JPS61254193A - Production of unssaturated wax ester - Google Patents

Production of unssaturated wax ester

Info

Publication number
JPS61254193A
JPS61254193A JP60097618A JP9761885A JPS61254193A JP S61254193 A JPS61254193 A JP S61254193A JP 60097618 A JP60097618 A JP 60097618A JP 9761885 A JP9761885 A JP 9761885A JP S61254193 A JPS61254193 A JP S61254193A
Authority
JP
Japan
Prior art keywords
medium
mold
unsaturated
wax
wax ester
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
JP60097618A
Other languages
Japanese (ja)
Other versions
JPH0527384B2 (en
Inventor
Masakazu Okumura
昌和 奥村
Shigeru Ii
井伊 茂
Hisao Araki
久雄 荒木
Yoshiki Tani
吉樹 谷
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.)
Harima Chemical Inc
Original Assignee
Harima Chemical Inc
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 Harima Chemical Inc filed Critical Harima Chemical Inc
Priority to JP60097618A priority Critical patent/JPS61254193A/en
Publication of JPS61254193A publication Critical patent/JPS61254193A/en
Publication of JPH0527384B2 publication Critical patent/JPH0527384B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To obtain unsaturated wax ester suitable as a substitute raw material for a sperm oil in high yield of production, by cultivating aerobically Euglena of a protozoan and changing a medium to an anaerobic state. CONSTITUTION:A microorganism of the genus Euglena (e.g., Englena gracillis Z strain) is inoculated into a medium consisting of a carbon source (e.g., glucose), a nitrogen source (e.g., NH4NO3 or peptone), ca, vitamin B1, etc. At the early stage of culture or after the mold is grown at a certain degree, 0.1-5wt% based on the medium of an unsaturated fatty acid (e.g., linoleic acid) is added to the medium, and the mold is cultivated at 20-33 deg.C at 3.0-7.0pH under an aerobic condition such as aeration or stirring for 3-6 days. Then when the growth of the mold in the medium is approximately in a stationary phase, nitrogen is introduced to the medium which is changed to an anaerobic state, the medium is kept in the state for 1-5 days, unsaturated wax ester is accumulated in the mold cell and it is extracted and separated from the mold.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、原生動物コーーグレナ(E uglena、
ミドリムシ)を培養することにより、不飽和ワックスエ
ステルを高収量に製造する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention is directed to the protozoan Euglena,
The present invention relates to a method for producing unsaturated wax esters in high yield by culturing Euglena (euglena).

ワックスエステルは、化学的には、高級脂肪族アルコー
ルと高級脂肪酸どのエステルであって、動(11物の表
皮保護、湿潤維持、熱10失の防」1等の作用があり、
まIζ産業的には、潤滑剤、艶出し剤、1σ水剤、化粧
品の原料等として、多量に使用されている。
Chemically speaking, wax esters are esters of higher aliphatic alcohols and higher fatty acids, and have 11 functions such as protecting the epidermis, maintaining moisture, and preventing heat loss.
Industrially, it is used in large quantities as a lubricant, polishing agent, 1σ water solution, raw material for cosmetics, etc.

従来不飽和ワックスエステルは、はどんどは動植物に起
因する天然物1)r +ろ製造されており、イの供給は
必ずしも安定しているとは言えなかった。
Conventionally, unsaturated wax esters have mostly been produced from natural products derived from animals and plants (1), and the supply of (1) has not always been stable.

特にマツ」つ鯨油からは良質の潤滑油として適づるワッ
クスエステルが得られているが、近年捕鯨禁止に端を発
づる供給不安により、代替原11の必要に氾まられてい
る。
In particular, wax esters suitable as high-quality lubricants are obtained from whale oil, but in recent years there has been a need for alternative raw materials due to supply concerns stemming from the ban on whaling.

マツコラ鯨油は、炭素数かそれぞれ14〜18の長鎖脂
肪酸と長鎖アルコールとからなる直鎖状ニスデルであつ
C1その脂肪酸及びアルコールは、それぞれ飽和又は、
二重結合を一個有づる不飽和のものである。
Matukola whale oil is a linear Nisdelic acid consisting of a long-chain fatty acid and a long-chain alcohol with carbon numbers of 14 to 18, respectively.
It is unsaturated with one double bond.

このマツコラ鯨油の代す4原わ1どして、深海魚Aレン
ジラフイー (1−1oplostethus atl
anticus)油や、植物ホホバ(3immonds
ia chinensiS)油が注目されている。オレ
ンジラフイー油は、炭素数がぞれぞれ16〜22であり
、飽和又は二重結合を一個有する不飽和の、長鎖脂肪酸
と長鎖アルコールとのエステルを主成分と覆るものであ
り、)したホホバ油は、炭素数がそれぞれ20及び22
で、イれぞれ二重結合−個をイjする不飽和長鎖脂肪酸
と不飽和長鎖アル丁】−ルとの」ステルを主成分と1゛
るものである。これら(まマツ=]つ扛(油に類似の招
逍を右しており、マツコラ鯨油の代%)i原料とイ「す
1りるものであるが、前者では血犯制限や魚身の問題か
あり、また後者では1IIi種から収穫に至る;にてに
長期間を要するものであって、充分に安定した供給源と
は菖え4「かった1、 また微生物学的にワックス−」lステルを41−産η−
る方法が知られている。このブ)法は、微/:1−物の
成γ〒が速く、生産性の調整が容易て゛あって、優れた
万)人で゛ある、。
This Matukora whale oil substitutes 4 raw materials for deep-sea fish A-range roughfish (1-1oplostethus atl).
anticus) oil, plant jojoba (3 immonds)
ia chinensiS) oil is attracting attention. Orange roughy oil has 16 to 22 carbon atoms each, and is mainly composed of saturated or unsaturated esters of long-chain fatty acids and long-chain alcohols having one double bond. ) jojoba oil has carbon numbers of 20 and 22, respectively.
The main components are unsaturated long-chain fatty acids and unsaturated long-chain alkylene esters, each of which has a double bond. These (matsu kola whale oil) have a similar effect to oil, and are used as raw materials and oil, but the former has restrictions on blood crimes, In addition, the latter requires a long period of time to harvest from the 1IIIi seeds, and there is no sufficiently stable source of supply. 41-yield η-
There are known methods to do this. This b) method is excellent because it allows for rapid growth of micro-products and easy adjustment of productivity.

従来の技術 而して従〉1ζ微41:物=゛/・的にワックスエステ
ルを1守る方法として、M 1crococcus c
erificansを用いてへAIJj゛カンからバル
ミザンFl’2ゼヂルを牛I11′−づる方法〈米国特
許3/109506号)、原生動物て1−グLノーlに
J−リ、炭素数か26・〜30の飽和ii1ノ鎖ワック
スニスデルを生産づる方法(特開昭59−118090
号) 、Nocardia属h’A l1il菌を用い
てへ4リゾカンからパルミヂンPI9セブルを’、1 
i’i″づる 方 ン人 〈 △ dv    △ p
pl   M 1crohio1.  1  /I  
、5   (1971イ「)93頁)、△c i n 
c l Ol)a c t e r 属細菌等を使用し
て飽和炭化水素からマツ−]つ鯨油・1゛)4・小バ油
に類似の化学04 造を有寸61ノックス丁スーノルを
11する方法(米国121訂第7′I/I O/I 2
B3″;5)等が知られている。
According to the conventional technology, as a method of protecting wax esters from a physical standpoint, M
erificans to produce valmisan Fl'2 from AIJJ゛kan (U.S. Pat. No. 3/109,506), protozoa to 1-Gnorl, J-Li, carbon number 26... Method for producing 30 saturated II 1-chain wax Nisdel (Japanese Unexamined Patent Publication No. 118090/1989)
No.), Parmidin PI9 Sebru from Rhizocane using Nocardia h'Al1il bacterium ', 1
i'i''zuru person 〈 △ dv △ p
pl M 1crohio1. 1/I
, 5 (1971 I') p. 93), △ci in
Using bacteria of the genus C.I.A.C.T.E.R., saturated hydrocarbons are converted to pine-]whale oil, 1゛)4, and a chemical similar to small butterfly oil. Method (U.S. 121st Edition 7'I/I O/I 2
B3'';5) and the like are known.

発明が解決しJ:うと1ノーる問題」jJしかしイrか
ら前′−E省の方θ、で゛杓1)れろt)の131.1
べて飽和の1ソックス−エステルであった。マツ−1つ
j!:j油は前)ホのJ、うに潤滑油として(つれてい
るか、潤滑油どしては114斤性、耐火化1)1を満足
する必要があり、そのため1m +1、ワックスエステ
ルを構成する脂肪酸及びアルー]−ルの炭素数がイれそ
れ17′IJx十てあり、脂肪酸及びアルコールの少イ
丁くとも一方に不飽和二11う結合を右しくいることが
必要であると省えられている。従つ(、前)小のJ、う
な飽和ワックス1−ステルは、マツ−]つ?・:t 1
Tllの代%j jBij%’!lとしては)凶当でな
い。
131.1 of 131.1, which is solved by the invention.
All were saturated 1 sox-esters. Pine - one j! :J oil must satisfy 1) as a lubricant (as a lubricant, as a lubricant, 114 catty properties, fire resistance 1), and therefore constitutes 1m + 1, wax ester. It can be omitted that the number of carbon atoms in fatty acids and alcohols is 17'IJx 10, and that it is necessary to have an unsaturated 211 bond in at least one of the fatty acids and alcohols. ing. Follow (, front) small J, eel saturated wax 1-stell, pine-] one?・:t 1
Tll's %j jBij%'! (as a person) is not unreasonable.

また前)ボの従来の方法のうノウ米用特許/I40/l
283号の方法にJ、れば、不飽和のワックスニスアル
がIrlられるが、その生産性は低く好ましい方法とは
いえイfい。
(Previously) Bo's traditional method patent for use of rice/I40/l
If the method of No. 283 is used, unsaturated wax nitrogen is produced, but the productivity is low and although it is a preferred method, it is not suitable.

本発明はかかる事情に8監みなされたしのであって、原
11−動物ユーグレナを培養することにより、潤滑油等
どして(◎れたマツ=1つ鯨油の代酋原*≧1どして適
当イf不飽和のワックスエステルを、高収量に生産リ−
る方法を提供することを目的とづるL)のである。
The present invention has been made in consideration of such circumstances, and by culturing animal Euglena, it is possible to obtain lubricating oil, etc. to produce suitable unsaturated wax esters in high yields.
The purpose of this is to provide a method for

問題点を解決づる手段 而して本発明は、培地に原生動物〕−グレナを好気的に
16養し、該培地に不能■1脂肪酸を添加した後、培地
を嫌気状態に移行することを特徴とJるものである。
As a means of solving the problem, the present invention provides a method of cultivating protozoa - Grena in a medium aerobically, adding a fatty acid to the medium, and then shifting the medium to an anaerobic state. It is a characteristic.

本発明にa3いて使用するコーター−;I−LSI、動
物学の分類上ユーグレナ属(ミトリムシ属)に属する原
生動物であって、この属に属する枡、変師、変異株を含
むものである。代表的なものとしてコーグレナ・グラシ
リス・7株(F 1ljJlenil QI’aC! 
l :S7)、コーグレナ・グラシリス・バシラリス変
株(F uglena  (1raciliS bac
illaris)  、 ]  −グブレノー・ヒリデ
ィス(FF u(11ena viritlis) 、
アスタシア・ロンガ(△StaSialonga)等を
挙げることがて゛さる。
The coater used in the present invention is I-LSI, which is a protozoan that belongs to the genus Euglena (genus Euglena) according to the zoological classification, and includes Masu, Hengeshi, and Mutant strains belonging to this genus. A representative example is Coglena gracilis 7 strains (F 1ljJlenil QI'aC!
l :S7), Fuglena (1raciliS bac
illiaris),] - Gubreno hiridis (FF u(11ena viritlis),
Examples include Astasia longa (△StaSialonga).

また]−グブレは、池や沼等の天然水系にも自然に生息
しており、これらを採取して利用づ−ることも可能であ
る1、またこれらを紫外線処理、熱処理、抗生物質処理
、二1へロソグアニジン処理等の公知の方法で処理した
各種の変異株し使用覆ることができる。
]-Gubure naturally inhabits natural water systems such as ponds and swamps, and it is also possible to collect and use them1.They can also be treated with ultraviolet light, heat, antibiotics, Various mutant strains treated with known methods such as 21-herosoguanidine treatment can be used.

ユーグレナの18養に使用Jる培地は、−1−レン・ハ
ッhナー培地(ジャーナルAブプロ1−ゾΔロジー(J
ournal of Protozoology ) 
1 /l 3 < 196フイ[)増補17頁記載)や
、ハツI−ナー培地(シ17−)−ルΔブプ[11〜ゾ
Δロシ一6巻(1959年)23頁記載)等の公知の培
地を使用することができる。
The medium used for the cultivation of Euglena is -1-Len Hachner medium (Journal
our own of Protozoology)
1 / l 3 < 196 F [) (enlarged p. 17)), Hatsu I-ner medium (S 17-) -l Δbup [11 to Zo Δ Roshi vol. 16 (1959) p. 23], etc. Known media can be used.

また、1ジJ索源と]ノCグルコース、澱粉水解物、糖
蜜水解物、グルタミン酸、耐酸、エタノール等を使用し
、窒素源どして硝酸−アンモニウム、第ニし)i M 
、/7ン土−ウノい1す11酸アンモニウム等のJ、う
>r照(、猛窒素源、グルタミン酸、アスパラギン酸等
のアミノ酸又は、ベフ゛1〜ン、カリ゛ミノ酸、酵1劇
丁二〜ス、−」−ンスブーーブリカー等の(if幾窒素
1原を、j西宜fil含わ11、こhにカルシウム、ン
クネシウム、7ンカン、八等の、l!!!、1よ〕油と
、ヒ゛タミンStルびB124・(敬重1111えたよ
うイ「培地を使用Jること0てさる1、また1炙素i斤
を使用1ユづ゛、1−グレリの光合成に1,1、ること
1)てさる。
In addition, the nitrogen source is nitrate-ammonium, nitrate-ammonium, etc., using glucose, starch hydrolyzate, molasses hydrolyzate, glutamic acid, acid resistance, ethanol, etc.
,/7 soil - ammonium oxide, etc. 2 ~ s, -'' - nsboob liquor, etc. (if how many nitrogen 1 element, j Nishi fil contains 11, oh, calcium, nucnesium, 7 nkan, 8th grade, l!!!, 1. ] oil and vitamin Strebium B124 (respectfully 1111). , 1) Tesaru.

丁7−クレナの培1:、!l記度は20〜33℃がj回
当でiV+す、ネ刀光fil 1−1 fit、3.0
□−7,0がiia 3.pである。
Ding 7 - Kurena's Cultivation 1:,! The temperature is 20 to 33 degrees Celsius, iV+, Netoko fil 1-1 fit, 3.0
□-7,0 is iia 3. It is p.

jと1杏は光照04 ’−F :!;4は11j′i黒
下のい1fれで行っても良い、 yt、たIf’; 3
:’! IIンには、1分間当り50へ・2F〕O回の
振器、又は適度の通気攪拌を行うことが!lfましい。
j and 1 anzu are light 04'-F:! ;4 can be done with 11j'i black bottom 1f, yt, taIf'; 3
:'! For II-in, use a shaker at a rate of 50°/2F]O times per minute, or perform moderate aeration stirring! It's adorable.

このJ、)イ; ’l’l’気条イ′1下て培養づ−る
ことにより、コーク(ノリ置51約3・〜・(30で成
長の定常期に達し、′1Ill fl包の11ン11′
・は、If’< j’¥液1Q当りの<12燥!「・早
として10〜20gどなる。
By culturing under 'l'l' airways A'1, the stationary phase of growth was reached at about 30 to 30 ml, and '1 Ill fl follicles were grown. 11'11'
・If'<j'¥<12 dryness per 1Q of liquid! ``・It's about 10 to 20 grams at first.

本発明において培41!1に添加する小胞([1脂肪醸
としくは、ミリス1〜レイン酸、パルミ1−レ、イン酸
、Δレイン酸、Jライシン酸、リノール酸、リルン酸、
ガl’レイン0(2、ボン1〜イン酸、セ1〜レイン6
1、エルカ酸tqが挙(Jられるが、[111勺とする
ワックスニス−フルの化4j%、絹成に応じた各種脂肪
酸及び、これらの8種アミン塩、金属」nを使用するこ
とがでさる、。
In the present invention, the vesicles added to the culture medium 41!
Gal'lein 0 (2, bon 1 ~ inic acid, se 1 ~ lein 6
1. Erucic acid (tq) is mentioned (J), but it is also possible to use [111% of wax varnish, 4j% of wax varnish, various fatty acids depending on silk formation, 8 types of amine salts thereof, and metals]. Dezaru.

不飽和脂肪酸の添加j)は、培地に対()で0.1〜5
%程1αであり、1′1に0.5〜2%稈度が適当であ
る1、培養の初期に添加りる揚台には、1rii i開
度に添加4るとユーグレノ−の成育を1ift害づるの
(゛、1%以下、さらに好ましくは、0.2〜0.5%
とづるのが良い。
Addition of unsaturated fatty acids j) to the medium is from 0.1 to 5
% 1α, and 0.5 to 2% culm degree is appropriate for 1'1. 1% or less, more preferably 0.2 to 0.5%
It is better to spell it out.

これらの不飽和脂肪酸の18地への添加rtl、期は、
培養開始後いかイ3・るll:’i 1jllでも良い
。培地に最初から添加L/ −U i15 イ(4:〉
J、イ(1) ’r アルh’、Mf y! ’7’)
初1v1に高温度の脂117+酸かあると閑の成育を遅
らせるので、菌かある程度成育した後に添加するのが好
ましい。
The addition rtl and period of these unsaturated fatty acids to 18 regions are as follows:
After the start of culture, it may be 3 times. Added to the medium from the beginning L/-U i15 i (4:>
J, I (1) 'r Alh', Mf y! '7')
If high-temperature fat 117 + acid is present at the beginning of 1v1, it will delay the growth of the dormant, so it is preferable to add it after the bacteria has grown to a certain extent.

また、轡の−[稈においで培地を嫌気状態に移行Jる際
には、添加1)た不v)1和脂肪酸がづ−Cに細胞内に
取込まれていることが望ましいので、嫌気状態に移行゛
りる1・〜・2[」前に添加刀るのが最し好ましい。
In addition, when transferring the medium to an anaerobic state in the culm of the culm, it is desirable that the added 1) and 1) fatty acids have been taken into the cells by the anaerobic state. It is most preferable to add it 1 to 2 times before the transition to the state.

培地の!+1F気状態への移行は、培地中に窒素を通じ
ることにより行う。移行の時期は、コーグレナの成長の
定常期イ(1近が好ましい。培地を嫌気状態に移行し〕
ζ後、1〜5B間イの状態に保持づることに」:す、細
胞中に不飽和ワックスニスデルが蓄積される。
Of medium! The transition to +1F air condition is carried out by passing nitrogen into the medium. The timing of the transition is during the stationary phase of Coglena growth (preferably around 1.5 pm; the medium is shifted to an anaerobic state).
After ζ, unsaturated wax Nisdel is accumulated in the cells by maintaining the state between 1 and 5B.

このようにして細胞内に1ノツクスエステルが蓄積され
たく、i:らば、遠心ブχN1等の方法で培養液/〕冒
ろ菌体を分1lall シ、絹膏人によって脂質を抽出
し、続いて該脂質からワックス」ステルを分離づ−る。
In order to accumulate 1 NOx ester in the cells in this way, remove the culture solution/infected bacterial cells by a method such as Raba or centrifugal tube, and extract the lipids using a silk paste. Subsequently, the wax stellate is separated from the lipid.

脂V(の抽出は、湿菌体をクロロホルム/メタノールd
液を用いて抽出処理刃−ることにより行うことがでさ、
またこの脂質からシリカゲルを使用したカラムク[1マ
ドグラフ−r−等でワックスエステルを分Sa+!)る
For extraction of fat V, wet bacterial cells are chloroform/methanol d
This can be done by using a liquid extraction process blade.
Also, from this lipid, wax esters are extracted using a column using silica gel [1Madograph-r-, etc.]. ).

作用 =  9 − ユーグ1ノ士は細菌−)酵母等に比べればかくfり大き
い111細胞の原生動物であるか、これらの微11−物
と同様L;二tツク1γ1首することができ、大量に生
産することができる。また]−クフレを好気的に培養し
1.:+’A !1IIi気条件下に保持するとワック
ス−■−ステルを生成ηることは前記特開11n 59
−118090により知られてd3す、子の41−成品
は乾燥菌体重へ1の50%にもji′刀る−しのであっ
て、極δl)C生産性の高いもの【゛ある。
Action = 9 - Hugue 1 is a protozoan with 111 cells, which is larger than bacteria -) yeast, etc., or it can have a 111-cell structure similar to these microscopic organisms, Can be produced in large quantities. [Also]-Cultivate Coufre aerobically 1. :+'A! It is stated in the above-mentioned Japanese Patent Application Laid-Open No. 11n 59 that wax-■-stellate is formed when the wax is kept under atmospheric conditions.
-118090 is known as d3, and its 41-product has a dry bacterial weight of up to 50% of 1, and has an extremely high δl)C productivity.

、コークレナによる!111i気条イ′1干におけるワ
ックスエステルの生成機B+f IJl、次のようなも
のであると考えられでいる。1 −づなわち、好気条件下に培養されたユーグレナを嫌気
条件■に置くと、好気条(!1下で貯蔵された多W1で
あるバラミ11ンが、グル2]−ス甲(riに分解され
、解糖系を経てピルビン酸になる1、生成(〕Iζピル
ヒン醸+J: 、アレヂルコ丁ンザイムAにイアり、さ
らにアセヂルコエンIJ”イノ、△l)+ rら脂肪/
lりか合成される。l この上うな過稈を経て合成された脂肪R91J、炭素数
14を中心どして11〜17の飽和の直鎖脂肪酸である
が、その一部はは(゛同様の炭素数分布を持つアルコー
ルに還元され、イの両成分の間でニスデル化反応が生じ
、ワックスエステルが生成するのである。従って、通常
の培地による培養においては、脂肪酸もアルコールもい
ずれも飽和のbの°Cあり、これらから1qられるワッ
クスエステルち飽和のもののみである。
, by Corklena! The wax ester generator B+f IJl in 111i air conditioner A'1 is believed to be as follows. 1 - That is, when Euglena cultured under aerobic conditions is placed in anaerobic conditions ■, baramin 11, which is a multi-W1 stored under aerobic conditions (! It is decomposed into ri and becomes pyruvic acid through glycolysis 1. Production (Iζ Pyruhin + J: , Alejylcoene IJ"Ino, △l) + r et al fat /
Only one is synthesized. The fat R91J synthesized through this process is a saturated straight chain fatty acid with 11 to 17 carbon atoms, with the center being 14. The Nisdell reaction occurs between both components of A and wax ester is produced. Therefore, in culture in a normal medium, both fatty acids and alcohols are saturated at °C. 1q of wax esters are the only saturated ones.

而してこのユーグレナに」;る嫌気状態にお(プるワッ
クスエステル生成過程においC1細胞内に培地から取込
んだ小胞和服+1/I酸が存右づ−ると、その一部はグ
ルコースに由来4−る飽和長鎖アルT」−ルとの間に−
Jスプル結合を形成して、小胞和服117i mと飽和
アルコールとのエステルを生じ、また他の一部は不飽和
長鎖アルコールに還元された後、グルコース由来の飽和
脂肪酸及び培地から取り込んだ不飽和脂肪酸との間に−
[スーアル結合を形成り−るのである。
During the wax ester production process, the vesicle +1/I acid taken in from the culture medium is present in the C1 cells, and some of it is converted into glucose. Between the 4-saturated long-chain al T'-ru derived from -
J-sprue bonds are formed to produce esters of vesicle Japanese 117im and saturated alcohols, and the other part is reduced to unsaturated long-chain alcohols, followed by saturated fatty acids derived from glucose and unsaturated alcohols taken from the medium. Between saturated fatty acids
[It forms a Sual bond.]

発明の効果 本発明によれば、このようにしてコーグレナの=  1
1  = 通常の嫌気状態下での培養にJ、る飽和ワックス−エス
テルに加えて、培地に添加した小胞和服111i uに
由来する不飽和ワックスエステルを効率良り(1−成さ
ぜることができるのである。
Effects of the Invention According to the present invention, in this way Coglena's = 1
1 = In addition to the saturated wax-esters produced during cultivation under normal anaerobic conditions, the unsaturated wax-esters derived from the vesicles added to the medium were added to the culture medium to efficiently (1-) This is possible.

而して本発明により1■られIこワックス」スrルは、
モの成分中に高率で不飽和二重結合を右しCJ−タリ、
マツコラ鯨fillに類似の化学構造をイラし、その代
替原料どl〕で潤滑剤等の用途に広く使用することがで
さる。
Therefore, according to the present invention, 1.
CJ-Tari, which has a high proportion of unsaturated double bonds in its components,
It has a chemical structure similar to that of Matsukora whale fill, and can be used as an alternative raw material for a wide range of applications such as lubricants.

しか−し二1−グレナは極めて入手の容易な原生動物で
あり、それを培養することによって、大量に目つ安定し
て不飽和ワックスエステルを供給づることがでさるので
ある。
However, 21-grena is a protozoan that is extremely easy to obtain, and by culturing it, it is possible to stably supply unsaturated wax esters in large quantities.

また細胞内の蓄積パラミロン中、培地からのグルコース
等のアレデル]エンザイムΔ供給源の供給量及び、JF
4 if!!に添Il[11−る不飽和脂肪酸の杆顆と
その供給槽を調節4ることにJ、す、生成りるワックス
エステルの組成を変化させることが可能である。
In addition, in the intracellular accumulated paramylon, the supply amount of the enzyme Δ source such as glucose from the medium, and the JF
4 if! ! By adjusting the amount of unsaturated fatty acid added to the rod and its feed tank, it is possible to change the composition of the wax ester produced.

実施例 =  12  = 以下本発明の実施例について説明する。Example = 12 = Examples of the present invention will be described below.

実施例−1 グルコース2g、ボリペブ1〜ン0.5g、硫酸アンモ
ニウム25mQ、炭酸水素アンモニウム25■9、第二
燐酸アンモニウム25m01炭酸マグネシウム60mq
、炭酸カルシウム12mg、モール塩5m9、硫酸マン
ガン−水和物1.8mg、硫酸亜鉛七水和物2.5mg
、ビタミンB+ 0.25mg及びビタミンBI20.
0005…qを、脱イオン水100mQに溶解し、pH
を4.5に調整した。これを500mQ容の艮頚振需フ
ラスコに入れて培地とし、ここにユーグレナ・グラシリ
ス・7株を接種し、1分間に120回振盪しt「がら暗
黒下に28℃で3日間培養した。
Example-1 Glucose 2g, Voripeb 1-0.5g, ammonium sulfate 25mQ, ammonium bicarbonate 25mQ, diammonium phosphate 25m01 magnesium carbonate 60mq
, calcium carbonate 12mg, Mohr's salt 5m9, manganese sulfate hydrate 1.8mg, zinc sulfate heptahydrate 2.5mg
, vitamin B+ 0.25mg and vitamin BI20.
0005…q was dissolved in 100 mQ of deionized water, and the pH
was adjusted to 4.5. This was placed in a 500 mQ volume shaker flask to serve as a medium, and Euglena gracilis 7 strains were inoculated therein, shaken 120 times per minute, and cultured in the dark at 28°C for 3 days.

然る後日本油脂株式会社製オレインM!2(7ルインA
1293.5%、リノール酸1.7%、ステアリン酸2
.4%)を19添加し、ざらに1日培養を継続した。
After that, Olein M! manufactured by Nippon Oil & Fats Co., Ltd. 2 (7 Ruin A
1293.5%, linoleic acid 1.7%, stearic acid 2
.. 4%) was added thereto, and the culture was continued for 1 day.

次いでフラスT]内容物を全て200m1容Hつ口丸底
フラスコに移()、p Hを6.5に調整し、2O′C
でゆるやかに攪拌しながら、室内光の下で窒素ガスを通
気しながら、さらに5日間培養を継続し 1こ 。
Next, transfer the entire contents of flask T to a 200 ml H-necked round bottom flask (), adjust the pH to 6.5, and add 2O'C.
Cultivation was continued for an additional 5 days while gently stirring and aerating nitrogen gas under room light.

次に遠心分離にJ、り菌体を集め、0.85%食塩水で
2回洗浄した後、その菌体をクロロ小ル11/メタノー
ル(1:1)混液に浸漬し、超γ′1波でホモジナイズ
して菌体を破砕すると共に、脂質を抽出した。抽出した
脂質はシリカゲルカラムにΩ荷し、ヘキサン/酢酸エチ
ル(10:0.5)ifP液で溶出し、純粋のワックス
エステル画分を19だ。
Next, the bacterial cells were collected by centrifugation, washed twice with 0.85% saline, and then immersed in a mixture of chlorol 11/methanol (1:1). Homogenization was performed using waves to disrupt the bacterial cells and extract lipids. The extracted lipids were loaded onto a silica gel column and eluted with hexane/ethyl acetate (10:0.5) ifP solution to obtain the pure wax ester fraction.

ワックスエステルの収量は、培養液100mf!当り約
0.85!IIであ・)1こ。
The yield of wax ester is 100mf of culture solution! Approximately 0.85 hit! In II.)1.

分離1したワックスエステルを常法に従い、アルカリで
鹸化して脂肪酸成分とアルコール成分とに分(′J、脂
肪酸成分をメチルエステル化した後、それぞれガスクロ
マI−グラフィーによる分析を行い、構成成分の組成を
検問した。その結果を表−1に示す。
The separated wax ester was saponified with an alkali according to a conventional method to separate the fatty acid component and the alcohol component ('J). The results are shown in Table 1.

=  14  = 実施1シ]−2 Eノ−グレナ・グラシリス・7株の野生株を、500最
容の長頚振盪フラスコ中の1%グルコースを主炭素源と
り−るコーレン・ハラ1−ナー培地100耐に接種し、
初光11)−13,5で1分間に120回振盪しながら
、nR黒下、28℃で培養した、14日間培養した後、
遠心力l(によって細胞を集め、19のAレイン?!+
2 (実施例−1と同じ)を含む100ynQの]−レ
ン・ハツ]−ナー培地<pl−17,0)に再懸潤し、
実施例−1にaシ(プると同様に、1曇1」′しなから
室温(10〜15℃)で窒素ガスを通じ=  15 − て5日間培養した。
= 14 = Execution 1]-2 Seven wild strains of E. noglena gracilis were grown in Koren-Hara 1-ner medium with 1% glucose as the main carbon source in a 500-capacity long-neck shake flask. Inoculated to 100 resistant,
After culturing for 14 days, the cells were cultured at 28°C under nR black while shaking 120 times per minute at First Light 11)-13,5.
Collect cells by centrifugal force l (19 A rain?!+
2 (same as Example-1) and resuspended in 100ynQ]-Len Hatsu]-ner medium <pl-17,0),
In the same manner as in Example 1, the cells were cultured for 5 days at room temperature (10-15° C.) under nitrogen gas.

然る後実施例−1に)小べたと同様に操作して菌体を集
め、脂質を抽出し、ワックスエステルを分離した。ワッ
クスエステルの収量は、培地100耐当り、約0.’1
.OQであった。またそのワックスニスアルの構成成分
の組成は、表−2の通りであった。
Thereafter, the cells were collected in the same manner as in Example 1), the lipids were extracted, and the wax ester was separated. The yield of wax ester is approximately 0.0% per 100 ml of culture medium. '1
.. It was OQ. The composition of the constituent components of the wax Nissal was as shown in Table 2.

実施例−3 培地に添加する不飽和脂肪酸どして、和光純薬工業株式
会ネ1製のリノール酸くリノール酸88゜7%、Aレイ
ン酸9,8%、α−リルン酸O95%、パルミチンMt
0.6%)を19使用した外は、実施例−2と同様にし
−Cワックスエステルを1qた。11ンfβ(;1培地
100mf!当り約0.80!]であり、その構成成分
の組成は、表−3の通りであつ1こ 。
Example 3 The unsaturated fatty acids added to the culture medium were linoleic acid 88.7%, A-leic acid 9.8%, α-lylunic acid O 95%, manufactured by Wako Pure Chemical Industries, Ltd. Palmitin Mt
The procedure was the same as in Example 2 except that 1q of -C wax ester was used, except that 19% of 0.6%) was used. 11 fβ (approximately 0.80 per 100 mf! of one medium!), and the composition of its constituent components is as shown in Table 3.

実施例−4 18地に添7J[+−する不飽和脂肪酸として、半月化
学薬品工業株式会社製のα−リルン酸(α−リルン般7
2.7%、リノール酸19.7%、Aレイン酸7.1%
)19を使用した外は、実施例−2と同様にしてワック
スエステルを得た。ワックスエステルの収量は培地10
0mQ当り約0,91qであり、その構成成分の組成は
、表−4の通りであった。
Example-4 As an unsaturated fatty acid added to 18 bases, α-lylunic acid (α-lyllun general 7
2.7%, linoleic acid 19.7%, A-leic acid 7.1%
) A wax ester was obtained in the same manner as in Example 2, except that 19 was used. The yield of wax ester is medium 10.
It was about 0.91q per 0mQ, and the composition of its constituent components was as shown in Table 4.

以上の実施例から、培地からユーグレナの細胞内に取込
まれた不飽和脂肪酸及び、該不飽和脂肪酸がユーグレナ
が持つ長鎖脂肪酸)9元酵素系により還元された不飽和
長鎖アルコールを、それぞれ構成成分どじて右づる不飽
和ワックスエステルが効率よく生成していることが理解
できる。
From the above examples, the unsaturated fatty acids taken into the cells of Euglena from the medium and the unsaturated long-chain alcohols that were reduced by the long-chain fatty acid (long-chain fatty acids) that Euglena has, respectively. It can be seen that the unsaturated wax esters, which have different constituent components, are produced efficiently.

また、実)履例−1のように、培地に不飽和脂肪酸を添
加した後ただちに嫌気状態に移行せず、好気的培養を経
た場合には、菌体内に取り込まれた小胞11 flit
 1I7i n:2か/′l酸化を受りだことに起因す
ると考えられる、鎖長の減成した不飽和脂肪酸、及びて
れが還元されたことに起因刈ると考2られる鎖長の減成
した不飽和アルコールち、一部生成している、。
In addition, as in Example 1, if unsaturated fatty acids are added to the medium and the medium is not immediately converted to an anaerobic state but subjected to aerobic culture, the vesicles 11 flit taken into the bacterial cells.
1I7i n: 2/'l Unsaturated fatty acids with reduced chain length, which is thought to be caused by receiving oxidation, and reduced chain length, which is thought to be caused by reduction of tere. Some unsaturated alcohols are produced.

Claims (1)

【特許請求の範囲】[Claims] 1 培地に原生動物ユーグレナを好気的に培養し、該培
地に不飽和脂肪酸を添加した後、培地を嫌気状態に移行
することを特徴とする、不飽和ワックスエステルの製造
方法
1. A method for producing an unsaturated wax ester, which comprises aerobically cultivating the protozoan Euglena in a medium, adding an unsaturated fatty acid to the medium, and then shifting the medium to an anaerobic state.
JP60097618A 1985-05-07 1985-05-07 Production of unssaturated wax ester Granted JPS61254193A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60097618A JPS61254193A (en) 1985-05-07 1985-05-07 Production of unssaturated wax ester

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60097618A JPS61254193A (en) 1985-05-07 1985-05-07 Production of unssaturated wax ester

Publications (2)

Publication Number Publication Date
JPS61254193A true JPS61254193A (en) 1986-11-11
JPH0527384B2 JPH0527384B2 (en) 1993-04-21

Family

ID=14197187

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60097618A Granted JPS61254193A (en) 1985-05-07 1985-05-07 Production of unssaturated wax ester

Country Status (1)

Country Link
JP (1) JPS61254193A (en)

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02138964A (en) * 1988-11-18 1990-05-28 Harima Chem Inc Method for enriching nutrient in alga of genus euglena
JPH02219566A (en) * 1989-02-21 1990-09-03 Harima Chem Inc Treated euglena and use thereof
JP2011246605A (en) * 2010-05-26 2011-12-08 Hitachi Plant Technologies Ltd Method for producing biofuel
CN103003413A (en) * 2010-07-20 2013-03-27 优瑞纳股份有限公司 Process for production of euglena containing wax ester at high content, and process for production of wax ester
DE102012223213A1 (en) 2011-12-16 2013-06-20 Sumitomo Rubber Industries, Ltd. Rubber composition for a tire and pneumatic tire
WO2013115288A1 (en) * 2012-01-31 2013-08-08 株式会社ユーグレナ Method for producing euglena having high wax ester content
JP2014019856A (en) * 2012-07-23 2014-02-03 Sumitomo Rubber Ind Ltd Rubber composition for tire and pneumatic tire
US20150011784A1 (en) * 2012-01-31 2015-01-08 Jx Nippon Oil & Energy Corporation Method for producing fuel oil base
JP2015098539A (en) * 2013-11-19 2015-05-28 住友ゴム工業株式会社 Tire rubber composition and pneumatic tire
JP2019110894A (en) * 2017-12-21 2019-07-11 学校法人明治大学 Method for producing amino acid and method of culturing euglena
JP2020520644A (en) * 2017-05-17 2020-07-16 プロヴィヴィ インコーポレイテッド Microorganisms and related compounds for the production of insect pheromones
US11214818B2 (en) 2016-06-06 2022-01-04 Provivi, Inc. Semi-biosynthetic production of fatty alcohols and fatty aldehydes
US11844353B2 (en) 2015-11-18 2023-12-19 Provivi, Inc. Microorganisms for the production of insect pheromones and related compounds

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013153981A1 (en) * 2012-04-10 2013-10-17 花王株式会社 Method for producing fatty acid ester

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59118090A (en) * 1982-12-22 1984-07-07 Shozaburo Kitaoka Preparation of wax ester, higher fatty alcohol and higher fatty acid
JPS6078587A (en) * 1983-10-05 1985-05-04 Lion Corp Preparation of fatty acid ester

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59118090A (en) * 1982-12-22 1984-07-07 Shozaburo Kitaoka Preparation of wax ester, higher fatty alcohol and higher fatty acid
JPS6078587A (en) * 1983-10-05 1985-05-04 Lion Corp Preparation of fatty acid ester

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02138964A (en) * 1988-11-18 1990-05-28 Harima Chem Inc Method for enriching nutrient in alga of genus euglena
JPH02219566A (en) * 1989-02-21 1990-09-03 Harima Chem Inc Treated euglena and use thereof
US8951773B2 (en) 2010-05-26 2015-02-10 Hitachi, Ltd. Production method for biofuel
JP2011246605A (en) * 2010-05-26 2011-12-08 Hitachi Plant Technologies Ltd Method for producing biofuel
CN103003413A (en) * 2010-07-20 2013-03-27 优瑞纳股份有限公司 Process for production of euglena containing wax ester at high content, and process for production of wax ester
US9045784B2 (en) 2010-07-20 2015-06-02 Euglena Co., Ltd. Method for production of euglena containing wax ester at high content, and method for production of wax ester
DE102012223213A1 (en) 2011-12-16 2013-06-20 Sumitomo Rubber Industries, Ltd. Rubber composition for a tire and pneumatic tire
US20150010987A1 (en) * 2012-01-31 2015-01-08 Euglena Co., Ltd. Method for producing euglena having high wax ester content
US20150011784A1 (en) * 2012-01-31 2015-01-08 Jx Nippon Oil & Energy Corporation Method for producing fuel oil base
JP2013153730A (en) * 2012-01-31 2013-08-15 Euglena Co Ltd Method for producing euglena having high wax ester content
WO2013115288A1 (en) * 2012-01-31 2013-08-08 株式会社ユーグレナ Method for producing euglena having high wax ester content
TWI564391B (en) * 2012-01-31 2017-01-01 Euglena Co Ltd Method for producing Euglena with high wax content
JP2014019856A (en) * 2012-07-23 2014-02-03 Sumitomo Rubber Ind Ltd Rubber composition for tire and pneumatic tire
JP2015098539A (en) * 2013-11-19 2015-05-28 住友ゴム工業株式会社 Tire rubber composition and pneumatic tire
US11844353B2 (en) 2015-11-18 2023-12-19 Provivi, Inc. Microorganisms for the production of insect pheromones and related compounds
US11214818B2 (en) 2016-06-06 2022-01-04 Provivi, Inc. Semi-biosynthetic production of fatty alcohols and fatty aldehydes
JP2020520644A (en) * 2017-05-17 2020-07-16 プロヴィヴィ インコーポレイテッド Microorganisms and related compounds for the production of insect pheromones
US11866760B2 (en) 2017-05-17 2024-01-09 Provivi, Inc. Microorganisms for the production of insect pheromones and related compounds
JP2019110894A (en) * 2017-12-21 2019-07-11 学校法人明治大学 Method for producing amino acid and method of culturing euglena

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