and a copolymer is produced while dropping a nitrogen source or a carbon source.

【0014】使用する炭素源としては、ショ糖と、γ−
ブラロラクトン、4−ヒドロキシ酪酸、及びHO(CH
2 n OH(nは4〜12の偶数)で表わされる化合物
から選ばれた少なくとも1つとを併用する。このうちシ
ョ糖とγ−ブチロラクトンとを併用するのが最も好まし
い。上記炭素源の濃度は共重合体の生産性の面から総量
で3〜100g/lの範囲が好ましく、5〜20g/l
の範囲が特に好ましい。また、ショ糖と併用する上記γ
−ブチロラクトン等(以下γ−BL類と記す)の量比
は、4HB単位が効率よく導入されるためには、総炭素
源に対し、0.5〜6重量%が好ましく、特に好ましい
のは1〜3重量%である。γ−BL類の量が上記範囲よ
り小さい場合は、共重合体への4HB成分の導入率が少
なく、また上記範囲より大きい場合は共重合体自体の生
産量およびγ−BL類から4HB成分への転換効率が低
下する。
The carbon sources used are sucrose and γ-
Bularolactone, 4-hydroxybutyric acid, and HO (CH
2 ) Used in combination with at least one selected from compounds represented by n OH (n is an even number of 4 to 12). Of these, it is most preferable to use sucrose and γ-butyrolactone together. The concentration of the above carbon source is preferably in the range of 3 to 100 g / l in terms of the productivity of the copolymer, and 5 to 20 g / l.
Is particularly preferred. Also, the above γ used in combination with sucrose
-The amount ratio of butyrolactone and the like (hereinafter referred to as γ-BLs) is preferably 0.5 to 6% by weight, and particularly preferably 1 to 5% by weight based on the total carbon source in order to efficiently introduce 4HB units. ~ 3% by weight. When the amount of γ-BLs is less than the above range, the introduction rate of the 4HB component into the copolymer is low, and when it is more than the above range, the production amount of the copolymer itself and the γ-BLs to the 4HB component are changed. Conversion efficiency is reduced.

【0015】尚、本発明の目的にあう範囲内であれば、
公知の他の炭素源を併用することも可能である。かかる
他の炭素源としては、例えば、メタノール、エタノール
および酢酸等の合成炭素源、二酸化炭素等の無機炭素
源、酵母エキス、糖蜜、ペプトンおよび肉エキス等の天
然物、アラビノース、フルクトース、グルコース、マン
ノース等の糖類等が挙げられる。
Incidentally, within the scope of the object of the present invention,
It is also possible to use other known carbon sources in combination. Examples of such other carbon sources include synthetic carbon sources such as methanol, ethanol and acetic acid, inorganic carbon sources such as carbon dioxide, natural products such as yeast extract, molasses, peptone and meat extract, arabinose, fructose, glucose and mannose. And the like.

【0016】窒素源としては、例えば、アンモニア、ア
ンモニウム塩、硝酸塩等の無機窒素化合物および/また
は、例えば尿素、コーン・スティーブ・リカー、カゼイ
ン、ペプトン、酵母エキス、肉エキス等の窒素含有物が
あり、特に好ましいのは硫酸アンモニウムである。無機
成分としては、例えば、カルシウム塩、マグネシウム
塩、カリウム塩、ナトリウム塩、りん酸塩、マンガン
塩、亜鉛塩、鉄塩、銅塩、モリブデン塩、コバルト塩、
ニッケル塩、クロム塩、ほう素化合物およびよう素化合
物であり、好ましくは、リン酸二水素カリウム、リン酸
水素二ナトリウム、硫酸マグネシウムなどがあげられ
る。
Examples of the nitrogen source include inorganic nitrogen compounds such as ammonia, ammonium salts and nitrates and / or nitrogen-containing substances such as urea, corn steve liquor, casein, peptone, yeast extract and meat extract. Particularly preferred is ammonium sulfate. As the inorganic component, for example, calcium salt, magnesium salt, potassium salt, sodium salt, phosphate, manganese salt, zinc salt, iron salt, copper salt, molybdenum salt, cobalt salt,
Nickel salts, chromium salts, boron compounds and iodine compounds, preferably potassium dihydrogen phosphate, disodium hydrogen phosphate, magnesium sulfate and the like can be mentioned.

【0017】また、必要に応じて、ビタミン類なども使
用することができる。培養条件としては、温度は、たと
えば、20〜45℃程度、好ましくは30〜42℃程度
とされ、また、pHは、たとえば、6〜10程度、好ま
しくは6.5〜9.5程度とされる。このような条件で
好気的に培養する。これらの条件をはずして培養した場
合には、微生物の増殖は比較的悪くなるが、これらの条
件をはずして培養することを妨げない。
If necessary, vitamins and the like can also be used. As the culture conditions, the temperature is, for example, about 20 to 45 ° C., preferably about 30 to 42 ° C., and the pH is, for example, about 6 to 10 and preferably about 6.5 to 9.5. It It cultures aerobically under such conditions. When the culture is carried out under these conditions, the growth of microorganisms becomes relatively poor, but it does not prevent the culture under these conditions.

【0018】このように培養して得られた培養液から、
濾過および遠心分離などの通常の固液分離手段によって
菌体を分離回収し、この菌体を洗浄、乾燥して乾燥菌体
を得、この乾燥菌体から、常法により、たとえば、クロ
ロホルムのような有機溶剤で生成された共重合体を抽出
し、この抽出液に、たとえば、ヘキサンのような貧溶媒
を加えて、共重合体を沈澱させる。本発明の製造法によ
れば、共重合体中の3HB単位、4HB単位の割合は添
加炭素源γ−BL類の比率により任意に調節することが
できる。
From the culture solution obtained by culturing in this way,
The cells are separated and recovered by a usual solid-liquid separation means such as filtration and centrifugation, and the cells are washed and dried to obtain dried cells. From the dried cells, for example, chloroform is used. A copolymer produced with a different organic solvent is extracted, and a poor solvent such as hexane is added to the extract to precipitate the copolymer. According to the production method of the present invention, the ratio of 3HB units and 4HB units in the copolymer can be arbitrarily adjusted by the ratio of the added carbon source γ-BLs.

【0019】[0019]

【実施例】本発明を実施例によりさらに具体的に説明す
る。なお本発明はこれらの実施例に限定されるものでは
ない。 〈実施例1〜4および比較例1〜2〉アルカリゲネス
ラタス(ATCC29713)を使用して共重合体を製
造した。
EXAMPLES The present invention will be described more specifically by way of examples. The present invention is not limited to these examples. <Examples 1-4 and Comparative Examples 1-2> Alcaligenes
The copolymer was prepared using ratus (ATCC 29713).

【0020】菌体の培養 次の組成を有するコルベン中の培地100mlに前記の
微生物を植菌し、30℃で48時間振とう培養した。得
られた培養液から遠心分離により菌体を分離して菌体を
得た。
Cultivation of bacterial cells 100 ml of a medium in Kolben having the following composition was inoculated with the above-mentioned microorganism and shake-cultured at 30 ° C. for 48 hours. The cells were separated from the obtained culture solution by centrifugation to obtain the cells.

【0021】[0021]

【表1】 [Table 1]

【0022】*Trace−element solu
tion(1リットル中)の組成は、H3 BO3 0.
3g、CoCl2 ・6H2 O 0.2g、ZnSO4
7H 2 O 0.1g、MnCl2 ・4H2 O 30m
g、NaMoO4 ・2H2 O30mg、NiCl・6H
2 O 20mg及びCuSO4 ・5H2 O 10mgで
ある。 **炭素源として後記表−1に記載のショ糖およびγ−
ブチロラクトン又は4−ヒドロキシ酪酸を使用した。
(単位g/l培地) 前記菌体を蒸留水で洗浄し、引続きアセトンで洗浄し、
これを減圧乾燥(20℃、0.1mmHg)して乾燥菌
体を得た。
* Trace-element solu
composition (in 1 liter) is H3BO3 0.
3g, CoCl2・ 6H2O 0.2g, ZnSOFour
7H 2O 0.1g, MnCl2・ 4H2O 30m
g, NaMoOFour・ 2H2O30mg, NiCl / 6H
2O 20mg and CuSOFour・ 5H2O 10 mg
is there. ** Sucrose and γ-as described in Table 1 below as carbon sources
Butyrolactone or 4-hydroxybutyric acid was used.
(Unit: g / l medium) The cells were washed with distilled water and then with acetone,
This is dried under reduced pressure (20 ° C, 0.1 mmHg) and dried.
Got the body

【0023】共重合体の分離回収:このようにして得
られた乾燥菌体から熱クロロホルムで共重合体を抽出
し、この抽出液にヘキサンを加えて共重合体を沈澱さ
せ、この沈澱を濾取、乾燥して共重合体を得た。
Separation and recovery of the copolymer: The copolymer was extracted from the dried cells thus obtained with hot chloroform, hexane was added to the extract to precipitate the copolymer, and the precipitate was filtered. It was taken and dried to obtain a copolymer.

【0024】共重合体の特性 このようにして得られた共重合体の組成、その他をつぎ
のようにして測定し、その結果を表−1に示した。 組成:3HB単位、4HB単位のモル比をH−NMR
(270MHz)スペクトルより求めた。
Characteristics of Copolymer The composition of the copolymer thus obtained and other properties were measured as follows, and the results are shown in Table 1. Composition: 3HB unit, 4HB unit molar ratio H-NMR
It was determined from the (270 MHz) spectrum.

【0025】乾燥菌体重量:遠心分離により集菌したも
のを凍結乾燥した。 ポリエステル含率:乾燥菌体中のポリエステル含率(モ
ル%) 4HB転換率:使用したγ−BL類に対して4HBとし
て共重合体に導入されたγ−BL類の割合
Dry cell weight: The cells collected by centrifugation were freeze-dried. Polyester content: Polyester content in dry cells (mol%) 4HB conversion: Ratio of γ-BLs introduced into the copolymer as 4HB with respect to γ-BLs used.

【0026】[0026]

【表2】 [Table 2]

【0027】[0027]

【発明の効果】本発明によれば3HB単位と4HB単位
からなる共重合体を少量のγ−BL類の存在下、効率的
に得ることができる。本発明の方法で得られた共重合体
は、優れた種々の機械的特性および生体適合性あるいは
生分解性を有しているので、手術糸および骨折固定材料
などの医用材料の原料として好適であり、また、徐放性
システムへの利用などの多方面への応用が期待される。
According to the present invention, a copolymer comprising 3HB units and 4HB units can be efficiently obtained in the presence of a small amount of γ-BLs. Since the copolymer obtained by the method of the present invention has various excellent mechanical properties and biocompatibility or biodegradability, it is suitable as a raw material for medical materials such as surgical threads and fracture fixation materials. In addition, it is expected to be applied to various fields such as use in sustained release systems.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 3−ヒドロキシブチレート単位97〜8
0モル%および4−ヒドロキシブチレート単位3〜20
モル%からなるポリエステル共重合体を、アルカリゲネ
ス属菌の存在下に製造する方法において、炭素源として
ショ糖とγ−ブチロラクトン、4−ヒドロキシ酪酸及び
HO(CH2 n OH(nは4〜12の偶数)で表わさ
れる化合物から選ばれた少なくとも1つとを併用するこ
とを特徴とするポリエステル共重合体の製造方法。
1. 3-hydroxybutyrate units 97-8
0 mol% and 4-hydroxybutyrate units 3-20
In the method for producing a polyester copolymer comprising mol% in the presence of a bacterium of the genus Alcaligenes, sucrose and γ-butyrolactone as a carbon source, 4-hydroxybutyric acid and HO (CH 2 ) n OH (n is 4 to 12). And at least one selected from the compounds represented by the formula (1), the method for producing a polyester copolymer.
【請求項2】 アルカリゲネス属菌がアルカリゲネス
ラタスであることを特徴とする、請求項1記載のポリエ
ステル共重合体の製造方法。
2. The Alcaligenes genus is Alcaligenes
The method for producing a polyester copolymer according to claim 1, which is Latus.
【請求項3】 総炭素源中γ−ブチロラクトンが0.5
〜6重量%であることを特徴とする請求項1または2記
載のポリエステル共重合体の製造方法。
3. The amount of γ-butyrolactone in the total carbon source is 0.5.
The method for producing a polyester copolymer according to claim 1 or 2, wherein the content is from 6 to 6% by weight.
【請求項4】 総炭素源の濃度を3〜100g/リット
ルとすることを特徴とする請求項1ないし3のいずれか
に記載のポリエステル共重合体の製造方法。
4. The process for producing a polyester copolymer according to claim 1, wherein the concentration of the total carbon source is 3 to 100 g / liter.
JP4315246A 1992-11-25 1992-11-25 Production of copolyester Pending JPH06181784A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4315246A JPH06181784A (en) 1992-11-25 1992-11-25 Production of copolyester

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4315246A JPH06181784A (en) 1992-11-25 1992-11-25 Production of copolyester

Publications (1)

Publication Number Publication Date
JPH06181784A true JPH06181784A (en) 1994-07-05

Family

ID=18063132

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4315246A Pending JPH06181784A (en) 1992-11-25 1992-11-25 Production of copolyester

Country Status (1)

Country Link
JP (1) JPH06181784A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5821299A (en) * 1996-02-16 1998-10-13 The Proctor & Gamble Company Solvent extraction of polyhydroxy-alkanoates from biomass facilitated by the use of marginal nonsolvent
US5942597A (en) * 1995-08-21 1999-08-24 The Procter & Gamble Company Solvent extraction of polyhydroxyalkanoates from biomass
EP1113033A3 (en) * 1999-12-27 2002-10-16 Canon Kabushiki Kaisha Polyhydroxyalkanoate, method for production thereof and microorganisms for use in the same
WO2019044836A1 (en) 2017-08-29 2019-03-07 三菱瓦斯化学株式会社 Polyester including 4-hydroxybutyrate units

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5942597A (en) * 1995-08-21 1999-08-24 The Procter & Gamble Company Solvent extraction of polyhydroxyalkanoates from biomass
US5821299A (en) * 1996-02-16 1998-10-13 The Proctor & Gamble Company Solvent extraction of polyhydroxy-alkanoates from biomass facilitated by the use of marginal nonsolvent
EP1113033A3 (en) * 1999-12-27 2002-10-16 Canon Kabushiki Kaisha Polyhydroxyalkanoate, method for production thereof and microorganisms for use in the same
WO2019044836A1 (en) 2017-08-29 2019-03-07 三菱瓦斯化学株式会社 Polyester including 4-hydroxybutyrate units
KR20200046051A (en) 2017-08-29 2020-05-06 미쯔비시 가스 케미칼 컴파니, 인코포레이티드 Polyester comprising 4-hydroxybutyrate units
US11466120B2 (en) 2017-08-29 2022-10-11 Mitsubishi Gas Chemical Company, Inc. Polyester containing 4-hydroxybutyrate unit
KR20240134063A (en) 2017-08-29 2024-09-05 미쯔비시 가스 케미칼 컴파니, 인코포레이티드 Polyester including 4-hydroxybutyrate units
KR20240134066A (en) 2017-08-29 2024-09-05 미쯔비시 가스 케미칼 컴파니, 인코포레이티드 Polyester including 4-hydroxybutyrate units

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