JPH02200193A - Production of omega3 based highly unsaturated fatty acid-containing lipid - Google Patents
Production of omega3 based highly unsaturated fatty acid-containing lipidInfo
- Publication number
- JPH02200193A JPH02200193A JP1019739A JP1973989A JPH02200193A JP H02200193 A JPH02200193 A JP H02200193A JP 1019739 A JP1019739 A JP 1019739A JP 1973989 A JP1973989 A JP 1973989A JP H02200193 A JPH02200193 A JP H02200193A
- Authority
- JP
- Japan
- Prior art keywords
- unsaturated fatty
- highly unsaturated
- omega3
- fatty acid
- based highly
- 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
Links
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明はω3系高度不飽和脂肪酸含有脂質の製造法に関
する。エイコサトリエン酸、エイコサテトラエン酸、エ
イコサベンクエン酸などのω3系高度不飽和脂肪酸は医
薬品、生化学試薬等として有用である。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing a lipid containing omega-3 highly unsaturated fatty acids. Omega-3 highly unsaturated fatty acids such as eicosatrienoic acid, eicosatetraenoic acid, and eicosabencitric acid are useful as pharmaceuticals, biochemical reagents, and the like.
〔従来の技術、発明が解決しようとする課題〕ω3系高
度不飽和脂肪酸の発酵生産法としては、糸状菌のモルテ
ィニラ属微生物を用いてエイコサペンタエン酸を製造す
る方法(特開昭63−14697号)2海洋細菌を用い
て同じくエイコサベンクエン酸を製造する方法〔埋込ら
、日本農芸化学会誌、62、 p259(1988)
)などが報告されている。そのほか、ハエカビ目のエン
トモフソラ属やコニディオボラス属の微生物がエイコサ
テトラエン酸およびエイコサベンクエン酸を生産するこ
と(J、 P、 Latgeら、J、 Gen、 Mi
crobiol、、 月u、 p151〜1.58(1
980))も知られている。[Prior art and problems to be solved by the invention] As a fermentation production method for ω3-based highly unsaturated fatty acids, a method for producing eicosapentaenoic acid using a microorganism of the genus Mortinilla (Japanese Patent Application Laid-open No. 14697/1983) ) 2 Method for producing eicosaben citric acid using marine bacteria [Mude et al., Journal of the Japanese Society of Agricultural Chemistry, 62, p. 259 (1988)
) etc. have been reported. In addition, microorganisms of the genus Entomophsora and Conidiobolus of the order Hyperoptera produce eicosatetraenoic acid and eicosabencitric acid (J, P., Latge et al., J., Gen., Mi.
crobiol,, month u, p151~1.58(1
980)) is also known.
しかしながら、これら方法により得られるω3系高度不
飽和脂肪酸の収率が低く、実用化するには問題がある。However, the yield of ω3 highly unsaturated fatty acids obtained by these methods is low, and there are problems in putting them into practical use.
そこで、本発明者はω3系高度不飽和脂肪酸を含有する
脂質を発酵法により効率よ(大量に生産する方法につい
て鋭意検討を重ねた結果、特定の微生物を用い、ω3系
高度不飽和脂肪酸の前駆体となるα−リノレン酸を培地
に添加し′ζ培養すればよいことを見出し、本発明を完
成させた。Therefore, the inventors of the present invention have developed a method for efficiently producing large quantities of lipids containing omega-3 polyunsaturated fatty acids using a fermentation method. The present invention was completed based on the discovery that α-linolenic acid, which serves as a protein, can be added to the medium and cultured in 'ζ.
すなわち、本発明はコニディオボラス属に属し、ω3系
高度不飽和脂肪酸生産能を有する微生物をα−リノレン
酸またはその誘導体を含む培地に培養し、培養物からω
3系高度不飽和脂肪酸含有脂質を採取することを特徴と
するω3系高度不飽和脂肪酸含有脂質の製造法を提供す
るものである。That is, the present invention involves culturing a microorganism belonging to the genus Conidiobolas and having the ability to produce ω3-based highly unsaturated fatty acids in a medium containing α-linolenic acid or its derivatives, and producing ω from the culture.
The present invention provides a method for producing a lipid containing ω3 highly unsaturated fatty acids, which is characterized by collecting a lipid containing ω3 highly unsaturated fatty acids.
本発明でいうω3系高度不飽和脂肪酸とは、11.14
、17−エイコサトリエン酸(以下、C2063と称す
。); 8.11.14.17−ニイコサテトラエン酸
(以下、C10m4と称す。): 5.8.11.14
.17エイコサベンクエン酸(以下、C!。、、と称す
。)などを指す。The ω3-based highly unsaturated fatty acids as used in the present invention are 11.14
, 17-eicosatrienoic acid (hereinafter referred to as C2063); 8.11.14.17-nicosatrienoic acid (hereinafter referred to as C10m4): 5.8.11.14
.. 17 eicosaben citric acid (hereinafter referred to as C!), etc.
本発明において用いる微生物は、ハエカビ目のコニディ
オボラス属に属し、ω3系高度不飽和脂肪酸生産能を有
する微生物である。具体的にはコニディオボラス・ナノ
デス剋匹」違山江巨匹傾■CBS 183/62.コニ
ディオボラス・ランブラウジニス−匹旦悼j譚功亙お」
b吐Q」至)^TCC12585等が挙げられる。The microorganism used in the present invention belongs to the genus Conidiobolus of the order Hyperoptera and has the ability to produce ω3 polyunsaturated fatty acids. Specifically, "Conidiobolus Nanodes vs.""Unlike a giant fish" CBS 183/62. Conidiobolus lamblausinis
Examples include TCC12585.
本発明には上記微生物のほか、これらから誘導される変
異株であって上記のようにω3系高度不飽和脂肪酸を生
産する能力を有するもの等も等しく使用することができ
る。In addition to the above-mentioned microorganisms, mutant strains derived from these microorganisms having the ability to produce ω3-based highly unsaturated fatty acids as described above can also be used in the present invention.
上記微生物を培養するための培地は、該微生物が良く生
育して目的とする脂質を生産しうるちのであればよ(、
炭素源、窒素源、無機塩類および必要に応じて微生物の
生育に好適な微量元素や栄養源を添加することもできる
。炭素源としては、炭水化物や油脂などが用いられ、具
体的にはブドウ糖、大豆油、サフラワー油、アマニ油な
どが挙げられる。また、窒素源としては酵母エキス、ペ
プトン、コーン・ステイープ・リカー、大豆側などの有
機窒素源が好末しい。無機塩類としてはKH2PO4,
Fe5Oa ・711zO,MgSO4・78zO,’
1nsOaなどが用いられる。The medium for culturing the above-mentioned microorganisms may be one that allows the microorganisms to grow well and produce the desired lipids (
A carbon source, a nitrogen source, inorganic salts, and if necessary, trace elements and nutrient sources suitable for the growth of microorganisms can also be added. As the carbon source, carbohydrates, fats and oils, etc. are used, and specific examples include glucose, soybean oil, safflower oil, and linseed oil. In addition, as a nitrogen source, organic nitrogen sources such as yeast extract, peptone, corn staple liquor, and soybean are preferable. Inorganic salts include KH2PO4,
Fe5Oa ・711zO, MgSO4・78zO,'
1 nsOa or the like is used.
本発明では、上記培地にα−リノレン酸またはその誘導
体を含有させることが必要である。α−リノレン酸また
はその誘導体の供給源としては、アマニ油、α−リノレ
ン酸のエチルエステル、αリルン酸ナトリウム塩などが
挙げられるが、そのほかα−リノレン酸を含むものであ
れば用いることができる。α−リノレン酸またはその誘
導体を培地に添加する量は、例えばアマニ油を用いる場
合は0.1〜10容量%、好ましくは3〜5容置%であ
り、その他のものを用いる場合は0.1〜10容量%、
好ましくは2〜5容量%である。In the present invention, it is necessary for the medium to contain α-linolenic acid or a derivative thereof. Sources of α-linolenic acid or its derivatives include linseed oil, ethyl ester of α-linolenic acid, sodium α-linolenic acid, and any other source containing α-linolenic acid can be used. . The amount of α-linolenic acid or its derivative added to the medium is, for example, 0.1 to 10% by volume when using linseed oil, preferably 3 to 5% by volume, and 0.1 to 10% by volume when using other materials. 1 to 10% by volume,
Preferably it is 2 to 5% by volume.
α−リノレン酸またはその誘導体を培地に添加する時期
は、培養を始める前でも培養の途中であってもよいが、
培113日以内に添加することが好ましい。α-Linolenic acid or its derivatives may be added to the medium before or during the culture, but
It is preferable to add it within 113 days of culture.
上記微生物の培養は、通常上記した液体培地で振とう培
養や通気攪拌培養などにより行なわれる。The above-mentioned microorganisms are usually cultured in the above-mentioned liquid medium by shaking culture, aerated stirring culture, or the like.
培養温度は10〜40°C1好ましくは20〜30゛C
で、培養日数は2〜10日、好ましくは3〜5日である
。Culture temperature is 10-40°C, preferably 20-30°C
The number of days of culture is 2 to 10 days, preferably 3 to 5 days.
このようにして培養物中に02゜−3+czosn+c
*。、。In this way, 02°-3+czosn+c was added to the culture.
*. ,.
などを含む脂質が生産されるので、培養物から02゜、
、。Since lipids containing such as
,.
Czoma、Cto、sなどを含む脂質を採取すればよ
い。Lipids containing Czoma, Cto, s, etc. may be collected.
採取にあたっては、C2゜S、、 C,。”4+CZ。When collecting, C2°S,,C,. “4+CZ.
5.などを含む脂質を培養物よりそのまま採取してもよ
いが、培養物には未利用のα−リノレン酸や炭素源とし
て加えた油脂等が含まれるため、培養物より菌体を分離
し、この菌体からC2゜aff+c2゜S6.C2゜、
。5. However, since the culture contains unused α-linolenic acid and fats and oils added as a carbon source, bacterial cells are separated from the culture. C2゜aff+c2゜S6. C2゜,
.
などを含む脂質を採取することが好ましい。該脂質から
02゜−31Cz。−4,C2゜、、などを採取するに
は、溶媒抽出法やクロマトグラフィー法などの常法によ
ればよい。It is preferable to collect lipids containing the following. 02°-31Cz from the lipid. -4, C2°, etc. can be collected by conventional methods such as solvent extraction and chromatography.
C実施例〕 次に、本発明を実施例により説明する。C Example] Next, the present invention will be explained by examples.
実施例1
第1表に示した組成の培地に、炭素限として第2表に示
した所定量のアマニ油(バルミチン酸6%、ステアリン
酸3%、オレイン酸15%、リノール酸IG%、α−リ
ノレン酸60%)を培地l!に対して加えた5種類の培
地を作成した。各培地100dを500d容三角フラス
コに入れ、コニディオボラス・ランブラウジニスATC
C12585を接種し、30°Cで4日間振とう培養し
た。Example 1 A culture medium having the composition shown in Table 1 was added with a predetermined amount of linseed oil (valmitic acid 6%, stearic acid 3%, oleic acid 15%, linoleic acid IG%, α -linolenic acid (60%) in the medium! Five types of culture media were created. Pour 100 d of each medium into a 500 d Erlenmeyer flask, and add Conidiobolus lamblausinis ATC.
C12585 was inoculated and cultured with shaking at 30°C for 4 days.
卯」−表
K HIP 04 1.5 gM
gSOn 0.5gペプトン
10g
イーストエキストラクト 5g
F e SO47H2O0,01g
蒸留水 1!
培養終了後、遠心分離により菌体を集菌し、リン酸緩衝
液(pH7,0)を用いて洗浄して吸引濾過により菌体
を採取した。この菌体をステンレス製のカップに入れ、
グラスビーズ、メタノール、クロロホルムを加えてホモ
ジナイザーで菌体を破砕し、菌体内の脂質を抽出した。Rabbit” - table K HIP 04 1.5 gM
gSOn 0.5g peptone
10g Yeast extract 5g F e SO47H2O0.01g Distilled water 1! After the culture was completed, the bacterial cells were collected by centrifugation, washed with phosphate buffer (pH 7,0), and collected by suction filtration. Put the bacteria into a stainless steel cup,
Glass beads, methanol, and chloroform were added, and the cells were disrupted using a homogenizer, and the lipids inside the cells were extracted.
次いで、抽出した脂質をメチルエステル化して、キャピ
ラリーガスクロマトグラフィー(カラム PE020M
)により脂肪酸組成を調べた。この結果を第2表に示す
。Next, the extracted lipids were methyl esterified and subjected to capillary gas chromatography (column PE020M).
), the fatty acid composition was investigated. The results are shown in Table 2.
表より明らかなように、アマニ油の添加量3容量%で菌
体の収量はほぼ最高に達し、添加量が4容量%および5
容量%でもほぼ変わりがなかった。As is clear from the table, the bacterial cell yield reached almost the maximum when the amount of linseed oil added was 3% by volume, and when the amount of added flaxseed oil was 4% and 5% by volume.
There was almost no difference in capacity %.
C工、、 C2゜。4およびC2゜、、の同定は、以下
の方法により行なった。11−14−17−エイコサト
リエン酸(CZ。、、)および5−8−11−1417
−ニイコサペンクエン酸(C2゜5.)についでは、こ
れらの標品とキャピラリーガスクロマトグラフィー(カ
ラム PE020M)においてリテンションタイムが一
致した。また、標品と菌体から抽出した脂質のメチルエ
ステル化物を混合してキャピラリーガスクロマトグラフ
ィーで分析したところ、C2゜、、およびC2゜、、の
画分のピークが大きくなった。一方、硝酸銀含浸薄層ク
ロマトグラフィーによりトリエン画分、テトラエン画分
およびペンタエン画分を分離した。トリエン画分にはジ
−ホモ−T−リノレン酸、C2゜、3.γ−リノレン酸
久−リノレン酸が含まれていた。テトラ
ラエン画分には6−9−12−15−オクタデカテトラ
エン酸、アラキドン酸、 Czo−4が含まれていた
。ペンタエン画分にはC2゜8.が含まれていた。C engineering, C2゜. 4 and C2°, were identified by the following method. 11-14-17-eicosatrienoic acid (CZ., ) and 5-8-11-1417
-Nicosapene citric acid (C2°5.) had the same retention time as these standards in capillary gas chromatography (column PE020M). Furthermore, when the sample and the methyl ester of lipid extracted from bacterial cells were mixed and analyzed by capillary gas chromatography, the peaks of the C2°, , and C2° fractions became large. On the other hand, a triene fraction, a tetraene fraction, and a pentaene fraction were separated by thin layer chromatography impregnated with silver nitrate. The triene fraction contains di-homo-T-linolenic acid, C2°, 3. γ-linolenic acid Contains γ-linolenic acid. The tetralaene fraction contained 6-9-12-15-octadecatetraenoic acid, arachidonic acid, and Czo-4. The pentaene fraction contains C2°8. was included.
これらの両分のメチルエステル化物をキャピラリーガス
クロマトグラフィーにより、各々の脂肪酸に分離し、次
いでピコリニル誘導体化し、キャピラリーガスマススペ
クトラムにより同定した。この結果、C2゜、、は11
−14−17−エイコサトリエン酸、C2゜84は8−
11−14−17−ニイコサテトラエン酸、C2゜8.
は5−8−11−1417−ニイコサペンクエン酸であ
ると同定した。Both of these methyl esterified products were separated into their respective fatty acids by capillary gas chromatography, then picolinyl derivatized, and identified by capillary gas mass spectra. As a result, C2°,, is 11
-14-17-eicosatrienoic acid, C2゜84 is 8-
11-14-17-nicosatetraenoic acid, C2°8.
was identified as 5-8-11-1417-nicosapencitric acid.
比較例1
第1表に示した組成の培地に、炭素源としてグルコース
30 g/l、を加えた培地を作成した。この培地10
0dを500 ml容三角フラスコに入れ、コニディオ
ボラス・ランブラウジニス^TCC12585を接種し
、30°Cで3日間振とう培養した。Comparative Example 1 A medium was prepared by adding 30 g/l of glucose as a carbon source to a medium having the composition shown in Table 1. This medium 10
0d was placed in a 500 ml Erlenmeyer flask, inoculated with Conidiobolus lamblausinis^TCC12585, and cultured with shaking at 30°C for 3 days.
培養終了後、実施例1と同様の方法にて菌体内の脂質の
分析を行なったところ、菌体収量は19g/1.油脂含
量は3.8g/lであり、C2゜、、。After the culture was completed, the lipids in the bacterial cells were analyzed in the same manner as in Example 1, and the bacterial cell yield was 19 g/1. The oil content is 3.8g/l, and the temperature is C2°.
czo−4* c、。、、は検出されなかった。czo-4*c,. , were not detected.
実施例2
第1表に示した組成の培地に、炭素源としてグルコース
30 g/j2を加えた培地を作成した。この培地1.
00 mlを500 mll正三角フラスコ入れ、コニ
ディオボラス・ランブラウジニスATCC12585を
接種し、30“Cで2日間振とう培養した。2日間の培
養後、アマニ油を培地II!、あたり1容量%となるよ
うに加えて、さらに2日間振とう培養した。Example 2 A medium was prepared by adding 30 g/j2 of glucose as a carbon source to a medium having the composition shown in Table 1. This medium 1.
00 ml was placed in a 500 ml regular Erlenmeyer flask, Conidiobolus lamblausinis ATCC 12585 was inoculated, and cultured with shaking at 30"C for 2 days. After 2 days of culture, linseed oil was added to medium II! to give a concentration of 1% by volume. The cells were added in the same manner as above, and cultured with shaking for an additional 2 days.
培養終了後、実施例工と同様の方法で菌体内の脂質の分
析を行なったところ、C2゜53が0.85g/l、
Czo−mが0.09 g/ i!、 Czo−sが0
.45g/I!、の収量で得られた。After the cultivation was completed, the lipids in the bacterial cells were analyzed in the same manner as in the example, and the C2゜53 was 0.85 g/l.
Czo-m is 0.09 g/i! , Czo-s is 0
.. 45g/I! , was obtained with a yield of .
実施例3
第1表に示した組成の培地に、第3表に示した所定量の
グルコースとアマニ油を加えた6種類の培地を作成した
。各培地100 mを500d容三角フラスコに入れ、
コニディオボラス・ランブラウジニスATCC1258
5を接種し、30℃で4日間振とう培養した。Example 3 Six types of culture media were prepared by adding predetermined amounts of glucose and linseed oil shown in Table 3 to the culture medium having the composition shown in Table 1. Put 100 m of each medium into a 500 d Erlenmeyer flask,
Conidiobolus lamblausinis ATCC1258
5 was inoculated and cultured with shaking at 30°C for 4 days.
培養終了後、実施例1と同様の方法で菌体内の脂質の分
析をした。この結果を第3表に示す。After the cultivation was completed, lipids within the bacterial cells were analyzed in the same manner as in Example 1. The results are shown in Table 3.
実施例4
第1表に示した組成の培地に、炭素源としてアマニ油を
培地11あたり3容量%となるように加えた培地を作成
した。この培地100成を500威容三角フラスコに入
れたものを2つ作り、各々に第4表に示したコニディオ
ボラス属に属する菌を接種し、30″Cで4日間振とう
培養した。この結果を第4表に示す。Example 4 A medium was prepared by adding linseed oil as a carbon source to a medium having the composition shown in Table 1 in an amount of 3% by volume per medium 11. Two 500-capacity Erlenmeyer flasks containing 100 volumes of this medium were prepared, and each was inoculated with the bacteria belonging to the genus Conidiobolus shown in Table 4, and cultured with shaking at 30"C for 4 days. Results. are shown in Table 4.
/ / / して有用なものである。/ / / It is useful.
Claims (2)
肪酸生産能を有する微生物をα−リノレン酸またはその
誘導体を含む培地に培養し、培養物からω3系高度不飽
和脂肪酸含有脂質を採取することを特徴とするω3系高
度不飽和脂肪酸含有脂質の製造法。(1) Cultivate a microorganism belonging to the genus Conidiobolus and capable of producing ω3 highly unsaturated fatty acids in a medium containing α-linolenic acid or its derivatives, and collect lipids containing ω3 highly unsaturated fatty acids from the culture. A method for producing a lipid containing omega-3 highly unsaturated fatty acids.
主成分とするものである請求項1記載の製造法。(2) The production method according to claim 1, wherein the ω3 highly unsaturated fatty acid contains eicosatrienoic acid as a main component.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1019739A JPH02200193A (en) | 1989-01-31 | 1989-01-31 | Production of omega3 based highly unsaturated fatty acid-containing lipid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1019739A JPH02200193A (en) | 1989-01-31 | 1989-01-31 | Production of omega3 based highly unsaturated fatty acid-containing lipid |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02200193A true JPH02200193A (en) | 1990-08-08 |
Family
ID=12007707
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1019739A Pending JPH02200193A (en) | 1989-01-31 | 1989-01-31 | Production of omega3 based highly unsaturated fatty acid-containing lipid |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02200193A (en) |
-
1989
- 1989-01-31 JP JP1019739A patent/JPH02200193A/en active Pending
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP3354582B2 (en) | Method for producing omega-9 polyunsaturated fatty acid and lipid containing the same | |
JP2007503802A (en) | Method for increasing the yield of marine microbial biomass and / or components of the biomass | |
JPH0418838B2 (en) | ||
JPH0734752B2 (en) | Method for producing arachidonic acid and lipid containing the same | |
EP1606413B1 (en) | A method for enhancing levels of polyunsaturated fatty acids in thraustochytrid protists | |
JP3995290B2 (en) | Method for producing omega-9 polyunsaturated fatty acid and lipid containing the same | |
JP2006521814A (en) | Method for increasing the level of polyunsaturated fatty acids in Thraustochytrid protists | |
JPH01199588A (en) | Production of highly unsaturated aliphatic acid with filamentous fungus | |
JPH02200193A (en) | Production of omega3 based highly unsaturated fatty acid-containing lipid | |
JPH01228486A (en) | Highly unsaturated fatty acid having chain of odd carbon number and production of lipid containing said acid | |
JP2740854B2 (en) | Process for producing dihomo-γ-linolenic acid and inhibitor for fatty acid Δ5 desaturation reaction | |
JPH0223878A (en) | Production of highly unsaturated fatty acid and lipid containing said acid | |
JPH0712315B2 (en) | Eicosapentaenoic acid and method for producing lipid containing the same | |
JPH03272692A (en) | New highly unsaturated fatty acid and production of same fatty acid or lipid containing same fatty acid | |
JP4079494B2 (en) | Method for producing arachidonic acid and / or eicosapentaenoic acid-containing fats and oils | |
EP0304049A2 (en) | Method for the production of lipids containing bis-homo-linolenic acid | |
JPH01304892A (en) | Production of highly unsaturated fatty acid enriched fats and oils | |
JPH0216989A (en) | Production of omega6-based unsaturated fatty acid-containing phospholipid | |
JP2958361B2 (en) | Process for producing dihomo-γ-linolenic acid and inhibitor for △ 5-unsaturation reaction of fatty acid | |
JPH08163990A (en) | Oil-and-fat-containing alga and production of oil-and-fat derived therefrom | |
JPS639835B2 (en) | ||
JP4045403B2 (en) | Method for producing hydroxy fatty acid and γ-lactone | |
JPH0965871A (en) | Culture of maritime fine algae | |
JPH0722513B2 (en) | Bishomo-γ-linolenic acid and method for producing lipid containing the same | |
RU1822411C (en) | Process for preparing ethyl fatty acid esters |