JPH0564592A - Production of bio-polyester - Google Patents

Production of bio-polyester

Info

Publication number
JPH0564592A
JPH0564592A JP3254199A JP25419991A JPH0564592A JP H0564592 A JPH0564592 A JP H0564592A JP 3254199 A JP3254199 A JP 3254199A JP 25419991 A JP25419991 A JP 25419991A JP H0564592 A JPH0564592 A JP H0564592A
Authority
JP
Japan
Prior art keywords
polyester
hydroxybutyrate
chain fatty
carbon source
long
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
JP3254199A
Other languages
Japanese (ja)
Other versions
JP3114148B2 (en
Inventor
Minoru Akiyama
稔 秋山
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.)
Asahi Chemical Industry Co Ltd
Original Assignee
Asahi Chemical Industry 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 Asahi Chemical Industry Co Ltd filed Critical Asahi Chemical Industry Co Ltd
Priority to JP03254199A priority Critical patent/JP3114148B2/en
Priority to US07/903,021 priority patent/US5346817A/en
Priority to DE69221957T priority patent/DE69221957T2/en
Priority to EP92110632A priority patent/EP0520405B1/en
Publication of JPH0564592A publication Critical patent/JPH0564592A/en
Application granted granted Critical
Publication of JP3114148B2 publication Critical patent/JP3114148B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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

Abstract

PURPOSE:To obtain the subject polymer useful for bio-decomposable medical material, etc., in high yield by culturing a microbial strain belonging to genus Alcaligenes and capable of producing a polyester containing 3-hydroxybutyrate in a medium containing a long-chain fatty acid and collecting the product accumulated in the microbial cell. CONSTITUTION:A microbial strain belonging to genus Alcaligenes and capable of producing a polyester containing 3-hydroxybutyrate [e.g. Alcaligenes lipolytica AK201 (FERM P-12198)] is cultured in a liquid medium containing at least one kind of compound selected from long-chain fatty acid (e.g. undecanoic acid) and its derivative at 30 deg.C for 48hr under shaking at a rate of 130 strokes per minute. The culture liquid is subjected to centrifugal separation, washed with water and the collected microbial cells are freeze-dried. The freeze-dried cells are treated with hot chloroform to extract the polyester accumulated in the cell, the extracted liquid is concentrated, added with hexane and the precipitate is filtered and dried to obtain the objective bio-polyester composed of a copolymer of 3-hydroxybutyrate and 3-hydroxyvaleric acid, etc.

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(3HB)をモノマー単位として含有する脂肪族ポ
リエステルを、微生物の生合成機能を利用して製造する
方法に関するものである。ポリ(3−ヒドロキシブチレ
ート)(PHB)に代表される一群の微生物産生ポリエ
ステルは、石油由来の合成高分子とは異なり、微生物
や、ヒトを含めた高等動物の体内で容易に分解される性
質(生分解性)を有している。近年夥しい量の合成高分
子がプラスチック等として多方面で利用されると共に、
使用済みのプラスチックが腐らない嵩高い廃棄物として
蓄積し、自然環境の汚染を起こすことが深刻な問題とな
っている。該ポリエステルは生分解されることにより自
然の物質循環に取り込まれるので、環境保全を可能とす
るプラスチックとして利用することができる。また、医
療分野においては、回収不用のインプラント材料、薬物
担体としての利用が可能である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing an aliphatic polyester containing 3-hydroxybutyrate (3HB) as a monomer unit by utilizing the biosynthetic function of microorganisms. A group of microbial-produced polyesters represented by poly (3-hydroxybutyrate) (PHB), unlike synthetic polymers derived from petroleum, have the property of being easily decomposed in the body of microorganisms and higher animals including humans. It has (biodegradability). In recent years, enormous amounts of synthetic polymers have been used in various fields such as plastics,
It has become a serious problem that used plastic accumulates as bulky waste that does not rot and pollutes the natural environment. Since the polyester is biodegraded and taken into the natural material cycle, it can be used as a plastic that enables environmental protection. Further, in the medical field, it can be used as an implant material and a drug carrier that are not required to be recovered.

【0002】[0002]

【従来の技術】従来、多種の細菌がPHBを菌体内に生
成し、粒子として蓄積することが報告されてきた〔H.Br
andl et al,Adv.Biochem. Eng./Biotechnol., 41,77-93
(1990)〕。特に、アルカリゲネス・ユートロファス(Al
caligenes eutrophus)〔特開昭57−150393〕、
ノカルディア属(Nocardia) 、コリネバクテリウム属(C
orynebacterium) 、ロドコッカス属(Rhodococcus) のあ
る種の菌〔欧州特許90304267.9, April, 1990 〕、ロド
スピリルム・ルブルム(Rhodospirillum rubrum)〔H.Br
andl et al,Int.J.Biol.Macromol.,11,49-55(1989)〕等
は、一定の炭素源から3HBと3−ヒドロキシ吉草酸
(3HV)の共重合体または3HB、3HVを共に含有
成分とする共重合体を生成することが報告されている。
3HBと3HVの共重合体(P(HB/HV))は、硬
くて脆い欠点を有するPHBの物性を改良した熱可塑性
樹脂として工業的利用が進められている。
2. Description of the Related Art Conventionally, it has been reported that various kinds of bacteria produce PHB in cells and accumulate it as particles [H.Br.
andl et al, Adv.Biochem. Eng./Biotechnol., 41,77-93
(1990)]. Especially, Alcaligenes eutrophus (Al
caligenes eutrophus) [JP-A-57-150393],
Nocardia, Corynebacterium (C
orynebacterium), certain fungi of the genus Rhodococcus (European patent 90304267.9, April, 1990), Rhodospirillum rubrum (H.Br
andl et al, Int. J. Biol. Macromol., 11, 49-55 (1989)] et al. It has been reported to produce a copolymer as a component.
A copolymer of 3HB and 3HV (P (HB / HV)) is industrially utilized as a thermoplastic resin having improved physical properties of PHB, which has the drawback of being hard and brittle.

【0003】[0003]

【発明が解決しようとする課題】このような3HB単位
含有ポリエステルを微生物によって工業的に製造する場
合、原料、特に主原料である炭素源の種類、使用炭素源
に基づく収率、該ポリエステルの乾燥菌体含有率等が重
要な成立要件となる。炭素源の種類に関しては、メタノ
ール(特開昭56−117793)、果糖(特公平2−
20238)、ぶどう糖(特開昭57−15039
3)、蔗糖(特公昭63−32438)等の利用が報告
されている。しかし、生成ポリエステルの分子量が低
い、大量の入手に難がある、使用炭素源に基づく収率が
不十分である、単独重合体PHBにのみ適用が限定され
ている、といった欠点を各々有していた。
When such a 3HB unit-containing polyester is industrially produced by a microorganism, the raw materials, particularly the type of the carbon source as the main raw material, the yield based on the carbon source used, and the drying of the polyester are used. The cell content rate is an important requirement. Regarding the type of carbon source, methanol (JP-A-56-117793) and fructose (Japanese Patent Publication No.
20238), glucose (JP-A-57-15039).
3), sucrose (Japanese Patent Publication No. 63-32438) and the like have been reported to be used. However, they each have drawbacks such as low molecular weight of produced polyester, difficulty in obtaining large amount, insufficient yield based on carbon source used, and limited application to homopolymer PHB. It was

【0004】[0004]

【課題を解決するための手段】本発明者らは、前記課題
を解決するために、各種の炭素源で3HB含有ポリエス
テル生産菌の培養を実施した結果、従来炭素源としての
利用が知られていない長鎖脂肪酸ないしその誘導体を必
須炭素源としてアルカリゲネス属の細菌を培養すること
により、PHBまたはP(HB/HV)を高い収率、高
い乾燥菌体含有率にて生成することを見出した。
In order to solve the above-mentioned problems, the present inventors have cultivated 3HB-containing polyester-producing bacteria with various carbon sources, and as a result, have conventionally been known to be used as carbon sources. It was found that PHB or P (HB / HV) is produced at a high yield and a high dry cell content rate by culturing a bacterium of the genus Alcaligenes using a long-chain fatty acid or its derivative as an essential carbon source.

【0005】すなわち、本発明は、長鎖脂肪酸とその誘
導体からなる化合物群の少なくとも1種を必須炭素源と
する液体培地を用いて、アルカリゲネス属に属する3H
B含有ポリエステル生産菌を培養し、菌体内に3HB含
有ポリエステルを蓄積させ、これを採取する該ポリエス
テルの製造法を提供することにある。
That is, the present invention uses 3H belonging to the genus Alcaligenes using a liquid medium containing at least one compound of a long-chain fatty acid and its derivative as an essential carbon source.
The purpose of the present invention is to provide a method for producing a polyester which comprises culturing a B-containing polyester-producing bacterium, accumulating 3HB-containing polyester in the microbial cells, and collecting the polyester.

【0006】使用するアルカリゲネス属(Alcaligenes
)の細菌としては、A.faecalis(アルカリゲネス・フ
ェカリス)、A.denitrificans (アルカリゲネス・デニ
トリフィカンス)、A. eutrophus (アルカリゲネス・
ユートロファス)、A.paradoxus (アルカリゲネス・パ
ラドキサス)、A.aquamarinus (アルカリゲネス・アク
アマリナス)等の公知の菌種も使用可能であるが、本発
明者が分離した菌 A.lipolytica(アルカリゲネス・リポ
リティカ)AK201(微工研菌寄No. 12198)
は、この目的のために特に優れた性質を有している。上
記の公知の菌に関しては、バージーズ・マニュアル〔Be
rgey's Manual of Systematic Bacteriology,Vol.1(198
4)〕にその菌学的性質、主要な収集株が示されている。
Alcaligenes used
), A.faecalis (Alcaligenes faecalis), A.denitrificans (Alcaligenes denitrificans), A. eutrophus (Alcaligenes
Known bacterial species such as Eutrophus), A. paradoxus (Alcaligenes paradoxus), and A. aquamarinus (Alcaligenes aquamarinus) can also be used, but the bacterium A. lipolytica (Alcaligenes lipolytica) AK201 isolated by the present inventor (Ministry of Microbiological Research No. 12198)
Have particularly good properties for this purpose. For the above-mentioned known bacteria, see the Berseys Manual [Be
rgey's Manual of Systematic Bacteriology, Vol.1 (198
4)] shows its mycological properties and major collected strains.

【0007】A.lipolytica AK201の菌学的性質
は、以下のとおりである。 (a)形態学的性状 1)細胞の形及び大きさ:桿菌、0.4〜0.7×0.7
〜1.5μm 2)細胞の多形性:なし 3)運動性:あり 4)胞子:なし 5)グラム染色性:陰性
The mycological properties of A. lipolytica AK201 are as follows. (A) Morphological properties 1) Shape and size of cells: bacillus, 0.4 to 0.7 × 0.7
~ 1.5μm 2) Cell polymorphism: None 3) Motility: Yes 4) Spores: None 5) Gram stainability: Negative

【0008】(b)培養性状 1)肉汁寒天平板培養:白色、生育良好 2)肉汁寒天斜面培養:白色、生育良好 3)肉汁液体培養:クリーム色、生育良好(B) Culture characteristics 1) Meat broth agar plate culture: white, good growth 2) Meat broth agar slope culture: white, good growth 3) Meat broth liquid culture: cream color, good growth

【0009】(c)生理学的性質 1)硝酸塩の還元:陰性 2)脱窒反応:陰性 3)インドールの生成:陰性 4)クエン酸の利用:陽性 5)無機窒素源の利用:陽性 6)色素の生成:陰性 7)ウレアーゼ:陽性 8)オキシダーゼ:陽性 9)カタラーゼ:陽性 10)生育温度およびpH:20〜37℃、pH6〜8 11)酸素に対する態度:好気性 12)O−Fテスト:陰性(アルカリ性反応を示した) 13)グルコースからの酸生成:陰性 14)ゼラチンの分解:陰性 15)糖の資化性:D−グルコース、L−アラビノース、
D−マンノース、D−マンニトール、麦芽糖に対し全て
陰性
(C) Physiological properties 1) Reduction of nitrate: Negative 2) Denitrification reaction: Negative 3) Formation of indole: Negative 4) Utilization of citric acid: Positive 5) Utilization of inorganic nitrogen source: Positive 6) Dye Generation: Negative 7) Urease: Positive 8) Oxidase: Positive 9) Catalase: Positive 10) Growth temperature and pH: 20-37 ° C, pH 6-8 11) Attitude toward oxygen: Aerobic 12) OF test: Negative 13) Acid production from glucose: negative 14) Gelatin decomposition: negative 15) Sugar assimilation: D-glucose, L-arabinose,
All negative for D-mannose, D-mannitol and maltose

【0010】本菌は、以上のとおり好気性、グラム陰
性、非発酵性、運動性桿菌であり、オキシダーゼ陽性、
O−Fテスト陰性等の他の菌学的性質を勘案してアルカ
リゲネス属に属すると同定されたものである。なお、菌
学的性質の試験は駒形和男〔長谷川武治(編)、微生物
の分類と同定(1990);好気性細菌〕、ザ・プロカ
リオーツ第1巻〔The Procaryotes ;A Handbook on Ha
bitats,Isolation and Identification of Bacteria,(E
d.) M.P.Starr et al (1981 )〕に記載の方法にて行っ
た。また、菌の同定にはバージーズ・マニュアル〔 Ber
gey's ManualofSystematic Bacteriology,Vol.1(198
4)〕にしたがった。
As mentioned above, the bacterium is an aerobic, gram-negative, non-fermenting, motile bacillus, oxidase-positive,
It was identified as belonging to the genus Alcaligenes in consideration of other mycological properties such as OF test negative. The examination of the mycological properties was conducted by Kazuo Komagata [Takeharu Hasegawa (ed.), Classification and identification of microorganisms (1990); Aerobic bacteria], The Procaryotes Volume 1 [The Procaryotes; A Handbook on Ha.
bitats, Isolation and Identification of Bacteria, (E
d.) MPStarr et al (1981)]. In addition, for identification of bacteria, the Berseys Manual [Ber
gey's ManualofSystematic Bacteriology, Vol.1 (198
4)].

【0011】本菌の菌学的性質、資化性をアルカリゲネ
ス属の既存菌種に関する性質、資化性との比較を表1〜
3に示した。
Comparison of the mycological properties and assimilation properties of this bacterium with those of existing strains of the genus Alcaligenes is shown in Tables 1 to 1.
Shown in 3.

【0012】[0012]

【表1】 [Table 1]

【0013】[0013]

【表2】 [Table 2]

【0014】[0014]

【表3】 [Table 3]

【0015】以上の如き照合の結果、本菌はアルカリゲ
ネス属に属する新種の菌と判定した。また、生育および
ポリエステル合成に対し、炭素源として油脂および長鎖
脂肪酸を良く資化することを特徴とするのでA.lipolyti
caと命名した。
As a result of the above-mentioned collation, this bacterium was determined to be a new strain belonging to the genus Alcaligenes. In addition, it is characterized by well assimilating fats and oils and long-chain fatty acids as carbon sources for growth and polyester synthesis.
I named it ca.

【0016】本発明に用いる長鎖脂肪酸とは、炭素数1
1〜22までの直鎖脂肪酸を意味する。好ましくは、炭
素数11〜18までのものである。また、長鎖脂肪酸の
誘導体には、Na+ 、K+ 、Ca2+、Mg2+等の金属塩
とアンモニウム塩、炭素数1〜3までのアルキルアルコ
ール、アルキレングリコール、グリセロールのモノまた
はポリエステル、およびアミド(−CONH2 )が含ま
れる。特に、長鎖脂肪酸のトリグリセライドあるいはそ
の混合物である油脂が、該誘導体に含まれることは言う
までもない。
The long-chain fatty acid used in the present invention has 1 carbon atom.
1 to 22 straight chain fatty acids are meant. Preferably, it has 11 to 18 carbon atoms. Derivatives of long chain fatty acids include metal salts and ammonium salts of Na + , K + , Ca 2+ , Mg 2+, etc., alkyl alcohols having 1 to 3 carbon atoms, alkylene glycols, mono- or polyesters of glycerol, and it includes amides (-CONH 2) is. It goes without saying that fats and oils, which are triglycerides of long-chain fatty acids or mixtures thereof, are included in the derivatives.

【0017】また、本発明に記述する“必須炭素源”と
は、3HB含有ポリエステルの蓄積、または該ポリエス
テルの蓄積のみでなく菌体そのものの増殖をも誘起する
炭素源であって、しかも、本発明の該ポリエステル製造
に必ず使用されるものを意味する。したがって、単に菌
体を増殖させるために増殖に有効な他の炭素源のみを使
用することを排除するものではない。
The "essential carbon source" described in the present invention is a carbon source that induces not only the accumulation of 3HB-containing polyester, or the accumulation of the polyester but also the growth of bacterial cells itself. Means that are necessarily used in the production of the polyester of the invention. Therefore, it is not excluded that only other carbon sources effective for growth are used solely for growing the bacterial cells.

【0018】本発明で製造される3HB含有ポリエステ
ルは、3HBの単独重合体(PHB)または3HBと3
HVとの共重合体(P(HB/HV))である。いずれ
のポリエステルが生成するかは、使用する炭素源の分子
構造に依存することが判明した。例えば、炭素源として
偶数炭素数の長鎖脂肪酸とその誘導体からなる1群中の
化合物のみで該菌株を培養し、菌体の増殖とポリエステ
ルの蓄積を誘起した場合は、PHBまたはP(HB/H
V)が生成する。一方、炭素源として奇数炭素数の長鎖
脂肪酸とその誘導体からなる1群中の化合物のみで該菌
体を同様に培養した場合、P(HB/HV)を生成す
る。また、偶数炭素数、奇数炭素数の上記各群中の化合
物を併用した場合もP(HB/HV)を生成する。生成
ポリエステルの種類は、上記のように、使用する必須炭
素源に依存するばかりでなく、ポリエステル生成に利用
される付加的な炭素源にも依存する。すなわち、偶数炭
素数の上記の1群中の化合物を必須炭素源とし、付加的
な炭素源として、前記化1式で示される化合物群の少な
くとも1種を併用した場合、P(HB/HV)を生成す
る。
The 3HB-containing polyester produced by the present invention is a 3HB homopolymer (PHB) or 3HB and 3HB.
It is a copolymer with HV (P (HB / HV)). It has been found that which polyester is produced depends on the molecular structure of the carbon source used. For example, when the strain is cultured only with a compound in a group consisting of a long-chain fatty acid having an even number of carbon atoms and its derivative as a carbon source to induce the growth of bacterial cells and the accumulation of polyester, PHB or P (HB / H
V) is generated. On the other hand, P (HB / HV) is produced when the bacterial cells are similarly cultured with only one group of compounds consisting of a long-chain fatty acid having an odd number of carbon atoms and its derivative as a carbon source. In addition, P (HB / HV) is also produced when the compounds in each of the above groups having an even carbon number and an odd carbon number are used in combination. The type of polyester produced depends not only on the essential carbon source used, as described above, but also on the additional carbon source utilized for polyester production. That is, when the compound in the above-mentioned group 1 having an even carbon number is used as an essential carbon source and at least one kind of the compound group represented by the above chemical formula 1 is used in combination as an additional carbon source, P (HB / HV) To generate.

【0019】ポリエステル製造のための菌の培養は、液
体培地中にて行う。培養温度は20〜40℃、好ましく
は24〜33℃である。培養の初発pHは6.0〜8.
0、好ましくは6.5〜7.5である。液体培地には、
合成、半合成、天然の培地を含め各種のものを用いるこ
とができる。無機培地を用いる場合には、そこに炭素源
の1種または複数種を加えて培養する。
Cultivation of the bacterium for producing polyester is carried out in a liquid medium. The culture temperature is 20-40 ° C, preferably 24-33 ° C. The initial pH of the culture is 6.0-8.
It is 0, preferably 6.5 to 7.5. The liquid medium contains
Various materials can be used, including synthetic, semi-synthetic and natural media. When an inorganic medium is used, one or more carbon sources are added thereto and the culture is performed.

【0020】菌体の増殖とポリエステルの蓄積の各進行
時期の前後関係から、操作上2種の培養方式に大別され
るが、本発明においては、両方の培養方式を目的に応じ
て使い分けることができる。そのうち、1段培養方式で
は、長鎖脂肪酸とその誘導体からなる化合物群中の少な
くとも1種を炭素源に用いて培養を行い、菌体増殖とポ
リエステルの蓄積を生起させる。この際、菌体の増殖を
促進するか、かつ(または)生成ポリエステルの特性を
制御するために付加的な炭素源を用いてもよい。もう一
方の2段培養方式では、1段目(前段)で専らまたは主
として菌体の増殖を生起させ、回収した菌体を2段目
(後段)の培地に投入して再び培養するが、後段では専
らまたは主としてポリエステルの蓄積を生起させる。し
たがって、2段培養で用いられる炭素源は、前段におい
ては菌体増殖に有利な炭素源を用い、後段においては長
鎖脂肪酸とその誘導体からなる化合物群中の少なくとも
1種を単独で、または付加的な炭素源と共に用いる。2
段培養の後段では、菌体増殖を抑制し、ポリエステル生
成を促進するために、必須栄養源の少なくとも1種、例
えば、窒素源や燐源を減量または全く除いて培養するの
が有利である。
[0020] Operationally, there are roughly two types of culture methods depending on the context of the respective growth stages of bacterial cell growth and polyester accumulation. In the present invention, both culture methods should be used according to the purpose. You can Among them, in the one-stage culture method, at least one selected from the group of compounds consisting of long-chain fatty acids and their derivatives is used as a carbon source for culturing to cause microbial cell growth and polyester accumulation. At this time, an additional carbon source may be used to promote the growth of bacterial cells and / or control the properties of the produced polyester. In the other two-stage culturing method, the first stage (previous stage) causes the cells to grow exclusively or mainly, and the recovered bacterial cells are added to the second stage (second stage) medium and cultivated again. Causes the accumulation of polyester exclusively or predominantly. Therefore, the carbon source used in the two-stage culture is a carbon source advantageous for bacterial growth in the former stage, and in the latter stage, at least one selected from the group consisting of long-chain fatty acids and their derivatives alone or added. Used with a typical carbon source. Two
In the latter stage of the step culture, it is advantageous to culture at least one of the essential nutrient sources, for example, nitrogen source and phosphorus source, in a reduced amount or completely removed in order to suppress bacterial growth and promote polyester production.

【0021】菌体の増殖やポリエステルの蓄積に有効な
付加的な炭素源には、各種の化合物や天然物由来にもの
が利用できる。そのような例としては、炭素数2〜10
までの直鎖脂肪酸;クエン酸、グルコン酸、コハク酸、
グルタール酸、アジピン酸、スベリン酸、アゼライン
酸、乳酸等の有機酸;メタノール、エタノール、グリセ
ロール等のアルコール;グルコース、フルクトース、蔗
糖等の糖類;n−オクタン、n−ノナン等の直鎖脂肪族
炭化水素等が挙げられる。既述の化1式の化合物も、付
加的な炭素源に含まれることは言うまでもない。また、
各種のアミノ酸、ポリペプトン、肉エキス、カザミノ
酸、酵母エキス、糖蜜等の含窒素有機栄養源は、2段培
養の前段における炭素源として適当である。
Various compounds and those derived from natural products can be used as additional carbon sources effective for the growth of bacterial cells and the accumulation of polyester. As such an example, carbon number 2-10
Straight chain fatty acids up to; citric acid, gluconic acid, succinic acid,
Organic acids such as glutaric acid, adipic acid, suberic acid, azelaic acid and lactic acid; alcohols such as methanol, ethanol and glycerol; sugars such as glucose, fructose and sucrose; straight-chain aliphatic carbonization such as n-octane and n-nonane Examples thereof include hydrogen. It goes without saying that the compound of the above formula 1 is also included in the additional carbon source. Also,
Nitrogen-containing organic nutrient sources such as various amino acids, polypeptone, meat extract, casamino acid, yeast extract and molasses are suitable as carbon sources in the pre-stage of the two-stage culture.

【0022】培地中の窒素源としては、無機アンモニウ
ム塩、例えば、燐酸アンモニウム、硫酸アンモニウム、
塩酸アンモニウム等、また、前記したアミノ酸類、含窒
素有機栄養源、および有機酸アンモニウム、有機酸アミ
ドが用いられる。無機イオンとしては、ナトリウム、カ
リウム、マグネシウム、カルシウム、塩素、硫酸、燐酸
の他、微量の鉄、マンガン、亜鉛、銅、コバルト等が全
て、または一部と組み合わせて用いられる。
As the nitrogen source in the medium, inorganic ammonium salts such as ammonium phosphate, ammonium sulfate,
Ammonium chloride and the like, the above-mentioned amino acids, nitrogen-containing organic nutrient sources, and organic acid ammonium and organic acid amide are used. As the inorganic ions, in addition to sodium, potassium, magnesium, calcium, chlorine, sulfuric acid, phosphoric acid, trace amounts of iron, manganese, zinc, copper, cobalt, etc. are used in whole or in part.

【0023】培養終了後は、遠心分離、濾過などにより
菌体を集める。1段培養では、この後、そのままポリエ
ステル分離のための菌体処理をする。例えば、集めた菌
体を蒸留水で洗浄後、凍結乾燥によって乾燥菌体を得
る。次いで、該菌体からポリエステルをクロロホルム等
の良溶媒で加熱下に抽出し、濃縮後、メタノール、ヘキ
サンなどの貧溶媒で再沈澱することによりポリエステル
を得る。2段培養の場合は、集めた菌体を後段の培地中
に投入し、再び培養を行う。後段培養終了後の集菌、菌
体処理、ポリエステル分離は、既述の方法にしたがって
行われる。
After completion of the culture, the cells are collected by centrifugation, filtration or the like. In the one-stage culture, after this, the bacterial cell treatment for polyester separation is performed as it is. For example, the collected bacterial cells are washed with distilled water and then freeze-dried to obtain dried bacterial cells. Next, the polyester is extracted from the bacterial cells with a good solvent such as chloroform under heating, concentrated, and then reprecipitated with a poor solvent such as methanol or hexane to obtain the polyester. In the case of two-stage culture, the collected bacterial cells are put into the latter-stage medium and the culture is performed again. After the completion of the second-stage culture, the bacteria collection, bacterial cell treatment, and polyester separation are performed according to the method described above.

【0024】[0024]

【実施例】以下に、アルカリゲネス・リポリティカ A
K201を用いた3HB含有ポリエステルの製造を実施
例をもって説明する。
[Examples] The following are Alcaligenes repolitica A
The production of 3HB-containing polyester using K201 will be described with examples.

【0025】実施例1〜4 アルカリゲネス・リポリティカ AK 201を表4に
示す組成の無機培地100mlに炭素源として各々ウンデ
カン酸(実施例1)、ペンタデカン酸(実施例2)、ス
テアリン酸ナトリウム(実施例3)、菜種油(実施例
4)を3g/lの割合で加えた液体培地を含む500ml
容積の坂口フラスコに無菌的に植菌後、30℃、48時
間、毎分130ストロークで振盪培養した。
Examples 1 to 4 Alcaligenes lipolytica AK 201 was added to 100 ml of an inorganic medium having the composition shown in Table 4 as a carbon source, undecanoic acid (Example 1), pentadecanoic acid (Example 2), and sodium stearate (Examples). 3), 500 ml containing a liquid medium to which rapeseed oil (Example 4) was added at a rate of 3 g / l
After aseptically inoculating into a Sakaguchi flask having a volume, the culture was carried out at 30 ° C. for 48 hours with shaking at 130 strokes per minute.

【0026】[0026]

【表4】 ただし、微量元素溶液は1M塩酸1lに次の各無機塩を
溶解したものである: FeSO4 ・7H2 O(2.78g)、MnCl2 ・4
2 O(1.98g)、CoSO4 ・7H2 O(2.8
1g)、CaCl2 ・2H2 O(1.67g)、CuC
2 ・2H2 O(0.17g)、ZnSO4 ・7H2
(0.29g)。
[Table 4] However, the trace element solution is obtained by dissolving the following inorganic salts in 1 liter of 1M hydrochloric acid: FeSO 4 .7H 2 O (2.78 g), MnCl 2 .4
H 2 O (1.98 g), CoSO 4 · 7H 2 O (2.8
1g), CaCl 2 · 2H 2 O (1.67g), CuC
l 2 · 2H 2 O (0.17g ), ZnSO 4 · 7H 2 O
(0.29 g).

【0027】培養終了後、培養液を遠心分離(8000
rpm,15分)し、水洗を経て集菌した。菌体を凍結
乾燥して乾燥菌体を得た。菌体中に蓄積したポリエステ
ルは、乾燥菌体から熱クロロホルムで抽出後、溶液を濃
縮し、ヘキサンを加えて沈澱させた。沈澱を濾過、乾燥
してポリエステルを得た。
After the culture was completed, the culture solution was centrifuged (8000).
(rpm, 15 minutes) and washed with water to collect the bacteria. The cells were freeze-dried to obtain dried cells. The polyester accumulated in the bacterial cells was extracted from the dried bacterial cells with hot chloroform, the solution was concentrated, and hexane was added to cause precipitation. The precipitate was filtered and dried to obtain polyester.

【0028】ポリエステルの分析には、組成決定のため
にガスクロマトグラフィー、融点、融解熱、ガラス転移
温度の測定に示差熱分析、分子量、分子量分布の決定に
ゲル濾過クロマトグラフィーを利用した。なお、ガスク
ロマトグラフィーには、乾燥菌体をメタノリシスして菌
体内ポリエステルをモノマーのメチルエステルとしたも
のを試料に用いた〔H.Brandl et al,Int.J.Biol.Macrom
ol.,11,49-55(1989)〕。また、ポリエステルの分析は、
以下の実施例においても同様にして行った。
For the analysis of polyester, gas chromatography was used to determine the composition, differential thermal analysis was used to measure the melting point, heat of fusion, and glass transition temperature, and gel filtration chromatography was used to determine the molecular weight and molecular weight distribution. In the gas chromatography, dried cells were subjected to methanolysis and intracellular polyester was used as a monomer methyl ester [H. Brandl et al, Int. J. Biol. Macrom].
ol., 11, 49-55 (1989)]. In addition, the analysis of polyester is
The same was done in the following examples.

【0029】上記実施例1〜4のポリエステル生合成の
結果を表5に示す。
The results of the polyester biosynthesis of Examples 1 to 4 above are shown in Table 5.

【表5】 [Table 5]

【0030】実施例5〜7 ラード(豚油)(実施例5)、オリーブ油(実施例
6)、ラウリン酸エチル(実施例7)を唯一の炭素源と
して、実施例1〜4と同様に培養を行った後、生成ポリ
エステルを分析した。
Examples 5 to 7 Lard (pig oil) (Example 5), olive oil (Example 6), and ethyl laurate (Example 7) were used as the sole carbon sources and cultured in the same manner as in Examples 1 to 4. After carrying out, the resulting polyester was analyzed.

【0031】実施例5〜7のポリエステル生合成の結果
を表6に示す。
The results of the polyester biosynthesis of Examples 5-7 are shown in Table 6.

【表6】 [Table 6]

【0032】実施例8 必須炭素源として菜種油2g/l、付加的炭素源として
プロピオン酸ナトリウム1g/lを併用する以外は、実
施例1〜4と同様の条件で72時間培養した後、生成ポ
リエステルを分析した。その結果、乾燥菌体重量は1.
9g/l、ポリエステル含有率22%で、該ポリエステ
ルの組成は3HB94%、3HV6%であった。また、
融点は153℃であった。
Example 8 A polyester produced after culturing for 72 hours under the same conditions as in Examples 1 to 4 except that 2 g / l of rapeseed oil was used as an essential carbon source and 1 g / l of sodium propionate was used as an additional carbon source. Was analyzed. As a result, the dry cell weight was 1.
The composition of the polyester was 3HB94% and 3HV6% with 9 g / l and a polyester content of 22%. Also,
The melting point was 153 ° C.

【0033】実施例9 ポリペプトン10g、肉エキス5g、酵母エキス10
g、(NH4 2 SO4 5gを水1lに溶解した培地の
100mlを含む坂口フラスコに該菌株を無菌的に植菌
後、30℃、24時間振盪培養した。培養終了後、培養
液を遠心分離(8000rpm,10分)して菌体を集
め、これを後段の培地(表4の無機培地から(NH4
2 HPO4 を除き、炭素源を加えたものを使用)100
mlに投入して、30℃、48時間振盪培養した。炭素源
には、必須炭素源としてパルミチン酸ナトリウム3g/
l、付加的炭素源としてn−ノニル酢酸2g/lを用い
た。培養後、生成ポリエステルを分析した。その結果、
乾燥菌体重量は7.4g/l、ポリエステル含有率46
%で、該ポリエステルの組成は3HB87%、3HV1
3%であった。また、融点は134℃であった。
Example 9 Polypeptone 10 g, meat extract 5 g, yeast extract 10
g, and 5 g of (NH 4 ) 2 SO 4 dissolved in 1 liter of water, the strain was aseptically inoculated into a Sakaguchi flask containing 100 ml of a medium, and then shake-cultured at 30 ° C. for 24 hours. After completion of the culture, the culture solution was centrifuged (8000 rpm, 10 minutes) to collect the bacterial cells, which were then collected from the latter medium (from the inorganic medium of Table 4 (NH 4 )).
2 Except for HPO 4 , use a carbon source added) 100
The mixture was added to the cells and cultured with shaking at 30 ° C. for 48 hours. As a carbon source, as an essential carbon source, sodium palmitate 3 g /
1, n-nonyl acetic acid 2 g / l was used as an additional carbon source. After culturing, the produced polyester was analyzed. as a result,
Dry cell weight is 7.4 g / l, polyester content is 46
%, The composition of the polyester is 3HB 87%, 3HV1
It was 3%. The melting point was 134 ° C.

【0034】[0034]

【発明の効果】本発明によれば、天然に豊富な油脂や、
長鎖脂肪酸から効率よく生分解性、熱可塑性の該ポリエ
ステルを生産することができる。
According to the present invention, naturally rich oils and fats,
The polyester having biodegradability and thermoplasticity can be efficiently produced from long chain fatty acids.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 長鎖脂肪酸とその誘導体からなる化合物
群の少なくとも1種を必須炭素源とする液体培地を用い
て、アルカリゲネス属に属する3−ヒドロキシブチレー
ト含有ポリエステル生産菌を培養し、菌体内に3−ヒド
ロキシブチレート含有ポリエステルを蓄積させ、これを
採取することを特徴とするバイオポリエステルの製造
法。
1. A 3-hydroxybutyrate-containing polyester-producing bacterium belonging to the genus Alcaligenes is cultivated in a liquid medium containing at least one compound of a long-chain fatty acid and its derivative as an essential carbon source, and the inside of the bacterium is cultivated. A method for producing a biopolyester, comprising collecting 3-hydroxybutyrate-containing polyester in and collecting the polyester.
【請求項2】 必須炭素源が奇数炭素数の長鎖脂肪酸と
その誘導体からなる化合物亜群の少なくとも1種であ
り、ポリエステルが3−ヒドロキシブチレートと3−ヒ
ドロキシ吉草酸の共重合体である請求項1記載の製造
法。
2. The essential carbon source is at least one of a compound subgroup consisting of long-chain fatty acids having odd carbon numbers and derivatives thereof, and the polyester is a copolymer of 3-hydroxybutyrate and 3-hydroxyvaleric acid. The manufacturing method according to claim 1.
【請求項3】 必須炭素源が偶数炭素数の長鎖脂肪酸と
その誘導体からなる化合物亜群の少なくとも1種であ
り、ポリエステルがポリ(3−ヒドロキシブチレート)
または3−ヒドロキシブチレートと3−ヒドロキシ吉草
酸の共重合体である請求項1記載の製造法。
3. The essential carbon source is at least one of a compound subgroup consisting of long-chain fatty acids having an even number of carbon atoms and derivatives thereof, and the polyester is poly (3-hydroxybutyrate).
The method according to claim 1, which is a copolymer of 3-hydroxybutyrate and 3-hydroxyvaleric acid.
【請求項4】 偶数炭素数の長鎖脂肪酸とその誘導体か
らなる化合物亜群の少なくとも1種を必須炭素源とし、
下記化1 【化1】CH3 (CH2 2n-1X (式中、XはCORまたはCH2 OR’を表わし、Rは
水素、メトキシまたはエトキシ、R’は水素、アセチル
またはプロピオニル、nは1〜4の整数を表わす。)で
示される化合物群の少なくとも1種を付加的炭素源とす
る液体培地を用いて、アルカリゲネス属に属する3−ヒ
ドロキシブチレート含有ポリエステル生産菌を培養し、
菌体内に3−ヒドロキシブチレートと3−ヒドロキシ吉
草酸の共重合体を蓄積させ、これを採取することを特徴
とするバイオポリエステルの製造法。
4. An essential carbon source comprising at least one compound selected from the group consisting of even-numbered long-chain fatty acids and their derivatives.
CH 3 (CH 2 ) 2n-1 X (wherein X represents COR or CH 2 OR ', R is hydrogen, methoxy or ethoxy, R'is hydrogen, acetyl or propionyl, n Represents an integer of 1 to 4), a 3-hydroxybutyrate-containing polyester-producing bacterium belonging to the genus Alcaligenes is cultivated using a liquid medium containing at least one kind of compound group represented by
A method for producing a biopolyester, which comprises accumulating a copolymer of 3-hydroxybutyrate and 3-hydroxyvaleric acid in cells and collecting the copolymer.
【請求項5】 必須炭素源が長鎖脂肪酸のトリグリセラ
イドまたはその混合物である請求項1ないし4のいずれ
かに記載の製造法。
5. The method according to claim 1, wherein the essential carbon source is triglyceride of long chain fatty acid or a mixture thereof.
JP03254199A 1991-06-24 1991-09-06 Method for producing biopolyester Expired - Fee Related JP3114148B2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP03254199A JP3114148B2 (en) 1991-09-06 1991-09-06 Method for producing biopolyester
US07/903,021 US5346817A (en) 1991-06-24 1992-06-23 Method for producing a microbial polyester
DE69221957T DE69221957T2 (en) 1991-06-24 1992-06-24 Process for producing a microbial polyester containing D - (-) - 3-hydroxybutyrate monomer units
EP92110632A EP0520405B1 (en) 1991-06-24 1992-06-24 Method for producing a microbial polyester comprising D-(-)-3-hydroxybutyrate monomer units

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP03254199A JP3114148B2 (en) 1991-09-06 1991-09-06 Method for producing biopolyester

Publications (2)

Publication Number Publication Date
JPH0564592A true JPH0564592A (en) 1993-03-19
JP3114148B2 JP3114148B2 (en) 2000-12-04

Family

ID=17261629

Family Applications (1)

Application Number Title Priority Date Filing Date
JP03254199A Expired - Fee Related JP3114148B2 (en) 1991-06-24 1991-09-06 Method for producing biopolyester

Country Status (1)

Country Link
JP (1) JP3114148B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006025375A1 (en) 2004-08-31 2006-03-09 Riken Biopolyester with thermal stability
JP2009500468A (en) * 2005-07-04 2009-01-08 エルジー・ケム・リミテッド Poly (3-hydroxyalkanoate) block copolymer having shape memory effect

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006025375A1 (en) 2004-08-31 2006-03-09 Riken Biopolyester with thermal stability
JP2009500468A (en) * 2005-07-04 2009-01-08 エルジー・ケム・リミテッド Poly (3-hydroxyalkanoate) block copolymer having shape memory effect

Also Published As

Publication number Publication date
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