JP4803434B2 - Highly efficient production method of mannosyl erythritol lipid - Google Patents

Highly efficient production method of mannosyl erythritol lipid Download PDF

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JP4803434B2
JP4803434B2 JP2006081597A JP2006081597A JP4803434B2 JP 4803434 B2 JP4803434 B2 JP 4803434B2 JP 2006081597 A JP2006081597 A JP 2006081597A JP 2006081597 A JP2006081597 A JP 2006081597A JP 4803434 B2 JP4803434 B2 JP 4803434B2
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mel
mannosyl erythritol
pseudozyma
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友岳 森田
徳馬 福岡
知弘 井村
大 北本
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National Institute of Advanced Industrial Science and Technology AIST
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for highly efficiently producing a mannosylerythritol lipid (MEL) of a glycolipid of one kind of a biosurfactant by using microorganisms. <P>SOLUTION: Microorganisms having MFL-producing ability, Pseudozyma parantarctica, are cultured in an MEL-producing medium consisting essentially of oils and fats such as a vegetable oil and fat. At the time, the MEL can be efficiently produced by regulating the culture temperature at 33-37&deg;C. <P>COPYRIGHT: (C)2008,JPO&amp;INPIT

Description

本発明は、バイオサーファクタントの一種であるマンノシルエリスリトールリピッドの生産効率(生産量、生産速度、及び収率)を大幅に向上させることができるマンノシルエリスリトールリピッドの生産方法に関する。   The present invention relates to a production method of mannosyl erythritol lipid capable of greatly improving the production efficiency (production amount, production rate, and yield) of mannosyl erythritol lipid which is a kind of biosurfactant.

糖脂質は、脂質に1〜数十個の単糖が結合した物質であり、生体内において細胞間の情報伝達に関与し、神経系及び免疫系の機能維持にも重要な役割を果たしていることなどが明らかにされつつある。また、糖脂質は,糖の性質に由来する親水性と脂質の性質に由来する親油性の二つの性質を合わせ持つ両親媒性物質であり、このような性質を有する両親媒性物質は界面活性物質と呼ばれている。石油化学工業が隆盛となるまでは、レシチン、サポニン等の生体成分由来の界面活性剤 (バイオサーファクタント)が利用されていた。近年、石油化学工業の発展により合成界面活性剤が開発され、その生産量が飛躍的に増加し、日常生活には無くてはならない物質となったが、この合成界面活性剤の使用量の拡大に伴って環境汚染が広がり、社会問題が生じている。このため、安全性が高く、環境に対する負荷を低減できる生分解性の高い界面活性物質の開発が望まれている。   Glycolipids are substances in which 1 to several tens of monosaccharides are bound to lipids, are involved in information transmission between cells in vivo, and play an important role in maintaining the functions of the nervous system and immune system. Etc. are being revealed. In addition, glycolipids are amphiphilic substances that have both hydrophilic properties derived from the properties of sugars and lipophilic properties derived from the properties of lipids. It is called a substance. Until the petrochemical industry prospered, surfactants (biosurfactants) derived from biological components such as lecithin and saponin were used. Synthetic surfactants have been developed in recent years due to the development of the petrochemical industry, and their production has dramatically increased, making it an indispensable substance for daily life. As a result, environmental pollution has spread and social problems have arisen. For this reason, it is desired to develop a highly biodegradable surfactant that is highly safe and can reduce the burden on the environment.

従来より、微生物が生産する界面活性物質としては、糖脂質系、アシルペプタイド系、リン脂質系、脂肪酸系及び高分子系の界面活性物質の5つに分類されている。これらの中でも、糖脂質系の界面活性剤が最もよく研究されており、細菌及び酵母による多くの種類の界面活性物質が報告されている。
前記細菌としては、Pseudomonas属によるラムノリピッド(非特許文献1及び2参照)とユスチラジン酸(非特許文献3参照)、Rhodococcus属によるトレハロースリピッド(非特許文献4参照)などが知られている。しかし、いずれも生産量は15g/L以下である。
前記酵母としては、Candida属によるソホロースリピッドとマンノシルエリスリトールリピッド(特許文献1参照)などが知られている。
前記ソホロースリピッドについては、Candida bombicolaを用いてグルコースとオレイン酸の流加培養法により200時間で180g/Lの効率的なソホロースリピッドの生産が可能であることが報告されている(非特許文献5参照)。
Conventionally, the surface active substances produced by microorganisms are classified into five types: surface active substances of glycolipid type, acyl peptide type, phospholipid type, fatty acid type and polymer type. Among these, glycolipid-based surfactants are the most studied, and many types of surfactants from bacteria and yeast have been reported.
Examples of the bacteria, (see Non-Patent Document 3) rhamnolipid (Non-Patent Documents 1 and 2 refer) and Yusuchirajin acid by Pseudomonas spp, such as trehalose lipid (see Non-Patent Document 4) is known by the genus Rhodococcus. However, in all cases, the production amount is 15 g / L or less.
As said yeast, the sophorose lipid by Candida genus, the mannosyl erythritol lipid (refer patent document 1), etc. are known.
As for the sophorose lipid, it has been reported that it is possible to efficiently produce 180 g / L of sophorose lipid in 200 hours by the fed-batch culture method of glucose and oleic acid using Candida bombicola (non-patent document). Reference 5).

前記マンノシルエリスリトールリピッド(MEL)については、Candida sp.B−7株を用いて5質量%の大豆油から5日間で35g/L(生産速度:0.3g/L/h、原料収率:70質量%)のMELの生産が可能であることが報告されている(非特許文献6及び7参照)。また、Candida antarctica T−34株を用いて8質量%の大豆油から8日間で38g/L(生産速度:0.2g/L/h、原料収率:48質量%)のMELの生産が可能であることが報告されている(非特許文献8及び9参照)。同じく、Candida antarctica T−34株を用いて6日間隔で計3回の逐次流加により24日後に25質量%のピーナッツ油から110g/L(生産速度:0.2g/L/h、原料収率:44質量%)のMELの生産が可能であることが報告されている(非特許文献10参照)。 Regarding the mannosyl erythritol lipid (MEL), Candida sp. It is possible to produce 35 g / L (production rate: 0.3 g / L / h, raw material yield: 70 mass%) of MEL from 5 mass% soybean oil using B-7 strain in 5 days. Have been reported (see Non-Patent Documents 6 and 7). Also, using Candida antarctica T-34 strain, it is possible to produce 38 g / L (production rate: 0.2 g / L / h, raw material yield: 48 mass%) from 8 mass% soybean oil in 8 days. (See Non-Patent Documents 8 and 9). Similarly, 110 g / L (production rate: 0.2 g / L / h, raw material yield) from 25% by mass of peanut oil after 24 days by Caddida antarctica T-34 strain using a total of 3 sequential feedings at 6-day intervals. It has been reported that production of MEL at a rate of 44 mass% is possible (see Non-Patent Document 10).

Candida sp.SY−16株を用いて10質量%の植物油脂から回分培養法により200時間で50g/L(生産速度:0.25g/L/h、原料収率:50質量%)のMELの生産が可能であると共に、流加培養法により20質量%の植物油から200時間で120g/L(生産速度:0.6g/L/h、原料収率:50質量%)のMELの生産が可能であることが報告されている(非特許文献11参照)。
Pseudozyma aphidis株を用いて80質量%の植物油脂から流加培養法により24時間で13.9g/L (生産速度:0.57g/L/h、原料収率:92質量%)のMELの生産が可能であることが報告されている(非特許文献12参照)。
また、醤油醸造工程において副産物として生産されるしょうゆ油(あぶら)を原料としてCandida antarctica T−34株を用いて7日間で8質量%のしょうゆ油から17g/L(生産速度:0.1g/L/ h、原料収率:21質量%)のMELの生産が可能であることが提案されている(特許文献2参照)。
Candida sp. 50g / L (production rate: 0.25g / L / h, raw material yield: 50% by mass) can be produced in 200 hours by batch culture method from 10% by weight of vegetable oil using SY-16 strain In addition, 120 g / L (production rate: 0.6 g / L / h, raw material yield: 50 mass%) of MEL can be produced from 20 mass% of vegetable oil in 200 hours by fed-batch culture method. Has been reported (see Non-Patent Document 11).
Production of 13.9 g / L (production rate: 0.57 g / L / h, raw material yield: 92% by mass) of MEL from 80% by mass of vegetable oil using Pseudozyma aphidis strain in 24 hours by fed-batch culture method Has been reported to be possible (see Non-Patent Document 12).
Moreover, 17 g / L (production rate: 0.1 g / L) from 8% by weight soy sauce oil in 7 days using soy sauce oil (oil) produced as a by-product in the soy sauce brewing process using Candida antarctica T-34 strain / H, raw material yield: 21% by mass) has been proposed (see Patent Document 2).

特開2002−45195号公報JP 2002-45195 A 特開2002−101847号公報JP 2002-101847 A S.Itoh, H.Honda, Ftonami and T.Suzuki: J. Antibiotics,23,885(1971).S. Itoh, H.C. Honda, Ftonami and T. Suzuki: J. et al. Antibiotics, 23, 885 (1971). M.Yamaguti, A.Sato and R.Yukuyama: Chem.Ind.,17,741(1976).M.M. Yamaguchi, A .; Sato and R.M. Yukuyama: Chem. Ind. 17, 741 (1976). S.S.Bhattacharijee, R.H.Haskins and P.A.Golin: Carbohyd.Res.,13,235(1970).S. S. Bhattacharijee, R.A. H. Haskins and P.M. A. Golin: Carbohyd. Res. 13, 235 (1970). P.Rapp, H.Boch, V.Wary and F.Wagner: J.Gen.Microbiol.,115,491(1979).P. Rapp, H.M. Boch, V.D. Wary and F.M. Wagner: J.M. Gen. Microbiol. 115, 491 (1979). U.Rau, C.Manzke and F.Wagner: Biotechnol.Lett., 18, 149(1996).U. Rau, C.I. Manzke and F.M. Wagner: Biotechnol. Lett. , 18, 149 (1996). T.Nakahara, H.Kawasaki, T.Sugisawa, Y.Takamori and T.Tabuchi: J.Ferment.Technol., 61, 19(1983).T.A. Nakahara, H .; Kawasaki, T .; Sugisawa, Y .; Takamori and T.K. Tabuchi: J. et al. Ferment. Technol. , 61, 19 (1983). H.Kawasaki, T.Nakahara, M.Oogaki and T.Tabuchi: J.Ferment.Technol., 61, 143(1983).H. Kawasaki, T .; Nakahara, M .; Oogaki and T.K. Tabuchi: J. et al. Ferment. Technol. 61, 143 (1983). D.Kitamoto, S.Akiba, C.Hioki and T.Tabuchi: Agric.Biol.Chem., 54, 31(1990).D. Kitamoto, S.M. Akiba, C.I. Hioki and T.W. Tabuchi: Agric. Biol. Chem. , 54, 31 (1990). D.KItamoto, K.Haneishi, T.Nakahara and T.Tabuchi: Agric.Biol.Chem., 54, 37(1990).D. Kitamoto, K. et al. Haneishi, T .; Nakahara and T.A. Tabuchi: Agric. Biol. Chem. , 54, 37 (1990). D.Kitamoto, K.Fijishiro, H.Yanagishita, T.Nakane and T.Nakahara: Biotechnol.Lett., 14, 305(1992).D. Kitamoto, K. et al. Fijishiro, H.M. Yanagishita, T .; Nakane and T.K. Nakahara: Biotechnol. Lett. , 14, 305 (1992). 金,伊炳大,桂樹徹,谷吉樹:平成10年日本生物工学会大会要旨,p195.Kim, Ito Univ., Toru Katsuragi, Yoshiki Tani: Abstracts of 1998 Annual Meeting of the Japanese Society for Biotechnology, p195. U.Rau, L.A.Naguyen, H.Roeper, H.Koch and S.Lang: Appl.Microbiol.Biotechnol.,(2005).U. Rau, L. A. Naguyen, H.H. Roeper, H. Koch and S. Lang: Appl. Microbiol. Biotechnol. , (2005).

一方、生分解性が高く、低毒性で環境に優しく、新規な生理機能を持つといわれるマンノシルエリスリトールリピッドなどのバイオサーファクタントを食品工業、医薬品工業、化学工業などで広く普及させていくためには、マンノシルエリスリトールリピッドの生産効率を高め、生産コストの低減を図ることが必要である。本発明は、このような要望に応え、従来における前記諸問題を解決し、以下の目的を達成することを課題とする。即ち、本発明は、マンノシルエリスリトールリピッドを生産する能力を有する微生物を用い、その培地組成及び培養条件を最適化することによって、マンノシルエリスリトールリピッド(MEL)を効率よく生産することができる方法を提供することを目的とする。   On the other hand, in order to widely disseminate biosurfactants such as mannosyl erythritol lipid, which is said to have high biodegradability, low toxicity, environmental friendliness and novel physiological functions, in the food industry, pharmaceutical industry, chemical industry, etc. It is necessary to increase the production efficiency of mannosyl erythritol lipid and to reduce the production cost. An object of the present invention is to meet such demands, solve the above-described problems, and achieve the following objects. That is, the present invention provides a method capable of efficiently producing mannosyl erythritol lipid (MEL) by using a microorganism having the ability to produce mannosyl erythritol lipid and optimizing the medium composition and culture conditions. For the purpose.

前記課題を解決するため本発明者らが鋭意検討を重ねた結果、マンノシルエリスリトールリピッド生産する能力を有する微生物を、植物油脂等の油脂類を主成分として含有する培地で培養してマンノシルエリスリトールリピッドを生産するに際し、培養温度を33〜37℃に設定することにより、マンノシルエリスリトールリピッドを高い生産効率で生産できることを見出し、本発明を完成するに至った。   As a result of intensive studies by the present inventors in order to solve the above problems, a microorganism having an ability to produce mannosyl erythritol lipid is cultured in a medium containing oils and fats such as vegetable oils as a main component, so that mannosyl erythritol lipids are obtained. In production, the inventors found that mannosyl erythritol lipid can be produced with high production efficiency by setting the culture temperature to 33 to 37 ° C., and the present invention has been completed.

すなわち、本発明は以下のとおりである。
(1)油脂類含有培地でマンノシルエリスリトールリピッドを生産する能力を有する微生物を培養してマンノシルエリスリトールリピッドを生産するに際し、培養温度を33〜37℃に設定することを特徴とする、マンノシルエリスリトールリピッドの生産方法。

(2)上記マンノシルエリスリトールリピッドを生産する能力を有する微生物が、シュードザイマ(Pseudozyma)属に属する微生物であることを特徴とする上記(1)に記載の生産方法。

(3)シュードザイマ(Pseudozyma)属に属する微生物がシュードザイマ・パラアンタクティカ(Pseudozyma parantarctica)に属する微生物であることを特徴とする、上記(2)に記載の生産方法。

(4)初発油脂類濃度が2〜30重量%である培地で培養を行うことを特徴とする、上記(1)〜(3)のいずれかに記載の生産方法。

(5)初発油脂類濃度が2〜30質量%である培地で培養を開始し、該培養開始後5〜7日目より油脂類及び/又はその他の栄養源を培地中に供給することを特徴とする、上記(1)〜(3)のいずれかに記載の生産方法。

(6)培地の窒素源として硝酸アンモニウムを使用することを特徴とする、上記(1)〜(5)のいずれかに記載の生産方法。

(7)培地組成が、以下に示されるものであることを特徴とする、上記(1)〜(5)のいずれか に記載の生産方法。
酵母エキス:0.1〜2g/L
硝酸ナトリウム:0.1〜1g/L
リン酸2水素カリウム:0.1〜2g/L
硫酸マグネシウム:0.1〜1g/L
植物油脂:20〜300g/L
That is, the present invention is as follows.
(1) When a mannosyl erythritol lipid is produced by culturing a microorganism capable of producing a mannosyl erythritol lipid in an oil-containing medium, the culture temperature is set to 33 to 37 ° C. Production method.

(2) The production method according to (1) above, wherein the microorganism having the ability to produce the mannosyl erythritol lipid is a microorganism belonging to the genus Pseudozyma .

(3) Pseudozyma (Pseudozyma) microorganism belonging to the genus characterized in that it is a microorganism belonging to Pseudozyma para Anta click Tikka (Pseudozyma parantarctica), method of production according to (2).

(4) The production method according to any one of (1) to (3) above, wherein the culture is performed in a medium having an initial oil and fat concentration of 2 to 30% by weight.

(5) Culturing is started in a medium having an initial oil and fat concentration of 2 to 30% by mass, and fats and / or other nutrient sources are supplied into the medium from 5 to 7 days after the start of the culture. The production method according to any one of (1) to (3) above.

(6) The production method according to any one of (1) to (5) above, wherein ammonium nitrate is used as a nitrogen source of the medium.

(7) The production method according to any one of (1) to (5) above, wherein the medium composition is as shown below.
Yeast extract: 0.1-2 g / L
Sodium nitrate: 0.1-1 g / L
Potassium dihydrogen phosphate: 0.1-2 g / L
Magnesium sulfate: 0.1-1 g / L
Vegetable oil and fat: 20-300 g / L

本発明によれば、マンノシルエリスリトールリピッドを生成する能力を有する微生物を植物油脂等の油脂類含有培地で培養するに際し、培養温度を33〜37℃、特に35℃に設定することで、マンノシルエリスリトールリピッドを極めて効率良く生産できる。特に、シュードザイマ属に属する微生物であるシュードザイマ・パラアンタクティカ(Pseudozyma parantarctica JCM 11752)を使用する場合には生産速度が約2倍に上昇する。 According to the present invention, when culturing a microorganism having the ability to produce mannosyl erythritol lipid in a fat-containing medium such as vegetable oil, the culture temperature is set to 33 to 37 ° C., particularly 35 ° C., so that mannosyl erythritol lipid is obtained. Can be produced very efficiently. In particular, when Pseudozyma parantarctica JCM 11752, which is a microorganism belonging to the genus Pseudozyma, is used, the production rate is increased about twice.

本発明によって、マンノシルエリスリトールリピッドを生産する際の温度制御エネルギーの削減が可能になる。つまり、マンノシルエリスリトールリピッド生産の際、発酵熱が生じるため培養温度の制御が必要であるが、以前の生産方法における培養温度が30℃以下であるのに対して、本発明では培養温度を35℃以上に設定することができ、5℃以上の冷却コスト(エネルギー)を削減することが可能である。   The present invention makes it possible to reduce temperature control energy when producing mannosyl erythritol lipids. That is, during the production of mannosyl erythritol lipid, the fermentation temperature is generated, and thus the culture temperature must be controlled. In contrast, the culture temperature in the previous production method is 30 ° C. or lower, whereas in the present invention, the culture temperature is 35 ° C. It can be set as described above, and the cooling cost (energy) of 5 ° C. or more can be reduced.

生産効率の向上に伴い、高い生産性を得るための培養手段の簡素化も期待できる。すなわち、以前の生産方法では、100 g/L 以上のマンノシルエリスリトールリピッドを得るために、数週間、培養状態のモニタリングと栄養源の途中添加が必要であった。一方、本発明によれば、1週間、振とう培養のみで100 g/L 以上のマンノシルエリスリトールリピッドが得られ、特殊な装置や培養状態のモニタリングと栄養源の途中添加は不要である。また、より高い生産量を得るために、数週間、培養状態のモニタリングと栄養源の途中添加を行えば、当然、以前の生産方法を凌駕する生産量が達成できる。   As production efficiency improves, simplification of culture means for obtaining high productivity can be expected. That is, in the previous production method, monitoring the culture state and adding nutrient sources during the course of several weeks were required in order to obtain mannosylerythritol lipids of 100 g / L or more. On the other hand, according to the present invention, mannosyl erythritol lipids of 100 g / L or more can be obtained only by shaking culture for 1 week, and special equipment, monitoring of the culture state, and intermediate addition of nutrient sources are unnecessary. Moreover, in order to obtain a higher production volume, if the culture state is monitored and nutrient sources are added during the course of several weeks, the production volume that naturally surpasses the previous production method can be achieved.

さらに、本発明においては、植物油等の油脂類の消費速度も向上するため、結果としてこれら由来の油分の生成物への混入を低減し、マンノシルエリスリトールリピッドの分離精製においても効果が期待できる。
したがって、本発明は、医薬等種々用途への使用が期待されるバイオサーファクタントの生産技術の発展に大いに貢献するものである。
Furthermore, in this invention, since the consumption rate of fats and oils, such as vegetable oil, also improves, as a result, mixing in the oil component of these origin is reduced, and the effect can be expected also in the separation and purification of mannosyl erythritol lipid.
Therefore, the present invention greatly contributes to the development of biosurfactant production technology expected to be used for various uses such as medicine.

(目的生産物)
本発明の目的生産物であるマンノシルエリスリトールリピッド(MEL)は、下記構造式(1)で表される化合物である。

Figure 0004803434
(Target product)
Mannosyl erythritol lipid (MEL), which is a target product of the present invention, is a compound represented by the following structural formula (1).
Figure 0004803434

前記構造式(1)において、R〜Rは、互いに同一であっても異なっていてもよく、水素原子、アセチル基、又は炭素原子数1〜14、好ましくは3〜12の飽和若しくは不飽和の脂肪酸残基を表す。
前記マンノシルエリスリトールリピッド(MEL)は、高い界面活性作用を有し、界面活性剤又はファインケミカルの種々の触媒として用いられる。ヒト急性前骨髄性白血病細胞性HL60株にマンノシルエリスリトールリピッドを作用させると顆粒系を分化させる白血病細胞細胞分化誘導作用があり、 また、ラット副腎髄質褐色細胞腫由来のPC12細胞にマンノシルエリスリトールリピッドを作用させると神経突起の伸長が生ずる神経系細胞株分化誘導作用等の生理活性作用を有する。更に、微生物産生の糖脂質として初めて、メラノーマ細胞のアポトーシスを誘導することが可能となり(X. Zhao et. al., Cancer Research,59, 482−486(1999))、癌細胞増殖抑制作用がある。これらの生理作用から見て、マンノシルエリスリトールリピッドには抗ガン剤等の医薬としての用途が期待される。また、マンノシルエリスリトールリピッド(MEL)には生分解性があり、高い安全性を有すると考えられているものである。
In the structural formula (1), R 1 to R 4 may be the same or different from each other, and may be a hydrogen atom, an acetyl group, or a saturated or unsaturated group having 1 to 14 carbon atoms, preferably 3 to 12 carbon atoms. Represents a saturated fatty acid residue.
The mannosyl erythritol lipid (MEL) has a high surface activity and is used as various surfactants or fine chemical catalysts. When mannosyl erythritol lipid is allowed to act on human acute promyelocytic leukemia cell line HL60, it induces leukemia cell differentiation that differentiates the granule system, and mannosyl erythritol lipid acts on PC12 cells derived from rat adrenal medullary pheochromocytoma It has a physiological activity such as a neural cell line differentiation-inducing action that causes neurite outgrowth. Furthermore, for the first time as a glycolipid produced by microorganisms, it becomes possible to induce apoptosis of melanoma cells (X. Zhao et. Al., Cancer Research, 59 , 482-486 (1999)) and has an effect of suppressing cancer cell growth. . In view of these physiological actions, mannosyl erythritol lipid is expected to be used as a medicine such as an anticancer agent. In addition, mannosyl erythritol lipid (MEL) is biodegradable and is considered to have high safety.

(使用微生物)
本発明の使用微生物については、マンノシルエリスリトールリピッドを生産する能力を有するものであれば特に制限はなく、例えばシュードザイマ属に属する微生物が挙げられ、このうち特に好ましい微生物としては、シュードザイマ・パラアンタクティカに属する微生物が挙げることができる。該微生物はマンノシルエリスリトール生産微生物として知られていなかったものであるが、本発明者等により、シュードザイマ・アンタクチカ等の既知のマンノシルエリスリトールリピッド生産菌と同等の生産性を有することが初めて確認されたものである。しかも、このシュードザイマ・パラアンタクティカ(Pseudozyma parantarctica)に属する微生物は、例えば33〜37℃で培養した場合の生産性向上効果が特に高く、例えば、シュードザイマ・パラアンタクティカ(Pseudozyma parantarctica)JCM 11752株の場合、培養温度35℃の場合約2倍に達する点で特筆すべきものである。
(Used microorganism)
The microorganism used in the present invention is not particularly limited as long as it has the ability to produce mannosyl erythritol lipids, and examples thereof include microorganisms belonging to the genus Pseudozyma. Among them, particularly preferable microorganisms include Pseudozyma paraantactica. Can be mentioned. The microorganism was not known as a mannosyl erythritol-producing microorganism, but was first confirmed by the present inventors to have productivity equivalent to that of known mannosyl erythritol lipid-producing bacteria such as pseudozyma and antactica. It is. Moreover, the microorganism belonging to Pseudozyma parantarctica has a particularly high productivity improvement effect when cultured at 33 to 37 ° C., for example, Pseudozyma parantarctica ( Pseudozyma parantarctica) JCM 11752 In the case of the strain, it is noteworthy in that it reaches about twice when the culture temperature is 35 ° C.

(マンノシルエリスリトールリピッドの生産)
本発明における使用微生物の培養においては、培地に、脂肪酸、脂肪酸トリグリセリド等の脂肪酸エステル類、あるいは植物油等の油脂類を含有させるが、温度条件以外の条件については、特に制限はなく、適宜選定することができる。例えば、酵母に対して一般に用いられる培地を使用でき、このような培地として、例えば、YPD培地(イーストイクストラクト10g、 ポリペプトン20g、及びグルコース100g)を挙げることができる。
MELの生産量を増加させるためには培養温度を33〜37℃に設定することが好ましく、本発明者等は、培養開始時の培養温度を変化させて培養を行った結果、培養温度を35℃に設定した場合に、特に良好なMELの生産速度、生産量、及び収率が得られるという知見を得ている。
(Mannosyl erythritol lipid production)
In culturing the microorganisms used in the present invention, the medium contains fatty acid esters such as fatty acids and fatty acid triglycerides, or fats and oils such as vegetable oils. Conditions other than temperature conditions are not particularly limited and are appropriately selected. be able to. For example, a medium generally used for yeast can be used, and examples of such a medium include YPD medium (yeast extract 10 g, polypeptone 20 g, and glucose 100 g).
In order to increase the production amount of MEL, it is preferable to set the culture temperature to 33 to 37 ° C., and as a result of culturing by changing the culture temperature at the start of the culture, the present inventors have set the culture temperature to 35 It has been found that particularly good MEL production rates, yields and yields can be obtained when set to ° C.

本発明の使用微生物、特に前記シュードザイマ・パラアンタクティカ(Pseudozyma parantarctica JCM 11752)株を用いてマンノシルエリスリトールリピッドを生産する場合の好適な培地組成は、以下のとおりである。
酵母エキスは、0.1〜2g/Lが好ましく、1g/Lが特に好ましい
硝酸ナトリウムは、0.1〜1g/Lが好ましく、0.5g/Lが特に好ましい。
リン酸2水素カリウムは、0.1〜2g/Lが好ましく、0.4g/Lが特に好ましい。
硫酸マグネシウムは、0.1〜1g/Lが好ましく、0.2g/Lが特に好ましい。
植物性油脂は、80g/L以上が好ましく、180g/Lが特に好ましい。
Microorganisms use of the present invention, the preferred medium composition of especially when producing mannosylerythritol lipid using the Pseudozyma para Anta click Tikka (Pseudozyma parantarctica JCM 11752) strain is as follows.
The yeast extract is preferably 0.1 to 2 g / L, particularly preferably 1 g / L. Sodium nitrate is preferably 0.1 to 1 g / L, particularly preferably 0.5 g / L.
The potassium dihydrogen phosphate is preferably 0.1 to 2 g / L, particularly preferably 0.4 g / L.
Magnesium sulfate is preferably 0.1 to 1 g / L, particularly preferably 0.2 g / L.
As for vegetable oil and fat, 80 g / L or more is preferable and 180 g / L is especially preferable.

本発明のマンノシルエリスリトールリピッドの製造方法は、特に制限はなく、目的に応じて適宜選定することができるが、例えば、種培養、本培養及びマンノシルエリスリトールリピッド生産培養の順にスケールアップしていくことが望ましい。
これらの培養における、培地、培養条件を例示すると以下のとおりである。
a)種培養;グルコース20g/L、酵母エキス1g/L、硝酸ナトリウム1g/L、リン酸2水素カリウム 0.5g/L、及び硫酸マグネシウム0.5g/Lの組成の液体培地4mLが入った試験管に1白金耳接種し、30℃で1日間振とう培養を行う。
The method for producing the mannosyl erythritol lipid of the present invention is not particularly limited and may be appropriately selected according to the purpose. For example, the seed culture, the main culture, and the mannosyl erythritol lipid production culture may be scaled up in this order. desirable.
Examples of culture media and culture conditions in these cultures are as follows.
a) Seed culture: 20 g / L of glucose, 1 g / L of yeast extract, 1 g / L of sodium nitrate, 0.5 g / L of potassium dihydrogen phosphate, and 4 mL of a liquid medium having a composition of 0.5 g / L of magnesium sulfate A platinum loop is inoculated into a test tube and cultured with shaking at 30 ° C. for 1 day.

b)本培養;所定量の植物性油脂等の油脂類と、酵母エキス1g/L、硝酸ナトリウム1 g/L、リン酸2水素カリウム0.5g/L、及び硫酸マグネシウム0.5g/Lの組成の液体培地100mLの入った坂口フラスコに接種して、33〜37℃で2日間培養を行う。
c)マンノシルエリスリトールリピッド生産培養;所定量の植物性油脂等の油脂類と酵母エキス1g/L、硝酸ナトリウム1g/L、リン酸2水素カリウム0.5g/L、及び硫酸マグネシウム 0.5g/Lの組成の液体培地1.4Lが入ったジャーファメンターに接種して、33〜37℃で800rpmの撹拌速度で培養を行う。この培養においては、培養途中から植物性油脂を培養容器中に流下させて、培地中の油脂類濃度を40〜200g/Lに保持することが望ましい。
b) Main culture: a predetermined amount of fats and oils such as vegetable oil and fat, yeast extract 1 g / L, sodium nitrate 1 g / L, potassium dihydrogen phosphate 0.5 g / L, and magnesium sulfate 0.5 g / L A Sakaguchi flask containing 100 mL of the liquid medium having the composition is inoculated and cultured at 33 to 37 ° C. for 2 days.
c) Mannosyl erythritol lipid production culture; predetermined amount of oils and fats such as vegetable oil and yeast extract 1 g / L, sodium nitrate 1 g / L, potassium dihydrogen phosphate 0.5 g / L, and magnesium sulfate 0.5 g / L A jar fermenter containing 1.4 L of a liquid medium having the following composition is inoculated and cultured at 33-37 ° C. at a stirring speed of 800 rpm. In this culturing, it is desirable that the vegetable fats and oils flow down into the culture vessel from the middle of the culturing to maintain the fats and oils concentration in the medium at 40 to 200 g / L.

以下に、本発明におけるマンノシルエリスリトールリピドの生産について実施例によりさらに詳細に説明するが、本発明はこれにより限定されるものではない。
なお、以下の実施例においては、マンノシルエリスリトールリピド生産試験用培地として、上記b)の本培養の培地を用いた。
Hereinafter, production of mannosyl erythritol lipid in the present invention will be described in more detail with reference to Examples, but the present invention is not limited thereto.
In the following Examples, the medium for main culture of b) above was used as a medium for production test of mannosyl erythritol lipid.

Pseudozyma parantarctica JCM 11752株の培養)
a)保存培地(麦芽エキス3g/L、酵母エキス3g/L、ペプトン5g/Lグルコース10g/L、寒天30g/L)に保存しておいたPseudozyma parantarctica JCM 11752株を、 グルコース20g/L、酵母エキス1g/L、硝酸ナトリウムム1g/L、リン酸2水素カリウム0.5g/L、及び硫酸マグネシウム0.5g/Lの組成の液 体培地4mLが入った試験管に1白金耳接種し30℃で振とう培養を行い、次いで、
b)得られた菌体培養液を所定量の植物性油脂と酵母エキス1g/L、硝酸ナトリウム1g/L、リン酸2水素カリウム0.5g/L、及び硫酸マグネシウム0.5g/Lの組成の液 体培地20mLの入った坂口フラスコに接種して、35℃で振とう培養を行った。
c)これを所定量の大豆油と酵母エキス1g/L、硝酸ナトリウム1g/L、リン酸2水素カリウム 0.5g/L、及び硫酸マグネシウム0.5g/Lの組成の液体培地1.4Lが入ったジャーファメンターに接種して、35℃で800rpmの撹拌速度で培養を行った。さらに、培養途中から1週間毎に植物性油脂(大豆油)を培養容器中に流下した。
( Pseudozyma parantarctica JCM 11752 strain culture)
a) Pseudozyma parantarctica JCM 11752 stored in a storage medium (malt extract 3 g / L, yeast extract 3 g / L, peptone 5 g / L glucose 10 g / L, agar 30 g / L), glucose 20 g / L, yeast 1 platinum ear was inoculated into a test tube containing 1 mL of extract, 1 g / L of sodium nitrate, 0.5 g / L of potassium dihydrogen phosphate and 0.5 g / L of magnesium sulfate. Shake culture at 0 ° C, then
b) Composition of the obtained cell culture broth with a predetermined amount of vegetable oil and fat, yeast extract 1 g / L, sodium nitrate 1 g / L, potassium dihydrogen phosphate 0.5 g / L, and magnesium sulfate 0.5 g / L Was inoculated into a Sakaguchi flask containing 20 mL of the liquid medium and cultured at 35 ° C. with shaking.
c) A liquid medium having a predetermined amount of soybean oil and yeast extract 1 g / L, sodium nitrate 1 g / L, potassium dihydrogen phosphate 0.5 g / L, and magnesium sulfate 0.5 g / L in a liquid medium 1.4 L The jar fermenter was inoculated and cultured at 35 ° C. with a stirring speed of 800 rpm. Further, vegetable oil (soybean oil) was allowed to flow down into the culture container every week from the middle of the culture.

上記a)-c)の各培養により得られた菌体培養液を使用して、以下の(1)〜(7)に示される試験を行った。
(試験手法、結果)
(1)Pseudozyma parantarctica JCM 11752株のマンノシルエリスリトールリピッド(MEL)生産能の確認
a)の培養を1日間行った後、b)の培養を大豆油添加培地で7日間行った後の培養液を採取し、これを用いてPseudozyma parantarctica JCM 11752株のバイオサーファクタントの生産性を薄層クロマトグラフィーで確認した。マンノシルエリスリトールリピッドの標準として、Pseudozyma antarctica JCM 10317株を上記と同じ条件で培養し、原料油脂等の不純物を取り除いた精製標品を用いた。マンノシルエリスリトールリピッド標準における、MEL−A,MEL−B及びMEL−Cはそれぞれ順に一般式中(R1、2=炭素原子数1〜14の脂肪酸残基、R3、4=アセチル基)、同(R1、2=炭素原子数1〜14の脂肪酸残基、R3=水素原子、R4=アセチル基)及び同(R1、2=炭素原子数1〜14の脂肪酸残基、R3=アセチル基、R4=水素原子)で表される化合物を示す。
結果を図1に示す。これによれば、両株とも大豆油含有培地でマンノシルエリスリトールリピッド(MEL)を生産している。また、マンノシルエリスリトールリピッドの標準と対比して、Pseudozyma parantarctica JCM 11752株が生産しているバイオサーファクタントはマンノシルエリスリトールリピッドであることがわかる。
Tests shown in the following (1) to (7) were performed using the cell culture broth obtained by each of the above cultures a) to c).
(Test method, results)
(1) Confirmation of mannosylerythritol lipid (MEL) production ability of Pseudozyma parantarctica JCM 11752 strain
After culturing a) for 1 day, the culture solution after b) culturing for 7 days in a soybean oil-added medium was collected and used to reduce the productivity of Pseudozyma parantarctica JCM 11752 biosurfactant. Confirmed by layer chromatography. As a standard for mannosyl erythritol lipid, Pseudozyma antarctica JCM 10317 strain was cultured under the same conditions as above, and a purified preparation from which impurities such as raw oils and fats were removed was used. In the mannosyl erythritol lipid standard, MEL-A, MEL-B and MEL-C are respectively in the general formulas (R1, 2 = fatty acid residue having 1 to 14 carbon atoms, R3, 4 = acetyl group) and (R1 2 = fatty acid residue having 1 to 14 carbon atoms, R3 = hydrogen atom, R4 = acetyl group) and the same (R1,2 = fatty acid residue having 1 to 14 carbon atoms, R3 = acetyl group, R4 = hydrogen) Atom) is shown.
The results are shown in FIG. According to this, both strains produce mannosyl erythritol lipid (MEL) in a soybean oil-containing medium. In contrast to the standard of mannosyl erythritol lipid, it can be seen that the biosurfactant produced by Pseudozyma parantarctica JCM 11752 is mannosyl erythritol lipid.

(2)マンノシルエリスリトールリピッド(MEL)生産用培地で同リピッドの生産
Pseudozyma parantarctica JCM 11752株を用い、a)の培養を1日間行った後、b)の培養を大豆油添加培地で7日間行った。培養液を採取し、精製後、生産されたMELを高速液体クロマトグラフィーで検出した。また、比較例としてPseudozyma antarctica JCM 10317株を上記と同じ条件で培養し、同様にして高速液体クロマトグラフィーで検出した。結果を図2に示す。なお、図2は、培養液中の酢酸エチル可溶分を精製後、高速液体クロマトグラフィーで検出した結果であり、既知のマンノシルエリスリトールリピッドのものと一致する。図2によれば、Pseudozyma parantarctica JCM 11752株はPseudozyma antarctica JCM 10317株と同様にMEL生産能力を有する。
(2) Mannosyl erythritol lipid (MEL) production in the same medium
Pseudozyma parantarctica JCM 11752 was used, and a) was cultured for 1 day, and then b) was cultured in a soybean oil-added medium for 7 days. The culture solution was collected and purified, and the produced MEL was detected by high performance liquid chromatography. As a comparative example, Pseudozyma antarctica JCM 10317 strain was cultured under the same conditions as described above and detected by high performance liquid chromatography in the same manner. The results are shown in FIG. In addition, FIG. 2 is the result of having detected the ethyl acetate soluble part in a culture solution, and having detected it by the high performance liquid chromatography, and corresponds with the thing of the known mannosyl erythritol lipid. According to FIG. 2, the Pseudozyma parantarctica JCM 11752 strain has a MEL production capacity similar to the Pseudozyma antarctica JCM 10317 strain.

(3)Pseudozyma parantarctica JCM 11752株が生産するマンノシルエリスリトールリピッド(MEL)の構造解析
Pseudozyma parantarctica JCM 11752株を用い、a)の培養を1日間行った後、b)の培養を大豆油添加培地で7日間行った。培養液を採取し、培養液中のMELを酢酸エチルで抽出し、精製後、H NMR で生産物の構造解析を行った(上段)。また、典型的なMELの構造解析結果の例としてPseudozyma antarctica JCM 10317株が生産するMELの分析結果を下段に示す。図3によれば、Pseudozyma parantarctica JCM 11752株が生産する物質は典型的なMELの構造を有することが明らかである。
(3) Structural analysis of mannosylerythritol lipid (MEL) produced by Pseudozyma parantarctica JCM 11752
Pseudozyma parantarctica JCM 11752 was used, and a) was cultured for 1 day, and then b) was cultured in a soybean oil-added medium for 7 days. The culture solution was collected, and MEL in the culture solution was extracted with ethyl acetate. After purification, the structure of the product was analyzed by 1 H NMR (upper). In addition, as an example of a typical structural analysis result of MEL, an analysis result of MEL produced by Pseudozyma antarctica JCM 10317 strain is shown in the lower part. According to FIG. 3, it is clear that the substance produced by Pseudozyma parantarctica JCM 11752 has a typical MEL structure.

(4)Pseudozyma parantarctica JCM 11752株のMEL生産に対する窒素源の影響
Pseudozyma parantarctica JCM 11752株を用い、a)の培養を1日間行った後、b)の培養を大豆油添加培地で7日間行った後、培養液を採取し、そのMEL生産量を高速液体クロマトグラフィーで検出した。このとき、培養液中の窒素源はそれぞれ図中に記載した組成に調製したものを用いた。結果を図4に示す。この結果によれば、Pseudozyma parantarctica JCM 11752株によるMEL生産において、最適な窒素源は硝酸ナトリウムである。
(4) Effect of nitrogen source on MEL production of Pseudozyma parantarctica JCM 11752
Using Pseudozyma parantarctica JCM 11752, a) was cultured for 1 day, b) was cultured in a soybean oil-added medium for 7 days, the culture was collected, and the amount of MEL produced was measured by high performance liquid chromatography. Detected with. At this time, the nitrogen sources in the culture solution were each prepared to have the composition described in the figure. The results are shown in FIG. According to this result, in the MEL production by Pseudozyma parantarctica JCM 11752, the most suitable nitrogen source is sodium nitrate.

(5)Pseudozyma parantarctica JCM 11752株のMEL生産に対する植物性油脂の影響
Pseudozyma parantarctica JCM 11752株を用い、a)の培養を1日間行った後、b)の培養を7日間行った後、培養液を採取し、そのMEL生産量を高速液体クロマトグラフィーで検出した。このとき、培養液中の植物性油脂はそれぞれ図中に記載した組成に調製したものを用いた。結果を図5に示す。この結果によれば、Pseudozyma parantarctica JCM 11752株は各種植物性油脂からMELを生産し、大豆油が最も良好な結果を示した。
(5) Effects of vegetable oils and fats on MEL production of Pseudozyma parantarctica JCM 11752
Using Pseudozyma parantarctica JCM 11752 strain, a) was cultured for 1 day, b) was cultured for 7 days, and then the culture broth was collected, and the amount of MEL produced was detected by high performance liquid chromatography. At this time, vegetable oils and fats in the culture solution were prepared to the compositions described in the figure. The results are shown in FIG. According to this result, Pseudozyma parantarctica JCM 11752 produced MEL from various vegetable oils, and soybean oil showed the best result.

(6)Pseudozyma parantarctica JCM 11752株のMEL生産に対する植物性油脂濃度の影響
Pseudozyma parantarctica JCM 11752株を用い、a)の培養を1日間行った後、b)の培養を7日間行った後、培養液を採取し、そのMEL生産量を高速液体クロマトグラフィーで検出した。このとき、培養液中に図中に示す量の大豆油を添加した。結果を図6に示す。この結果によれば、Pseudozyma parantarctica JCM 11752株によるMELの生産量は約50g/Lである。
(6) Effect of vegetable oil concentration on MEL production of Pseudozyma parantarctica JCM 11752
Using Pseudozyma parantarctica JCM 11752 strain, a) was cultured for 1 day, b) was cultured for 7 days, and then the culture broth was collected, and the amount of MEL produced was detected by high performance liquid chromatography. At this time, soybean oil in the amount shown in the figure was added to the culture solution. The results are shown in FIG. According to this result, the production amount of MEL by Pseudozyma parantarctica JCM 11752 strain is about 50 g / L.

(7)Pseudozyma parantarctica JCM 11752株のMEL生産に対する培養温度の影響
Pseudozyma parantarctica JCM 11752株を用い、a)の培養を1日間行った後、b)の培養を大豆油添加培地で7日間行った後、培養液を採取し、そのMEL生産量を高速液体クロマトグラフィーで検出した。このとき、培養温度を図7に示すように設定した。結果を図7に示す。この結果によれば、Pseudozyma parantarctica JCM 11752株の最適生産温度は35℃であり、30℃の場合と比べてMELの生産量は2倍以上高くなる。
(7) Effect of culture temperature on MEL production of Pseudozyma parantarctica JCM 11752
Using Pseudozyma parantarctica JCM 11752, a) was cultured for 1 day, b) was cultured in a soybean oil-added medium for 7 days, the culture was collected, and the amount of MEL produced was measured by high performance liquid chromatography. Detected with. At this time, the culture temperature was set as shown in FIG. The results are shown in FIG. According to this result, the optimum production temperature of Pseudozyma parantarctica JCM 11752 is 35 ° C, and the production of MEL is more than twice as high as that at 30 ° C.

(8)Pseudozyma parantarctica JCM 11752株のMEL生産培養
上記a)の培養を1日間行った後、b)の培養を、35℃で10日間行い、続いて、c)の培養を行った。c)の培養は160g/Lの大豆油を含む培地を用いて35℃で行った。培養途中から160g/Lの植物性油脂を1週間毎に培養容器中に流下させた。図8は、1週間毎に培養液を採取し、MEL生産量を高速液体クロマトグラフィーで定量して作製したグラフである。矢印は炭素源を添加した時点を示している。図8によると、14日間で生産されたMELの量は190g/L以上に達している。
(8) MEL production culture of Pseudozyma parantarctica JCM 11752 The above-mentioned a) was cultured for 1 day, then b) was cultured at 35 ° C. for 10 days, followed by c). C) was cultured at 35 ° C. using a medium containing 160 g / L soybean oil. From the middle of the culture, 160 g / L of vegetable oil was allowed to flow down into the culture container every week. FIG. 8 is a graph prepared by collecting a culture solution every week and quantifying the MEL production amount by high performance liquid chromatography. The arrow indicates the time when the carbon source is added. According to FIG. 8, the amount of MEL produced in 14 days reaches 190 g / L or more.


Pseudozyma parantarctica JCM 11752株が、大豆油含有培地でマンノシルエリスリトールリピドを生産しうること を示す、該培養物についての薄層クロマトグラフィー写真である。It is a thin layer chromatographic photograph about this culture | cultivation which shows that Pseudozyma parantarctica JCM11752 strain | stump | stock can produce mannosyl erythritol lipid in a soybean oil containing medium. Pseudozyma parantarctica JCM 11752株が、大豆油含有培地でマンノシルエリスリトールリピドを生産しうること を示す、該培養物についての高速液体クロマトグラフィーの分析結果を示す図である。It is a figure which shows the analysis result of the high performance liquid chromatography about this culture | cultivation which shows that Pseudozyma parantarctica JCM11752 strain | stump | stock can produce mannosyl erythritol lipid in a soybean oil containing medium. Pseudozyma parantarctica JCM 11752株が、大豆油含有培地でマンノシルエリスリトールリピドを生産しうることを示す、該培養物についての1H NMR による構造解析の結果を示す図である。It is a figure which shows the result of the structural analysis by 1H NMR about this culture | cultivation which shows that Pseudozyma parantarctica JCM11752 strain | stump | stock can produce mannosyl erythritol lipid in a soybean oil containing medium. Pseudozyma parantarctica JCM 11752株によるマンノシルエリスリトールリピドの生産に対する窒素源の影響を示すグラフである。It is a graph which shows the influence of a nitrogen source with respect to the production of mannosyl erythritol lipid by Pseudozyma parantarctica JCM11752 strain. Pseudozyma parantarctica JCM 11752株によるマンノシルエリスリトールリピドの生産に対する植物性油脂の影響を示すグラフである。It is a graph which shows the influence of vegetable oil and fats on the production of mannosyl erythritol lipid by Pseudozyma parantarctica JCM 11752 strain. Pseudozyma parantarctica JCM 11752株によるマンノシルエリスリトールリピドの生産に対する植物性油脂濃度の影響を示すグラフである。It is a graph which shows the influence of vegetable oil and fat concentration on the production of mannosyl erythritol lipid by Pseudozyma parantarctica JCM 11752 strain. Pseudozyma parantarctica JCM 11752株によるマンノシルエリスリトールリピドの生産に対する培養温度の影響を示すグラフである。It is a graph which shows the influence of culture | cultivation temperature with respect to the production of mannosyl erythritol lipid by Pseudozyma parantarctica JCM11752 strain | stump | stock. Pseudozyma parantarctica JCM 11752株のマンノシルエリスリトールリピド生産培養の結果を示すグラフである。It is a graph which shows the result of the mannosyl erythritol lipid production culture of Pseudozyma parantarctica JCM11752 strain | stump | stock.

Claims (3)

油脂類含有培地でマンノシルエリスリトールリピッドを生産する能力を有し、シュードザイマ・パラアンタクティカ(Pseudozyma parantarctica)に属する微生物を培養してマンノシルエリスリトールリピッドを生産するに際し、培養温度を33〜37℃に設定することを特徴とする、マンノシルエリスリトールリピッドの生産方法。 Upon possess the ability to produce the mannosylerythritol lipid in fats and oils containing medium, to produce mannosylerythritol lipid by culturing a microorganism belonging to the Pseudozyma para Anta click Atlantica (Pseudozyma parantarctica), set the culture temperature to 33~37 ℃ A method for producing mannosyl erythritol lipids, characterized in that: 初発油脂類濃度が2〜30重量%である培地で培養を行うことを特徴とする、請求項に記載の生産方法。 Initial fats and oils concentration and performing culture in a medium which is 2 to 30% by weight, method of production according to claim 1. 初発油脂類濃度が2〜30質量%である培地で培養を開始し、該培養開始後5〜7日目より油脂類及び/又はその他の栄養源を培地中に供給することを特徴とする、請求項1又は2に記載の生産方法。 The culture starts with a medium having an initial oil and fat concentration of 2 to 30% by mass, and oils and / or other nutrients are supplied into the medium from 5 to 7 days after the start of the culture. The production method according to claim 1 or 2 .
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