JP3506740B2 - Method for culturing algae containing docosahexaenoic acid - Google Patents

Method for culturing algae containing docosahexaenoic acid

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Publication number
JP3506740B2
JP3506740B2 JP24885093A JP24885093A JP3506740B2 JP 3506740 B2 JP3506740 B2 JP 3506740B2 JP 24885093 A JP24885093 A JP 24885093A JP 24885093 A JP24885093 A JP 24885093A JP 3506740 B2 JP3506740 B2 JP 3506740B2
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Prior art keywords
algae
weight
culture
salt concentration
culturing
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JPH0775557A (en
Inventor
清 長谷川
美代子 佐野
浩明 岩本
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日清オイリオ株式会社
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Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、従属栄養で生育し、ド
コサヘキサエン酸(以下、DHAと略す。)を産生する
能力のある藻類を培養し、その藻体内にDHA含有極性
脂質を豊富に蓄積せしめる前記藻類の培養方法に関す
る。
TECHNICAL FIELD The present invention relates to the cultivation of algae capable of producing docosahexaenoic acid (hereinafter abbreviated as DHA), which grows under heterotrophic conditions, and abundantly accumulates DHA-containing polar lipids in the algal body. The present invention relates to a method for culturing the algae.

【0002】[0002]

【従来の技術】DHAは、近年、種々の生理活性を有す
る高度不飽和脂肪酸の一種として注目されている。これ
を産生する能力のある藻類として、例えばアムフィディ
ニウム(Amphidinium)属等の藻類が報告されており(J.
Protozoal 、第17巻(2)、第213〜219頁、1
970年)、またイソクリシス(Isochrysis) 属のDH
A産生藻類の生産が試みられている(特開平4−346760
号公報)。しかしながら、それらはいずれも独立栄養で
生育する藻類であり、培養コストが高くつくだけでな
く、藻体中の油分含量が低く、満足できるDHA含有油
脂を生産できるまでには至っていない。一方、従属栄養
により生育するDHA産生藻類としてはクリプセコディ
ニウム(Crypthecodinium)属に属する藻類が知られてい
る(Phytochemistry 、第27巻(6)、第1679〜1
683頁、1988年)。
2. Description of the Related Art Recently, DHA has been attracting attention as a kind of highly unsaturated fatty acid having various physiological activities. As algae capable of producing this, for example, algae of the genus Amphidinium and the like have been reported (J.
Protozoal, Vol. 17 (2), pp. 213-219, 1
970), and also DH of the genus Isochrysis
Attempts have been made to produce A-producing algae (Japanese Patent Laid-Open No. 4-346760).
Issue). However, all of them are algae that grow autotrophically, and not only the culture cost is high, but also the oil content in the algal body is low, and satisfactory DHA-containing fats and oils cannot be produced. On the other hand, algae belonging to the genus Crypthecodinium are known as DHA-producing algae that grow by heterotrophy (Phytochemistry, Vol. 27 (6), No. 1679-1).
683, 1988).

【0003】従来、従属栄養的に生育する微生物や藻類
による油脂の生産においては、菌体あるいは藻体内へ油
脂分を蓄積させる手法に関心がもたれ、研究が推進され
てきた。すなわち前記生物細胞内への油分の蓄積は一般
に主としてトリグリセリドいわゆる中性脂質の型で行わ
れ、多量に蓄積した場合、それらトリグリセリドは細胞
中で油滴のような形態で蓄積される。そして細胞内へ多
量の油分を蓄積させる方法としては、培地組成のC/N
比率を高くし、あるいは窒素源の欠乏状態を人為的に与
える手法等が使われてきた。(「油脂」、第24巻
(5)、第126〜135頁、1971年)。
Conventionally, in the production of fats and oils by microorganisms and algae that grow heterotrophically, there has been interest in a technique for accumulating fats and oils in fungi or algae, and research has been promoted. That is, the accumulation of oil in the living cells is generally carried out mainly in the form of triglycerides, so-called neutral lipids, and when accumulated in large amounts, these triglycerides are accumulated in the cells in the form of oil droplets. And as a method for accumulating a large amount of oil in cells, C / N of the medium composition is
Methods such as increasing the ratio or artificially giving a deficiency state of the nitrogen source have been used. ("Fat and oil", Vol. 24 (5), pp. 126-135, 1971).

【0004】すなわち従属栄養的に生育する藻類では、
油分の大部分が主として中性脂質として藻体内に蓄積さ
れることは知られていた。例えば前記Phytochemistry、
第27巻(6)、第1679〜1683頁、1988年
によれば、クリプセコディニウム コーニー(Crypthec
odinium cohnii)の培養藻体中の油分は、その約72%
がトリアシルグリセリドを主体とする中性脂質、約28
%がホスファチジルコリン等のリン脂質を主体とする極
性脂質として存在し、さらにかかるリン脂質の構成脂肪
酸の主要脂肪酸はDHA等の高度不飽和脂肪酸である。
That is, in heterotrophically growing algae,
It has been known that most of the oil content is mainly accumulated in the algal body as neutral lipids. For example, the above-mentioned Phytochemistry,
According to Volume 27 (6), pp. 1679-1683, 1988, Crypthecodinium Cornie (Crypthec
About 72% of the oil content in the cultured algal cells of odinium cohnii)
Is a neutral lipid consisting mainly of triacylglyceride, about 28
% Exists as a polar lipid mainly composed of phospholipids such as phosphatidylcholine, and the main fatty acids constituting fatty acids of such phospholipids are highly unsaturated fatty acids such as DHA.

【0005】したがって油分を構成する脂肪酸のうち、
DHA等の高度不飽和脂肪酸以外のパルミチン酸、オレ
イン酸等の脂肪酸は主としてトリアシルグリセリドのよ
うな中性脂質として存在し、一方、DHA等の高度不飽
和脂肪酸はリン脂質や糖脂質といった極性脂質の形態で
藻体中に存在する傾向があると考えられる。しかしなが
ら、DHA産生能のある藻類を対象とし、その藻体中に
DHA含有極性脂質を多量に蓄積せしめる試みは、これ
までに行われていなかった。
Therefore, of the fatty acids that make up the oil,
Fatty acids such as palmitic acid and oleic acid other than highly unsaturated fatty acids such as DHA mainly exist as neutral lipids such as triacylglycerides, while highly unsaturated fatty acids such as DHA are polar lipids such as phospholipids and glycolipids. It is considered that they tend to exist in the alga body in the form of. However, no attempt has been made so far for algae capable of producing DHA to accumulate a large amount of DHA-containing polar lipid in the alga body.

【0006】[0006]

【発明が解決しようとする課題】本発明の目的は、従属
栄養で生育するDHA産生藻類を培養するにあたり、D
HA含有極性脂質を前記藻類の細胞内に豊富に蓄積せし
めることのできる培養方法を提供することにあり、ひい
ては効率良く、生産コストの低い工業的なDHA含有藻
類の生産法を提供することにある。
DISCLOSURE OF THE INVENTION An object of the present invention is to cultivate DHA-producing algae that grow in heterotrophic nutrients.
An object of the present invention is to provide a culturing method capable of abundantly accumulating HA-containing polar lipids in the cells of the algae, and further to provide an efficient and industrially low-cost industrial DHA-containing algae production method. .

【0007】[0007]

【課題を解決するための手段】本発明者らは、上記目的
を達成すべく鋭意研究を行った結果、従属栄養的に培養
でき、なおかつDHAを生産する能力のある単細胞藻類
の培養中に、培養液の食塩濃度を上昇させることによ
り、任意の培養時期に、藻体中のリン脂質や糖脂質等の
極性脂質濃度およびDHA含有量を顕著に上昇させるこ
とが可能であることを見出し、本発明を完成した。すな
わち本発明は、従属栄養で生育するDHA産生能のある
藻類を培養するにあたり、培養中、培養液の食塩濃度を
藻類の生育に好適な食塩濃度より0.1〜10重量%高
い値に設定して培養することを特徴とする藻類の培養方
法に関する。
Means for Solving the Problems As a result of intensive studies to achieve the above object, the present inventors have found that during culturing of unicellular algae capable of heterotrophic culture and capable of producing DHA, It was found that by increasing the salt concentration of the culture solution, it is possible to significantly increase the polar lipid concentration such as phospholipids and glycolipids in the algal cells and the DHA content at any culturing time. Completed the invention. That is, the present invention sets the salt concentration of the culture solution to a value higher by 0.1 to 10% by weight than the salt concentration suitable for the growth of algae during the culture when culturing algae capable of producing DHA that grow in heterotrophic. The present invention relates to a method for cultivating algae, which comprises culturing the algae.

【0008】本発明で用いる藻類は、従属栄養的に培養
が可能な、DHAを藻体内に産生、蓄積できる藻類であ
り、特にその種あるいは株を限定するものではない。こ
れに該当する藻類としては、例えば「微生物学辞典19
92年度版」(技報堂出版)によれば、有色藻門、渦鞭
毛藻綱、ペリディニウム目、クリプセコディニウム属に
属するクリプセコディニウム コーニー(Crypthecodin
ium cohnii)、トラウストキトリウム アウレウム(Th
raustochytrium aureum )等があげられる。これらの藻
類は、American Type Culture Collection(米国、略称
ATCC)等の藻類研究機関より容易に入手でき、例え
ば前者ではATCC30021、同30334、同30
336、同50052、また後者ではATCC2821
1、同34304等がある。
The algae used in the present invention are heterotrophically culturable algae capable of producing and accumulating DHA in the alga body, and the species or strain thereof is not particularly limited. Examples of algae corresponding to this include “Microbiology Dictionary 19
1992 edition ”(Gihodo Publishing Co., Ltd.), Crypthecodinium corny (Crypthecodin) belonging to the genus Chlorophyta, dinoflagellate, Peridinium, and genus Crypthecodinium.
ium cohnii), Thraustochytrium aureum (Th
raustochytrium aureum) and the like. These algae can be easily obtained from algae research institutes such as American Type Culture Collection (US, abbreviated as ATCC). For example, ATCC30021, 30334, 30
336, 50052, and in the latter ATCC 2821
1 and 34304.

【0009】本発明の実施に当たっては、上記の従属栄
養で生育し、かつDHA産生能のある藻類をまず常法に
より培地で培養し、ついで任意の時期に培地の食塩濃度
を上昇させる。すなわち、食塩濃度が1.2〜2.5重
量%である、天然もしくは人工海水培地、あるいはグル
コース、ショ糖等の炭素源、アンモニウム塩、酵母エキ
ス、アミノ酸またはその塩等の窒素源、各種ビタミン類
およびミネラル類を含む培地を用い、pHを5〜7と
し、20〜35℃で、好適にはその藻類の増殖曲線にお
ける指数増殖中期まで培養する。この初期の培養時のp
H、温度および食塩濃度がこの範囲を外れると藻類の増
殖そのものが阻害される傾向が大きくなる。
In carrying out the present invention, the algae that grow in the above-mentioned heterotrophic and have the ability to produce DHA are first cultivated in a medium by a conventional method, and then the salt concentration of the medium is increased at an arbitrary time. That is, a natural or artificial seawater medium having a salt concentration of 1.2 to 2.5% by weight, or a carbon source such as glucose and sucrose, an ammonium salt, a yeast extract, a nitrogen source such as an amino acid or a salt thereof, and various vitamins. Using a medium containing algae and minerals, the culture is carried out at a pH of 5 to 7 at 20 to 35 ° C., preferably until the middle exponential growth phase in the growth curve of the algae. P during this initial culture
If H, temperature and salt concentration deviate from this range, the growth of algae tends to be inhibited.

【0010】ついで任意の培養時期、好ましくは指数増
殖中期以降、例えば対数増殖期ないし定常期の任意の時
期において、培養液の食塩濃度を上昇させる。このとき
の食塩濃度の上昇値は、その藻類の生育に好適な食塩濃
度すなわち1.2〜2.5重量%よりも0.1〜10重
量%、好ましくは0.1〜3重量%高い値に設定し、そ
の食塩濃度で培養を継続する。食塩濃度の上昇幅が0.
1重量%に満たないとDHA含有極性脂質を高濃度に蓄
積せしめることができず、10重量%を超えて食塩濃度
を上昇させると藻類の増殖を阻害するので好ましくな
い。なお本発明では、培地中のかかる食塩濃度の上昇に
あたっては、食塩濃度のみならず、食塩以外の他の海水
構成成分も食塩と同時に加え、海水濃度として上昇させ
てもよい。このために用いる食塩および海水構成成分
は、天然海水の濃縮物を用いるのが至便である。
Then, the salt concentration of the culture solution is increased at an arbitrary culture time, preferably after the exponential growth phase, for example, at any time from the logarithmic growth phase to the stationary phase. The increase value of the salt concentration at this time is 0.1 to 10% by weight, preferably 0.1 to 3% by weight higher than the salt concentration suitable for the growth of the algae, that is, 1.2 to 2.5% by weight. And continue the culture at that salt concentration. The range of increase in salt concentration is 0.
If it is less than 1% by weight, the DHA-containing polar lipid cannot be accumulated at a high concentration, and if the salt concentration exceeds 10% by weight, the growth of algae is inhibited, which is not preferable. In the present invention, when increasing the salt concentration in the medium, not only the salt concentration but also other seawater constituents other than the salt may be added at the same time as the salt to increase the seawater concentration. It is convenient to use a concentrate of natural seawater as the salt and seawater constituents used for this purpose.

【0011】培地の食塩濃度を上昇させる時期は、前記
のとおり任意の培養時期でよく、例えば藻体の増殖量が
所望の量に達した時、あるいは培養工程の作業上必要な
時期等であるが、望ましくは藻体の指数増殖中期以降の
任意の段階である。これより前の培養段階においては、
急激な食塩濃度の上昇により藻類の増殖自体を阻害する
場合があり、好ましくない。なお増殖が定常期の培養藻
体にこの方法を適用すると、リン脂質や糖脂質等の極性
脂質濃度の高い藻体を高収量で得ることができるので好
ましい。
The time for increasing the salt concentration of the medium may be any culture time as described above, for example, when the growth amount of the algal cells reaches a desired amount or when it is necessary in the work of the culture process. However, it is preferably any stage after the middle exponential growth of algae. In the culture stages prior to this,
A rapid increase in salt concentration may inhibit the growth of algae, which is not preferable. Note that it is preferable to apply this method to cultured algal cells in a stationary phase, since algal cells with a high concentration of polar lipids such as phospholipids and glycolipids can be obtained in high yield.

【0012】かくして食塩濃度を上昇させた培養液で、
藻類の種類にもよるが、通常3〜50時間程度培養すれ
ば、本発明の目的とするDHA含有極性脂質を多量に含
む藻体を得ることができる。なお食塩濃度を上昇させた
後の培養時間が3時間に満たないと藻体中の極性脂質の
含量が少なく、逆に50時間を超えて長時間培養すると
藻体収量が低下する。
[0012] In the culture solution thus increased in salt concentration,
Although it depends on the type of algae, the alga body containing a large amount of the DHA-containing polar lipid, which is the object of the present invention, can be obtained by generally culturing for about 3 to 50 hours. If the culture time after raising the salt concentration is less than 3 hours, the content of polar lipids in the alga body is small, and conversely, if the culture is continued for a long time exceeding 50 hours, the alga body yield decreases.

【0013】本発明において培地の食塩濃度を上昇させ
て培養して得られる藻体の脂質含量は、培養時間や食塩
濃度の上昇を開始した時期等によっても異なるが、例え
ば食塩濃度上昇開始後およそ24時間で、油分のうち極
性脂質が50〜65重量%、中性脂質が35〜50重量
%となる。なお極性脂質の内訳は、大略、リン脂質が2
0〜40%、糖脂質が30〜50%、その他成分が約3
0%である。また、全脂質中の構成脂肪酸のうちDHA
含量は45〜50重量%であり、極性脂質中の構成脂肪
酸のうちDHA含量は60〜75重量%となる。これに
対し、食塩濃度を上昇させずに培養を行うと、油分含有
のうち極性脂質は20〜30重量%、中性脂質は70〜
80重量%であり、また全脂質中の構成脂肪酸のうちD
HA含量は20重量%程度、極性脂質中の構成脂肪酸の
うちDHA含量は40〜50重量%にとどまる。
In the present invention, the lipid content of the algal cells obtained by culturing by increasing the salt concentration of the medium varies depending on the culturing time and the time when the increase of the salt concentration is started. In 24 hours, 50 to 65% by weight of polar lipids and 35 to 50% by weight of neutral lipids are contained in the oil. The breakdown of polar lipids is that phospholipids are 2
0-40%, glycolipids 30-50%, other ingredients about 3
It is 0%. Of the constituent fatty acids in total lipids, DHA
The content is 45 to 50% by weight, and the DHA content of the constituent fatty acids in the polar lipid is 60 to 75% by weight. On the other hand, when the culture is carried out without increasing the salt concentration, the polar lipid content is 20 to 30% by weight and the neutral lipid content is 70 to
80% by weight, and D among the constituent fatty acids in total lipids
The HA content is about 20% by weight, and the DHA content of the constituent fatty acids in the polar lipid is 40 to 50% by weight.

【0014】[0014]

【実施例】【Example】

実施例1 クリプセコディニウム コーニー(Crypthecodinium co
hnii) ATCC30336を、表1に示した組成の培地
3リットルに植えつけ、30℃にて、pHを6.8に調
整しながらジャーファーメンターで通気培養した。培養
中、増殖した藻体の湿物重量を経時的に測定し、その増
殖曲線から対数増殖中期に相当する培養開始後100時
間目に、食塩を20g/1L添加して培地中の食塩濃度
を2重量%上昇させ、さらに24時間培養を継続した。
その後、培養藻体を遠心分離して集め、藻体を凍結乾燥
して乾燥藻体を62g得た。
Example 1 Crypthecodinium coney
hnii) ATCC30336 was inoculated into 3 liters of the medium having the composition shown in Table 1 and subjected to aeration culture with a jar fermenter at 30 ° C while adjusting the pH to 6.8. During the culture, the weight of the wet matter of the grown algal cells was measured over time, and from the growth curve, at 100 hours after the start of culture, which corresponds to the mid-logarithmic growth phase, 20 g / 1 L of salt was added to determine the salt concentration in the medium. It was increased by 2% by weight, and the culture was continued for another 24 hours.
Then, the cultured algal cells were collected by centrifugation and freeze-dried to obtain 62 g of dried algal cells.

【0015】この乾燥藻体6.2gをクロロホルム/メ
タノール=1:1(重量)混合溶媒中でヒスコトロンに
より細胞破砕後抽出し、0.5gの油分を得た。抽出油
分を、シリカゲルプレートを用いた薄層クロマトグラフ
ィー(TLC)でクロロホルム/メタノール/酢酸混合
溶媒にて展開し、極性脂質画分と中性脂質画分とに分離
した。ついでこのシリカゲルプレートより、それぞれの
スポットをかき取り、クロロホルム/メタノール=1:
1(重量)混合溶媒にて再抽出したところ、極性脂質含
量が52重量%、中性脂質含量が48重量%であった。
なお極性脂質のうち、リン脂質が30%、糖脂質が40
%、その他が30%であった。
6.2 g of the dried algal cells were crushed by a hiscotron in a mixed solvent of chloroform / methanol = 1: 1 (weight) and then extracted to obtain 0.5 g of oil. The extracted oil was developed by thin layer chromatography (TLC) using a silica gel plate with a mixed solvent of chloroform / methanol / acetic acid, and separated into a polar lipid fraction and a neutral lipid fraction. Then, each spot was scraped off from this silica gel plate, and chloroform / methanol = 1:
When re-extracted with 1 (weight) mixed solvent, the polar lipid content was 52% by weight and the neutral lipid content was 48% by weight.
Among polar lipids, phospholipids are 30% and glycolipids are 40%.
% And other were 30%.

【0016】また、抽出油分200mgに硫酸/メタノー
ル混液約5mlを加えて湯浴中で1.5時間還流し、メチ
ルエステル化した後、これにヘキサンおよび水各5mlを
加えて抽出し、脂肪酸組成をガスクロマトグラフィー
(GLC)で分析したところ、総脂肪酸中のDHA含量
は46重量%であった。さらに上記極性脂質の構成脂肪
酸組成を同様に処理しGLC分析した結果、極性脂質中
の構成脂肪酸のうちDHA含量は70重量%であった。
Further, to 200 mg of extracted oil, about 5 ml of a sulfuric acid / methanol mixture was added and refluxed for 1.5 hours in a water bath, methyl esterification was performed, and then 5 ml of hexane and 5 ml of water were added for extraction to obtain a fatty acid composition. When analyzed by gas chromatography (GLC), the DHA content in the total fatty acids was 46% by weight. Further, the constituent fatty acid composition of the polar lipid was similarly treated and subjected to GLC analysis. As a result, the content of DHA in the constituent fatty acid in the polar lipid was 70% by weight.

【0017】[0017]

【表1】 [Table 1]

【0018】 *ビタミンミックス水溶液 ビオチン : 0.003g/リットル−溶液 チアミン : 1.000 〃 **メタルミックス水溶液 Na2 EDTA : 1.00 g/リットル−溶液 FeCl3 ・6H2 O : 0.05 〃 H3 BO3 : 1.00 〃 MnCl2 ・4H2 O : 0.15 〃 ZnCl2 : 0.01 〃 CoCl2 ・6H2 O : 0.005 〃 [0018] * vitamin mix aqueous solution of biotin: 0.003g / liter - solution Thiamine: 1.000 〃 ** metal mix aqueous solution of Na 2 EDTA: 1.00 g / liter - solution FeCl 3 · 6H 2 O: 0.05 〃 H 3 BO 3: 1.00 〃 MnCl 2 · 4H 2 O: 0.15 〃 ZnCl 2: 0.01 〃 CoCl 2 · 6H 2 O: 0.005 〃

【0019】比較例1 実施例1と同じ藻株(ATCC30336)を、表1の
組成の培地3リットルに植えつけ、30℃にて、pHを
6.8に調節しながらジャーファーメンターで通気培養
した。培養中は食塩濃度を調節せず、培養開始後124
時間目に培養藻体を遠心分離して集め、凍結乾燥して乾
燥藻体を60g得た。この乾燥藻体6.0gをクロロホ
ルム/メタノール=1:1(重量)混合溶媒にて抽出
し、0.75gの油分を得た。抽出油分を実施例1と同
様に分析したところ、極性脂質含量:25重量%、中性
脂質含量:75重量%であった。また、抽出油分の総脂
肪酸中のDHA含量は18重量%であり、極性脂質の構
成脂肪酸中のDHA含量は45重量%であった。
Comparative Example 1 The same algae strain (ATCC30336) as in Example 1 was inoculated in 3 liters of the medium having the composition shown in Table 1, and aerated with a jar fermenter at 30 ° C. while adjusting the pH to 6.8. did. The salt concentration was not adjusted during the culture, and the
At the time, the cultured algal cells were collected by centrifugation and freeze-dried to obtain 60 g of dried algal cells. This dried alga body 6.0 g was extracted with a chloroform / methanol = 1: 1 (weight) mixed solvent to obtain 0.75 g of an oil component. When the extracted oil was analyzed in the same manner as in Example 1, the polar lipid content was 25% by weight and the neutral lipid content was 75% by weight. The DHA content in the total fatty acids of the extracted oil was 18% by weight, and the DHA content in the constituent fatty acids of the polar lipid was 45% by weight.

【0020】実施例2 トラウストキトリウム アウレウム(Thraustochytrium
aureum )ATCC34304を、表1に示した組成の
培地3リットルに植えつけ、25℃にて、pHを6.8
に調整しながらジャーファーメンターで通気培養した。
培養中、増殖した藻体の湿物重量を経時的に測定し、そ
の増殖曲線から対数増殖中期に相当する、培養開始後1
15時間目に、食塩を20g/1L添加して培地中の食
塩濃度を2重量%上昇させ、さらに24時間培養を継続
した。その後、培養藻体を遠心分離して集め、藻体を凍
結乾燥して乾燥藻体を55g得た。
Example 2 Thraustochytrium
aureum) ATCC34304 was inoculated into 3 liters of a medium having the composition shown in Table 1, and the pH was adjusted to 6.8 at 25 ° C.
Aeration culture was carried out with a jar fermenter while adjusting to.
During the culture, the weight of the wet matter of the grown algal cells was measured over time, and from the growth curve thereof, which corresponds to the middle logarithmic growth phase, 1
At 15 hours, 20 g / 1 L of salt was added to increase the salt concentration in the medium by 2% by weight, and the culture was continued for another 24 hours. Then, the cultured algal cells were collected by centrifugation, and the algal cells were freeze-dried to obtain 55 g of dried algal cells.

【0021】この乾燥藻体5.5gをクロロホルム/メ
タノール=1:1(重量)混合溶媒にて抽出し、0.6
gの油分を得た。さらに抽出油分を実施例1と同様に分
析したところ、極性脂質含量:58重量%、中性脂質含
量:42重量%であった。なお極性脂質のうち、リン脂
質が35%、糖脂質が35%、その他成分が30%であ
った。また、抽出油分の総脂肪酸中のDHA含量は50
重量%であり、極性脂質の構成脂肪酸中のDHA含量は
65重量%であった。
5.5 g of this dried algal cell was extracted with a mixed solvent of chloroform / methanol = 1: 1 (weight) to give 0.6
g oil was obtained. When the extracted oil was analyzed in the same manner as in Example 1, the polar lipid content was 58% by weight and the neutral lipid content was 42% by weight. Of the polar lipids, phospholipid was 35%, glycolipid was 35%, and other components were 30%. In addition, the DHA content in the total fatty acids of the extracted oil is 50
% By weight, and the DHA content in the constituent fatty acids of the polar lipid was 65% by weight.

【0022】比較例2 実施例2を同じ藻株(ATCC34304)を、表1の
組成の培地3リットルに植えつけ、25℃にて、pHを
6.8に調整しながらジャーファーメンターで通気培養
した。培養中は食塩濃度を調節せず、培養開始後139
時間目に培養藻体を遠心分離して集め、凍結乾燥して乾
燥藻体を52g得た。この乾燥藻体5.2gをクロロホ
ルム/メタノール=1:1(重量)混合溶媒にて抽出
し、0.5gの油分を得た。抽出油分を実施例1と同様
に分析したところ、極性脂質含量:30重量%、中性脂
質含量:70重量%であった。また、抽出油分の総脂肪
酸中のDHA含量は22重量%であり、極性脂質の構成
脂肪酸中のDHA含量は50重量%であった。
Comparative Example 2 The same algae strain as in Example 2 (ATCC34304) was inoculated in 3 liters of a medium having the composition shown in Table 1, and aerated at 25 ° C. with a jar fermenter while adjusting the pH to 6.8. did. The salt concentration was not adjusted during the culture, and 139 after the start of the culture.
At the time, the cultured algal cells were collected by centrifugation and freeze-dried to obtain 52 g of dried algal cells. 5.2 g of this dried algal cell was extracted with a mixed solvent of chloroform / methanol = 1: 1 (weight) to obtain 0.5 g of an oil component. When the extracted oil was analyzed in the same manner as in Example 1, the polar lipid content was 30% by weight and the neutral lipid content was 70% by weight. The DHA content in the total fatty acids of the extracted oil was 22% by weight, and the DHA content in the constituent fatty acids of the polar lipid was 50% by weight.

【0023】実施例3 クリプセコディニウム コーニー(Crypthecodinium co
hnii)ATCC30336を、実施例1と同条件下で培
養し、培養開始後100時間目に食塩を30g/1L添
加して培地中の食塩濃度を3重量%上昇させ、さらに2
4時間培養を継続した。その後、実施例1と同様の方法
で処理し、乾燥藻体55gを得、その5.5gから0.
4gの油分を得た。この油分中の極性脂質含量:60重
量%、中性脂質含量:40重量%であった。また、抽出
油分の総脂肪酸中のDHA含量は46重量%であり、極
性脂質の構成脂肪酸中のDHA含量は74重量%であっ
た。
EXAMPLE 3 Crypthecodinium co
hnii) ATCC30336 was cultivated under the same conditions as in Example 1 and 100 g of the culture was started to add 30 g / 1 L of salt to increase the salt concentration in the medium by 3% by weight, and further 2
Culture was continued for 4 hours. Thereafter, the same treatment as in Example 1 was carried out to obtain 55 g of dried algae, from 5.5 g of which was 0.5.
4 g of oil was obtained. The polar lipid content in this oil content was 60% by weight, and the neutral lipid content was 40% by weight. The DHA content in the total fatty acids of the extracted oil was 46% by weight, and the DHA content in the constituent fatty acids of the polar lipid was 74% by weight.

【0024】実施例4 実施例3において、定常期に相当する培養開始後130
時間目に食塩を3g/L添加すること以外はすべて同じ
条件で処理し、乾燥藻体80gを得、その8.0gから
0.8gの油分を得た。この油分中の極性脂質含量:5
1重量%、中性脂質含量:49重量%であった。また、
抽出油分の総脂肪酸中のDHA含量は45重量%であ
り、極性脂質の構成脂肪酸中のDHA含量は70重量%
であった。
Example 4 In Example 3, 130 after the start of culture corresponding to the stationary phase.
All were treated under the same conditions except that 3 g / L of sodium chloride was added at the time to obtain 80 g of dried alga bodies, and 8.0 g to 0.8 g of oil was obtained. Content of polar lipids in this oil: 5
The content was 1% by weight and the content of neutral lipid: 49% by weight. Also,
The DHA content in the total fatty acids of the extracted oil is 45% by weight, and the DHA content in the constituent fatty acids of the polar lipid is 70% by weight.
Met.

【0025】[0025]

【発明の効果】本発明によれば、従属栄養で生育しDH
A産生能のある藻類の培養において、任意の培養時期
に、極性脂質濃度が高く、DHAを多く含み、かつDH
A含量の多い極性脂質を多量に蓄積する藻体を得ること
ができるため、効率良く、また製造コストの安いDHA
含有藻類を生産することが可能になる。
INDUSTRIAL APPLICABILITY According to the present invention, DH grown in heterotrophic
In the culture of algae capable of producing A, the polar lipid concentration is high, the amount of DHA is high, and the DH
Since it is possible to obtain algal cells that accumulate a large amount of polar lipids with high A content, DHA is efficient and has a low manufacturing cost.
It becomes possible to produce the contained algae.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI (C12P 7/64 C12R 1:89) (58)調査した分野(Int.Cl.7,DB名) C12N 1/12 BIOSIS(DIALOG) WPI(DIALOG)─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 7 identifier FI (C12P 7/64 C12R 1:89) (58) Fields investigated (Int.Cl. 7 , DB name) C12N 1/12 BIOSIS ( DIALOG) WPI (DIALOG)

Claims (6)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】従属栄養で生育するドコサヘキサエン酸産
生能のある藻類の培養方法であって、 食塩濃度が1.2〜2.5重量%である培養液で培養
し、 培養中に培養液の食塩濃度を1.2〜2.5重量%より
0.1〜10重量%上昇させ、上昇後の食塩濃度で培養を継続する、 ことを特徴とする
ドコサヘキサエン酸含有藻類の培養方法。
1. A method for culturing algae capable of producing docosahexaenoic acid, which grows in heterotrophic culture, comprising culturing in a culture solution having a salt concentration of 1.2 to 2.5% by weight.
And the salt concentration of the culture solution in the culture is raised from 1.2 to 2.5 wt% 0.1 to 10 wt%, culturing is continued for brine concentration after rising, docosahexaenoic acid-containing, characterized in that Method of culturing algae.
【請求項2】食塩濃度を1.2〜2.5重量%より0.
1〜10重量%上昇させる時期が、培養中の藻類の指数
増殖期以降または定常期である請求項1に記載のドコサ
ヘキサエン酸含有藻類の培養方法。
2. A salt concentration of 1.2 to 2.5% by weight and a value of 0.
Time to increase to 10% by weight, the method of culturing docosahexaenoic acid-containing algae according to claim 1 which is exponential growth phase after or stationary phase of algae in culture.
【請求項3】藻類がクリプセコディニウム(Crypthec
odinium)属に属する単細胞藻類である請求項1または2
に記載のドコサヘキサエン酸含有藻類の培養方法。
3. The algae, chestnut-flops Seco di chloride (Crypthec
A single cell alga belonging to the genus odinium).
The method for culturing algae containing docosahexaenoic acid according to 1.
【請求項4】従属栄養で生育するドコサヘキサエン酸産4. Docosahexaenoic acid grown in heterotrophic
生能のある藻類を培養して得られるドコサヘキサエン酸Docosahexaenoic acid obtained by culturing viable algae
含有藻類の生産方法であって、A method for producing algae containing: 食塩濃度が1.2〜2.5重量%である培養液で培養Cultivated in a culture solution with a salt concentration of 1.2 to 2.5% by weight
し、Then 培養中に培養液の食塩濃度を1.2〜2.5重量%よりDuring cultivation, the salt concentration of the culture solution should be 1.2-2.5% by weight.
0.1〜10重量%上昇させ、0.1 to 10% by weight increase, 上昇後の食塩濃度で培養を継続する、ことを特徴とするIt is characterized in that the culture is continued at the increased salt concentration.
ドコサヘキサエン酸含有藻類の生産方法。A method for producing algae containing docosahexaenoic acid.
【請求項5】食塩濃度を1.2〜2.5重量%より0.5. A salt concentration of 1.2 to 2.5% by weight and a value of 0.
1〜10重量%上昇させる時期が、培養中の藻類の指数The time to increase 1 to 10% by weight is the index of algae in culture
増殖期以降または定常期である請求項4に記載のドコサThe docosa according to claim 4, which is after the growth phase or in the stationary phase.
ヘキサエン酸含有藻類の生産方法。Method for producing hexaenoic acid-containing algae.
【請求項6】藻類が、クリプセコディニウム(6. The algae is krypsecodinium ( CrypthecCrypthec
odiniumodinium )属に属する単細胞藻類である請求項4または) A unicellular alga belonging to the genus, or
5に記載のドコサヘキサエン酸含有藻類の生産方法。5. The method for producing an alga containing docosahexaenoic acid according to 5.
JP24885093A 1993-09-09 1993-09-09 Method for culturing algae containing docosahexaenoic acid Expired - Fee Related JP3506740B2 (en)

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