JPS60259192A - Production of microbial lipid - Google Patents

Production of microbial lipid

Info

Publication number
JPS60259192A
JPS60259192A JP59115162A JP11516284A JPS60259192A JP S60259192 A JPS60259192 A JP S60259192A JP 59115162 A JP59115162 A JP 59115162A JP 11516284 A JP11516284 A JP 11516284A JP S60259192 A JPS60259192 A JP S60259192A
Authority
JP
Japan
Prior art keywords
lipid
lipids
medium
culture
mortierella
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
JP59115162A
Other languages
Japanese (ja)
Other versions
JPS6251110B2 (en
Inventor
Osamu Suzuki
修 鈴木
Toshihiro Yokochi
俊弘 横地
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.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP59115162A priority Critical patent/JPS60259192A/en
Priority to DE8484306511T priority patent/DE3470061D1/en
Priority to EP84306511A priority patent/EP0155420B1/en
Priority to CA000473158A priority patent/CA1235083A/en
Publication of JPS60259192A publication Critical patent/JPS60259192A/en
Priority to US06/929,601 priority patent/US4783408A/en
Publication of JPS6251110B2 publication Critical patent/JPS6251110B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To increase the amounts of lipid with a high unsaturated fatty acid content and microbial cells and obtain the titled lipid by cultivating a microorganism, e.g. Mortierella isabellina, etc. in a culture medium containing acetic acid (salt) added thereto and a carbohydrate as a carbon source. CONSTITUTION:A strain, e.g. Mortierella isabellina (IFO 7824), Mortierella vinacea (IFO 6738), Mortierella nana (IFO 8794), Mortierella ramanniana (IFO 8287) or Mortierella ramanniana var. anglispora (IFO 8187), is cultivated in a culture medium containing acetic acid (salt) added thereto in an amount of e.g. 0.1-20g/ ladded thereto and a carbohydrate, e.g. glucose, as a carbon source, preferably at 3.0-6.0pH, and the aimed lipid is obtained from the resultant microbial cells.

Description

【発明の詳細な説明】 本発明はモルテイエレラ属に属するイサベリナ、ビナセ
ア、ナナ、ラマニアナ、ラマニアナ・アングリスポラの
菌株を炭水化物を炭素源とする培地に培養し脂質含量の
高い菌体を培地中に増殖するのに際して培地に酢酸ある
いは酢酸塩を加えることにより、菌体の増殖量及び菌体
中の脂質含量の(油脂など)、極性脂質(リン脂質、糖
脂質など)〕2採取する生産性の高い脂質の生産方法に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention involves culturing strains of Isabelina, Vinacea, Nana, Lamaniana, and Lamaniana anglispora belonging to the genus Morteierella in a medium containing carbohydrates as a carbon source, and growing bacterial cells with a high lipid content in the medium. By adding acetic acid or acetate to the culture medium during the process, the amount of bacterial growth, the lipid content in the bacterial cells (oil, fat, etc.), polar lipids (phospholipids, glycolipids, etc.)] 2. Highly productive lipids to be collected This relates to the production method.

本発明者らは既にモルテイエレラ属に属するイサベリナ
、ビナセア、ナナ、ラマニアナ・アングリスポラの糸状
菌菌株が高濃度Y炭水化物を炭素源とする培地に培養す
ることにより脂質含酸の高い菌体が培地中に高密度の製
造されること並びにその菌体より脂質を採取することに
よる生産性高く脂質が製造されることを見出した。捷だ
、同じくモルテイエレラ属に属する同種の糸状菌菌株が
高濃度の炭水化物を炭素源とした培地において培養され
た場合、γ−リルン酸含有脂質の高含計画体が高密度に
生産され、培養菌体よ!l) r −’Jルン酸含有脂
質あるいはγ−リルン酸が生産性高く製造されることを
見出した。
The present inventors have already cultivated filamentous fungal strains of Isabelina, Vinacea, Nana, and Lamaniana angrispora belonging to the genus Morteierella in a medium containing a high concentration of Y-carbohydrate as a carbon source. It has been found that lipids can be produced at high density and with high productivity by collecting lipids from the bacterial cells. However, when a filamentous fungal strain of the same species, also belonging to the genus Morteierella, is cultured in a medium with a high concentration of carbohydrate as a carbon source, a high concentration of γ-lylunic acid-containing lipids is produced at high density, and the cultured bacteria Body! l) It has been found that r-'J phosphoric acid-containing lipids or γ-phosphoric acid can be produced with high productivity.

以上の発明はそれぞれ動、植物に代わる微生物(糸状菌
)による脂質(油脂など)の生産に関するものであり、
後者の場合特につきみ阜(0θnotb−リルン酸ある
いはその含有脂質の製造方法に代るものである。
The above inventions each relate to the production of lipids (oils and fats, etc.) by microorganisms (filamentous fungi) in place of animals and plants.
In the latter case, it is particularly an alternative to the method for producing 0θnotb-lyrinnic acid or its containing lipids.

本発明者らは更にモルテイエレラ属に属するイサベリナ
、ビナセア、ナナ、ラマニアナ、ラマニアナ・アングリ
スポラの糸状菌菌株を炭水化物を炭素源とする培地に培
養して得られた菌体から脂質を採取する脂質の製造に際
して、培地に添加物あるいは補助炭素源として酢酸ある
いは酢酸塩を加えることにより、同じ培養条件下で加え
ない場合よりも乾燥菌体中に占める脂質の含量が10〜
300%増加し、しかも菌体増殖量の増加が同時に認め
られるため、脂質の生産性が著しく高くなる1/ルン酸
を含めた全不飽和脂肪酸の脂肪時に占める含、I¥iが
3〜18チ増加することを見出し、本発明は完成するに
至った。すなわち、本発明はモルテイエレラ属に属する
イサベリナ、ビナセア、ナナ、ラマニアナ、ラマニアナ
・アングリスポラの菌株を炭水化物を炭素源とする培地
に培養し、1旨質含量の高い菌体を培地中に増殖するに
隙して、培地に酢酸あるいは酢酸塩を加えることにより
、菌体の増殖量及び菌体中の脂質含量の大幅な増加を図
り、その菌体より脂質〔中性脂質(油脂など)極性脂質
(リン脂質、糖脂質など)〕を採取する生産性の高い脂
質の生産方法である。
The present inventors further cultivated filamentous fungal strains of Isabelina, Vinacea, Nana, Lamaniana, and Lamaniana anglispora belonging to the genus Morteierella in a medium containing carbohydrates as a carbon source, and produced lipids by collecting lipids from the cells obtained. By adding acetic acid or acetate to the culture medium as an additive or auxiliary carbon source, the content of lipids in dried bacterial cells can be increased by 10 to 10% compared to when no acetic acid is added under the same culture conditions.
300% increase, and at the same time an increase in the amount of bacterial cell proliferation is observed, resulting in a markedly higher lipid productivity. The present invention has been completed based on the discovery that the That is, the present invention involves culturing strains of Isabelina, Vinacea, Nana, Lamaniana, and Lamaniana angrispora belonging to the genus Morteierella in a medium containing carbohydrates as a carbon source, and cultivating bacteria with a high content of one substance in the medium. By adding acetic acid or acetate to the medium, we aim to significantly increase the growth rate of bacterial cells and the lipid content in the bacterial cells. This is a highly productive lipid production method that collects lipids, glycolipids, etc.).

本発明で用いる使用菌はモルテイエレラ(Mort−i
erella )属のイサベリナ(1sabellin
a ) (I FO7824;7884,7873,8
183.8309)ビナセア(Vinacea ) (
I P’06738 )、ナナ(nana ) (TF
O8794)、ラマ= 7 f (ramaniana
 ) (IFO8287)、ラマニアナ・アングリスポ
ラ(ramani−ana var、 anglisp
ora ) (IFO8187)の各種菌株である。な
お、上記した菌はいずれも財団法人発酵研究所に保存さ
れ、■FOカタログ(菌株目録)に記載されている糸状
菌である。
The bacteria used in the present invention are Morteiherella (Mort-i
erella ) genus Isabellina
a) (I FO7824;7884,7873,8
183.8309) Vinacea (
I P'06738), Nana (TF
O8794), Rama = 7 f (ramaniana
) (IFO8287), Ramani-ana var, anglisp
ora) (IFO8187). All of the above-mentioned bacteria are filamentous bacteria stored at the Fermentation Research Institute and listed in the ■FO Catalog (Bacterial Strain Catalog).

上記の糸状菌を培養する培地の炭素源である炭水化物と
しては、たとえばグルコース、フラクトース、サッカロ
ース、糖蜜、デン粉、木材糖化液などが用いられる。炭
水化物は培地】l中に20〜400g用いられるのが好
ましい。また窒素源としては、例えば硝酸アンモニウム
、硫酸アンモニウム、塩化アンモニウム、リン酸アンモ
ニウムナトの様々無機窒素源、または尿素、ペプトン、
酵母エキス、コーン・スチーブ・リカーなど有機窒素源
が用いられる。無機塩としては、例えばKH2PO4に
2HPO4,NaCl、 FeSO4,7+(20、M
gSO4−7H20、ZnSO4・71−120などが
用いられる。その他必安に応じて微量要素、その他の栄
養源を添加する。
Examples of carbohydrates used as carbon sources for the medium for culturing the filamentous fungi include glucose, fructose, saccharose, molasses, starch, and wood saccharification liquor. The carbohydrate is preferably used in an amount of 20 to 400 g per liter of culture medium. Examples of nitrogen sources include various inorganic nitrogen sources such as ammonium nitrate, ammonium sulfate, ammonium chloride, and ammonium phosphate, or urea, peptone,
Organic nitrogen sources such as yeast extract and corn/steve liquor are used. Examples of inorganic salts include KH2PO4, 2HPO4, NaCl, FeSO4,7+ (20, M
gSO4-7H20, ZnSO4.71-120, etc. are used. Add trace elements and other nutritional sources as needed.

上記糸状菌の培養は通常液体培地で、振とう培養、通気
攪拌培養などにより行われる。培地のpHは30〜60
が良く、通常2日〜10日間位培養が行われる。史に、
培養の初期すなわち初期培地に、また通気攪拌培養の場
合では前培養培地に、あるいは培養の中間段階で酢酸あ
るいは酢酸塩(ナトリウム塩、カリウム塩などのアルカ
リ金属塩)を炭素源濃度など培養条件に応じて0.1〜
20ji/l培地の割合で加えることにより菌体の培養
が行われる。かくして、培養物中にγ−リルン酸など不
飽和脂肪酸含量が高い脂質の高含量菌体が生産性i自り
生産されるので、培養物より菌体を分離し、脂質が糸状
菌菌体中に含まれるので、この菌体よりγ−リルン酸な
ど不飽和脂肪酸含量の高い脂質を採取するのが好適であ
る。培養物より菌体の分離に当っては菌糸があまりのび
ず極めて小単位(1〜10細胞)で培養されており、従
って、例えば遠心脱水器などにより極めて容易に分離さ
れ、乾燥度の高い菌体(含水率約60係)になる利点を
有することが明らかになった。γ−リルン酸など不飽和
脂肪酸含量の高い脂質の採取は常法によって溶媒抽出な
どにより行われる。
The above-mentioned filamentous fungi are usually cultured in a liquid medium by shaking culture, aerated agitation culture, or the like. The pH of the medium is 30-60
The culture is usually carried out for about 2 to 10 days. In history,
Add acetic acid or acetate (alkali metal salts such as sodium salts and potassium salts) to the culture conditions such as carbon source concentration in the initial stage of culture, in the preculture medium in the case of aerated agitation culture, or in the intermediate stage of culture. 0.1~ depending
The bacterial cells are cultured by adding 20 ji/l of the medium. In this way, bacterial cells with a high content of lipids with a high content of unsaturated fatty acids such as γ-lylunic acid are produced by themselves in the culture. Therefore, it is preferable to collect lipids with a high content of unsaturated fatty acids such as γ-lylunic acid from the bacterial cells. When separating bacterial cells from a culture, the hyphae do not spread very much and are cultured in extremely small units (1 to 10 cells). It has become clear that this product has the advantage of reducing the water content (water content of about 60%). Lipids with a high content of unsaturated fatty acids such as γ-lylunic acid are collected by conventional methods such as solvent extraction.

かくして、本発明によればr−リルン酸などの不飽和脂
肪酸含量が高い脂質を生産性高く製造することができ、
本発明はr−’)ルン酸含有脂質の製造法あるいけ脂質
の改質方法として優れたものである。本発明は、特に現
在植物種子から採取されているr −+)ルン酸含有脂
質の生産方法としてすぐれたものである。! なお、γ−リルン酸(18:3 (6,9,12))は
リノール酸と共に哺乳動物では体内で合成することので
きない、食飼として要求される脂肪酸(必須脂肪酸)で
ある。これはγ−リルン酸が体内でビスホモ−r−リル
ン酸となり、さらにはアラキドン酸となる前駆体である
こと、ビスホモ−γ−リルン酸、アラキドン酸はそれぞ
れプロスタグランジン、El + Fl cl及びF2
 + F2.tとなり生体中で極めて重要な生理的な役
割をはたしているからである。従って、γ−リルン酸含
有脂質は医薬品などとして利用できるものであることは
明らかである。
Thus, according to the present invention, lipids with a high content of unsaturated fatty acids such as r-lylunic acid can be produced with high productivity,
The present invention is excellent as a method for producing r-') phosphoric acid-containing lipids and a method for modifying fish lipids. The present invention is particularly excellent as a method for producing r-+) phosphoric acid-containing lipids, which are currently collected from plant seeds. ! Incidentally, γ-lylinic acid (18:3 (6,9,12)) is a fatty acid (essential fatty acid) that cannot be synthesized in the body of mammals and is required as a feed, along with linoleic acid. This is because γ-lylphinic acid is a precursor that becomes bishomo-r-lyllunic acid in the body and then arachidonic acid, and bishomo-γ-lylinic acid and arachidonic acid are respectively prostaglandins, El + Fl cl, and F2.
+F2. This is because it plays an extremely important physiological role in living organisms. Therefore, it is clear that γ-lylunic acid-containing lipids can be used as pharmaceuticals.

次に本発明の実施例を示すが、本発明はこれにより制限
を受けるものではない。
Next, examples of the present invention will be shown, but the present invention is not limited thereto.

実施例1゜ グルコース309 、 KH2PO42、!i’ 、 
MgSO3・7Hρ0.3g、NaC10,1g、Fe
SO4,7H7H2O10、CaCl22H20LoI
niiiI、 Cu5O,−5H200,2Tn9、Z
nSO4・7H201、Orng、M n C12・4
H201,Om?、’I”hiamine−HCIJ2
rng、D−Biotin O,o 2 mg ト窒素
源として(NH4)28043g、(C/N比(グルコ
ース中の炭素原子重量/窒素源中の窒素原子重量)は2
.2.2)を脱イオン水10100Oに混合し、p)(
を4.6に調整した合成培地を基準として酢酸あるいは
酢酸塩(ナトリウム塩、カリウム塩)を所定量加えて培
地を作成した。この合成培地400m1を11の三角フ
ラスコに入れ、それぞれ菌株を接種し、培養温度30°
Cで7日間150 rl;1mで振とり培養を行った。
Example 1゜Glucose 309, KH2PO42,! i',
MgSO3・7Hρ0.3g, NaC10.1g, Fe
SO4,7H7H2O10, CaCl22H20LoI
niiiI, Cu5O,-5H200,2Tn9,Z
nSO4・7H201, Orng, M n C12・4
H201, Om? ,'I”hiamine-HCIJ2
rng, D-Biotin O,o 2 mg as a nitrogen source (NH4) 28043 g, (C/N ratio (carbon atom weight in glucose/nitrogen atom weight in nitrogen source) is 2
.. 2.2) was mixed with 10100O of deionized water, p)(
A medium was prepared by adding a predetermined amount of acetic acid or acetate (sodium salt, potassium salt) based on a synthetic medium adjusted to 4.6. Pour 400ml of this synthetic medium into 11 Erlenmeyer flasks, inoculate each with the bacterial strain, and culture at 30°C.
Shaking culture was performed at 150 rl; 1 m for 7 days at C.

培養後、口過法あるいは遠心分離法で菌体を集めた。そ
の一部を含水率の定量の為、精秤し、恒温槽中120°
Cで−・膠液乾燥し、含水率をめ、残りの菌体について
脂質の抽出を行った。菌体からの脂質の抽出は、残りの
湿菌体にクロロホルム−メタノール(2:IV / V
 )混液を加え、ガラスピーズ存在下にホモジナイズす
ることにより菌体の破砕と脂質の抽出を同時に行った。
After culturing, the bacterial cells were collected by the mouth filtration method or centrifugation method. A part of it was accurately weighed to determine the moisture content and placed in a constant temperature bath at 120°.
The glue solution was dried at C, the water content was determined, and the remaining bacterial cells were extracted for lipids. Extraction of lipids from bacterial cells was performed by adding chloroform-methanol (2:IV/V) to the remaining wet bacterial cells.
) was added and homogenized in the presence of glass peas to simultaneously crush the bacterial cells and extract the lipids.

なお、抽出を完全に行うため、これを5回繰返し全抽出
液を集めた。上記抽出液をii”olchの分配洗浄法
によ゛り精製した後、溶媒を減圧留去し重量法で全脂質
を測定した。得られた脂質について常法によりメチルエ
ステル化した後、ガスクロマトグラフィーを行い脂肪酸
組成をめた。このような方法で各種モルテイエレラ属糸
状菌について酢酸今るいは酢酸塩(f、トリウム塙カリ
ウム塩)を添加した場合00しない場合汁d菌体増殖量
及び脂肪酸組成の変化について断聾結果を表−1に示し
た。
In order to perform the extraction completely, this was repeated five times and all the extracts were collected. After the above extract was purified by the partition washing method of II'olch, the solvent was distilled off under reduced pressure and the total lipids were measured by gravimetric method. Using this method, when acetic acid or acetate salt (f, thorium Hanawa potassium salt) was added to various types of Morteierella filamentous fungi, the amount of bacterial cell growth and fatty acid composition Table 1 shows the results regarding changes in deafness.

表−1の結果から、同じ菌株について、酢酸あるいは酢
酸塩(ナトリウム塩、カリウム塩)を添加した場合に添
加しない場合よりも常に菌体増殖量が高く、多くの場合
2倍以上の値が得られていることが分る。そのことは脂
質生成量に関して、更に顕著に表れており、15〜6倍
に増加していた。脂質含量においては、あまり変化が認
められ′ない場合もあるが、多くの場合10〜20係含
量が大きくなっていることが認められた。これらの事実
はグルコース100.9の消費に対して出来る菌体ii
f1g)及び脂質量(I)で表わした菌体係数及び脂質
係数がそれぞれ酢酸あるいは酢酸塩を添加しない場合と
比べて大幅に増加しており、この系に −おいて脂質及
び菌体の生産性が著しく高くなることが明らかになった
From the results in Table 1, for the same strain, when acetic acid or acetate salts (sodium salt, potassium salt) are added, the bacterial cell growth rate is always higher than when it is not added, and in many cases more than twice the value is obtained. I can see that it is being done. This was even more evident with regard to the amount of lipid production, which increased 15 to 6 times. Although in some cases the lipid content did not change much, in many cases it was observed that the 10-20 content increased. These facts indicate that bacterial cells formed in response to the consumption of glucose 100.9
The bacterial cell coefficient and lipid coefficient expressed as f1g) and lipid content (I) were significantly increased compared to the case where acetic acid or acetate was not added, respectively, and the productivity of lipids and bacterial cells was significantly increased in this system. was found to be significantly higher.

又、脂肪酸組成としてγ−リルン酸の含量カ酢醸あるい
は酢酸塩(ナトリウム塩、カリウム塩)を添加すること
により増加しており、全不飽和脂肪酸において1.7〜
201%の増加が認められた。
In addition, the fatty acid composition increases by adding vinegar or acetate (sodium salt, potassium salt), and the content of γ-lylunic acid increases from 1.7 to 1.7 in total unsaturated fatty acids.
An increase of 201% was observed.

1個の脂肪酸に対する不飽和結合の数を示す不飽和系数
もかなり大きく増加していることから、不飽和脂肪酸の
増加と同時に、不飽和脂肪酸の亮進 不飽和が起っていることが明らかである。こqとは酢酸
あるいは酢酸塩の添加がその生成指軍おいて高度不飽和
酸であるγ−リルン酸を含む不飽和脂肪酸含情苔増加さ
せると言う意味における脂質の改質に効果を及ぼしてい
ることが確認さオする。
The unsaturated number, which indicates the number of unsaturated bonds in one fatty acid, also increased considerably, so it is clear that the increasing unsaturation of unsaturated fatty acids is occurring at the same time as the increase in unsaturated fatty acids. be. Koq has an effect on lipid modification in the sense that the addition of acetic acid or acetate increases the amount of unsaturated fatty acids containing γ-lylunic acid, a highly unsaturated acid, in its production direction. That is confirmed.

A7824 −−4.35 2.01 〃 HM要ナナトリウム 5 8,83 4.38# 
7873 − − 5.54 2.19酢酸ナトリウム
 5 9,95 5.72〃 7884 −− − 5
.55 2.2]〃 酢酸すl・リウム 5 ’7,0
8 4.04〃 酢酸カリウム 5 6,30 3.8
4〃 酢酸 1 7,30 3.15 # 8183−−− 9.08 3.37〃 酢酸ナト
リウム 5 9.98 4.65#8309 − − 
5.25 1.30〃 酢酸ナトリウム 5 10,9
0 6.038 6738 、− −− 5.03 1
.85〃 酢酸ナトリウム 5 10,10 5.19
C8794−−4,522,33 〃 酢酸ナトリウム 5 9,15 4.421) 8
287 −−3.65 1.49〃 酢酸ナトリウム 
5 5,20 2.75r> 8187 − − − 
3.80 0.71〃 酢酸ナトリウム 5 8,33
 4.31表 −1 45,86,714,68,071!1 1.0349
.6 14,6 29,5 10,7 75.1 1.
0740.2 7.3 ] 8.2 4,7 63.’
、) (1,8457,5]9,1 33.2 6,7
 65.0 +、1(139,97,418,5305
9,0(1,7556,913,523,64,267
41(1,886+、3 12,8 21.0 4.2
 ()9.8 0.8942.8 10,5 21.9
 4,0 64.:(08537,211,230,3
4,2646(18246,615533,27973
710024,7’ 4,3 17.5 5,6 68
.4 041:(55,320,136,310,(1
88,51,:(i)36.8 6.2 ] 6.8 
3.2 5 G、3 0.6751.4 17,3 3
3.7 3,6 64.5 0.8:(51,37,8
15,15358,+ 0.7848.3 14,8 
30.5 6.1 7+、9(]イ)540.9 5,
0 12.2 5,8 64.6 0.8+52.9 
9,2 17.3 7,4 68.0 0.9618.
8 2,4 12.7 9.1 6]、7 f)、82
51.8 14,4 27.7 9,2 77.8 1
.00なお、表−1において、八け、モルテイエレライ
サベリナ(11ortiere11a 1sabe]、
]、ina ) 、13は、モルテイエレラビナセア(
Mortierella vinacea )、Cは、
モルテイエレラナナ(Mortierellanana
 )、Dは、モルテイエレララ=ンニアナ(’Mort
j、erellaramaniana )及びEは、モ
ルテイエレララマニア埴− グルコースを示し、不飽和係数は脂肪酸1個に〜誦( する不飽和結合の平均個数を示す。
A7824 --4.35 2.01 HM sodium sodium 5 8,83 4.38#
7873 - - 5.54 2.19 Sodium acetate 5 9,95 5.72 7884 - - 5
.. 55 2.2]〃 Sourium acetate 5 '7,0
8 4.04〃 Potassium acetate 5 6,30 3.8
4〃 Acetic acid 1 7,30 3.15 #8183 --- 9.08 3.37〃 Sodium acetate 5 9.98 4.65 #8309 ---
5.25 1.30 Sodium acetate 5 10,9
0 6.038 6738, - -- 5.03 1
.. 85 Sodium acetate 5 10,10 5.19
C8794--4,522,33 Sodium acetate 5 9,15 4.421) 8
287 --3.65 1.49 Sodium acetate
5 5,20 2.75r> 8187 - - -
3.80 0.71 Sodium acetate 5 8,33
4.31 Table -1 45,86,714,68,071!1 1.0349
.. 6 14,6 29,5 10,7 75.1 1.
0740.2 7.3 ] 8.2 4,7 63. '
,) (1,8457,5]9,1 33.2 6,7
65.0 +, 1 (139,97,418,5305
9,0(1,7556,913,523,64,267
41 (1,886+, 3 12,8 21.0 4.2
()9.8 0.8942.8 10.5 21.9
4,0 64. :(08537,211,230,3
4,2646 (18246,615533,27973
710024,7' 4,3 17.5 5,6 68
.. 4 041:(55,320,136,310,(1
88,51,: (i) 36.8 6.2 ] 6.8
3.2 5 G, 3 0.6751.4 17,3 3
3.7 3,6 64.5 0.8: (51,37,8
15,15358,+0.7848.3 14,8
30.5 6.1 7+, 9(]i) 540.9 5,
0 12.2 5,8 64.6 0.8+52.9
9,2 17.3 7,4 68.0 0.9618.
8 2,4 12.7 9.1 6], 7 f), 82
51.8 14.4 27.7 9.2 77.8 1
.. 00 In addition, in Table 1, Hake, Morteierreisaberina (11ortiere11a 1sabe),
], ina ), 13 is Morteierella lavinacea (
Mortierella vinacea), C is
Mortierellanana
), D is 'Mort
J, erellaramaniana) and E indicate molten glucose, and the unsaturation coefficient indicates the average number of unsaturated bonds in one fatty acid.

実施例2 グルコース60g、KH2PO42g、M、!9S04
・7I]200.3g、NaC10,1,g、−i’ 
fivト・エキス 0.2g、イースト・エキス 0.
2g、ペプトン0.1g、FeSO4・7 H2O10
mg、Caclz H2I42010 ”f/、cus
o4・5H2゜0.2m9、Mn504−41−1□0
1.0 ”9ト9.素源トL、”’C尿1t((NII
2)2CO)及び硫酸アンモニウム((NH4)zSO
4)をC/N比(炭素源中の炭素原子重量/窒素源中の
窒素原子重量)を約60になるように加え、脱イオン水
10100O[混合mfr嬉抽を禁漁用で岸査源である
炭水化物(グルコース)の濃度を増加させた場合、その
濃度に応じて培地成分を増加して、また窒素源を尿素な
どに変えた場合は同じC/N比になるように培地を調整
した。
Example 2 Glucose 60g, KH2PO42g, M! 9S04
・7I] 200.3g, NaC10,1,g, -i'
Fivto extract 0.2g, yeast extract 0.
2g, peptone 0.1g, FeSO4.7 H2O10
mg, Caclz H2I42010”f/, cus
o4・5H2゜0.2m9, Mn504-41-1□0
1.0 9.9.
2) 2CO) and ammonium sulfate ((NH4)zSO
4) was added so that the C/N ratio (weight of carbon atoms in the carbon source/weight of nitrogen atoms in the nitrogen source) was approximately 60, and 10,100 O of deionized water [mixed mfr happy extract was used for prohibited fishing at a shore inspection source]. When the concentration of a certain carbohydrate (glucose) was increased, the medium components were increased accordingly, and when the nitrogen source was changed to urea, etc., the medium was adjusted to maintain the same C/N ratio.

この培地を101の培養槽で培養する場合には61.3
01の培養槽でけ201仕込み、それぞれ菌株を接種し
、30°Cの培養温度で所定の時間、通気量0.5〜2
.OVVmで300〜700rpmで攪拌して培養を行
った。培養後遠心分離法で菌体を集めた。また、菌体の
増殖量、脂質生成量及び培地中の炭水化物濃度の測定を
行うため、培養の中間段階において所定の時間毎に10
0mtずつ試料の採取を行い、口過法により菌体と培地
の分離を行った。
When culturing this medium in 101 culture tanks, 61.3
Prepare 201 in a culture tank of 01, inoculate each strain, and incubate at a culture temperature of 30°C for a predetermined time with an aeration rate of 0.5 to 2.
.. Culture was performed using OVVm with stirring at 300 to 700 rpm. After culturing, the bacterial cells were collected by centrifugation. In addition, in order to measure the growth amount of bacterial cells, the amount of lipid production, and the carbohydrate concentration in the medium, 10
A sample of 0 mt was collected, and the bacterial cells and the medium were separated by the mouth filtration method.

分離された菌体からの脂質の抽出、定量は実施例1に従
って行った。菌体を除いた培地については高速液体クロ
マトグラフィーにより炭水化物(グルコース)の濃度を
測定し、濃度が0になった時点で培養を終了した。
Extraction and quantification of lipids from isolated bacterial cells were performed according to Example 1. The concentration of carbohydrate (glucose) in the medium from which the bacterial cells were removed was measured by high performance liquid chromatography, and the culture was terminated when the concentration reached 0.

菌株モルテイエレラ・ラマニアナ・アングリスポラIF
O8187について、グルコースを炭素源として種々の
条件での添加物としての酢酸す) IJウムの添加効果
を調べるため、101及び301培養槽により培養を行
い、菌体増殖量(乾燥重量g/l)、脂質生成量(g/
l)、脂質含量(%)などをめた。
Strain Morteierella lamaniana anglispora IF
O8187 was cultured in 101 and 301 culture vessels using glucose as a carbon source and acetic acid as an additive under various conditions. , lipid production (g/
l), lipid content (%), etc.

その結果を添加条件など含めて表−2に示した。The results are shown in Table 2, including the addition conditions.

表−2において101培養槽を用いた場合、グルコース
濃度約90gの系で酢酸ナトリウムの添加量を0.3〜
ICJjj/lと変えると同時に、添加条件などを変え
て培養を行った結果を無添加の場合と比較して示した。
In Table 2, when 101 culture tank is used, the amount of sodium acetate added is 0.3~
The results of culturing with ICJjj/l and at the same time changing the addition conditions are shown in comparison with the case without addition.

酢酸ナトリウムを添加した場合は添加条件によらず特に
脂質生成量及び脂質含量の大幅な増加が認められる。こ
のことは炭素源であるグルコース100 、!9に対す
る脂質の生成量である脂質系数が無添加の場合と比較し
て大きく増加していることからも分る。菌体の増殖量も
無添加の場合よりも一般的に大きくはなっているが幾分
ばらつきが認められた。3M培養槽を用いてのグルコー
ス濃度約2o1/13と高濃度炭素源による培養結果で
も無添加の場合よりも0.3及び51/11SA添加の
系ではいずれも菌体増殖は幾分低下したが、脂質含量は
10%以上増加しており、従って、脂質生成量が20%
以上増加していることが認められた。このことは脂質系
数の大きな増加となって表れており、SAの添加効果が
03〜5j9/1とかなり幅を持って菌体の高密度培養
により脂質生産に対して認められたことを示している。
When sodium acetate is added, a significant increase in lipid production and lipid content is observed regardless of the addition conditions. This means that the carbon source glucose 100,! This can also be seen from the fact that the lipid system number, which is the amount of lipid produced relative to 9, is significantly increased compared to the case without additives. Although the amount of bacterial cell growth was generally larger than in the case without additives, some variation was observed. Even with the culture results using a 3M culture tank with a glucose concentration of approximately 2o1/13 and a high concentration carbon source, bacterial cell growth was somewhat lower in both systems with 0.3 and 51/11SA added than in the case without additives. , the lipid content has increased by more than 10%, and therefore the lipid production has increased by 20%.
It was observed that the number of cases increased. This was manifested as a large increase in the number of lipid systems, indicating that the effect of SA addition was observed on lipid production by high-density culture of bacterial cells over a considerable range from 03 to 5j9/1. There is.

2 # G90 SA5 51 3 1 G90 5AIO69 4Iy G90 SA5 63 5 # G90 5AIO69,5 7〃 G85 5AIO51 8# G85 SA2.3 46 9 +’ G85 SAo、3 50 11 y G185 SA5 98  2 31.9 11.9 37.2 13.2 35.43
4.0 17.2 5Q、7 19.1 37.836
.1 18.4 51.0 2Q、5 40.140.
5 17.0 41.9 18.9 45.036.8
 17.9 48.5 19.8 40.931.3 
145 46.4 171 36.829.3 15.
7 53.4 18.4 34532.7 14.7 
45.0 17,3 38,434.4 15,2 4
4,2 17,9 40,777.6 28,8 37
,1 15,2 40,966.8 33,8 50,
6 18,2 36.1’745 35.9 48,2
 18,0 37.3なお、前記衣−2において、qは
グルコース、(Jは尿素、Asは硫酸アンモニウム、S
Aは酢酸ナトリウムを示す。
2 # G90 SA5 51 3 1 G90 5AIO69 4Iy G90 SA5 63 5 # G90 5AIO69,5 7〃 G85 5AIO51 8# G85 SA2.3 46 9 +' G85 SAo, 3 50 11 y G185 SA5 98 2 31.9 11.9 37.2 13.2 35.43
4.0 17.2 5Q, 7 19.1 37.836
.. 1 18.4 51.0 2Q, 5 40.140.
5 17.0 41.9 18.9 45.036.8
17.9 48.5 19.8 40.931.3
145 46.4 171 36.829.3 15.
7 53.4 18.4 34532.7 14.7
45.0 17,3 38,434.4 15,2 4
4,2 17,9 40,777.6 28,8 37
,1 15,2 40,966.8 33,8 50,
6 18,2 36.1'745 35.9 48,2
18,0 37.3 In the above coating-2, q is glucose, (J is urea, As is ammonium sulfate, S
A represents sodium acetate.

また、表−2に示した実験番号1〜12において、実験
番号1と10は対照試験(コントロール)であり、実験
番号2〜5では、前培養培地に′対してはSA無添加で
あり、実験番号4〜5では、培養スタート後、30時時
間区SAを添加し、実験番号6〜9及び実験番号11.
12では前培養地にS A 5 ji/11を添加した
In addition, in experiment numbers 1 to 12 shown in Table 2, experiment numbers 1 and 10 are control tests, and in experiment numbers 2 to 5, no SA was added to the preculture medium. In experiment numbers 4 to 5, SA was added at 30 o'clock after the start of culture, and in experiment numbers 6 to 9 and experiment number 11.
In No. 12, S A 5 ji/11 was added to the preculture medium.

Claims (1)

【特許請求の範囲】[Claims] (1) モルテイエレラ属に属するイサベリナ、ビナセ
ア、ナナ、ラマニアナ、ラマニアナ・アングリスポラの
菌株を炭水化物を炭素源とする培地に培養し、培養物よ
り脂質を採取するに際して、菌体を培養するための培地
に酢酸あるいは酢酸塩を加えることを特徴とする微生物
脂質の生産方法。
(1) Strains of Isabelina, Vinacea, Nana, Lamaniana, and Lamaniana angrispora belonging to the genus Morteierella are cultured in a medium using carbohydrates as a carbon source, and when lipids are collected from the culture, the strains are used as a medium for culturing the bacterial cells. A method for producing microbial lipids, characterized by adding acetic acid or acetate.
JP59115162A 1984-02-09 1984-06-05 Production of microbial lipid Granted JPS60259192A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP59115162A JPS60259192A (en) 1984-06-05 1984-06-05 Production of microbial lipid
DE8484306511T DE3470061D1 (en) 1984-02-09 1984-09-25 A method for the preparation of a fungal body and a lipid rich in gamma-linolenic acid therefrom
EP84306511A EP0155420B1 (en) 1984-02-09 1984-09-25 A method for the preparation of a fungal body and a lipid rich in gamma-linolenic acid therefrom
CA000473158A CA1235083A (en) 1984-02-09 1985-01-30 METHOD FOR THE PREPARATION OF A FUNGAL BODY AND A LIPID RICH IN .gamma.-LINOLENIC ACID THEREFROM
US06/929,601 US4783408A (en) 1984-02-09 1986-11-10 Method for the preparation of a fungal body and a lipid rich in Y-linolenic acid therefrom

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59115162A JPS60259192A (en) 1984-06-05 1984-06-05 Production of microbial lipid

Publications (2)

Publication Number Publication Date
JPS60259192A true JPS60259192A (en) 1985-12-21
JPS6251110B2 JPS6251110B2 (en) 1987-10-28

Family

ID=14655866

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59115162A Granted JPS60259192A (en) 1984-02-09 1984-06-05 Production of microbial lipid

Country Status (1)

Country Link
JP (1) JPS60259192A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5401646A (en) * 1986-07-08 1995-03-28 Suntory Limited Process for production of bishomo-gamma-linolenic acid and eicosapentaenoic acid

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5401646A (en) * 1986-07-08 1995-03-28 Suntory Limited Process for production of bishomo-gamma-linolenic acid and eicosapentaenoic acid

Also Published As

Publication number Publication date
JPS6251110B2 (en) 1987-10-28

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