JPH0775556A - Culture of alga containing docosahexaenoic acid - Google Patents
Culture of alga containing docosahexaenoic acidInfo
- Publication number
- JPH0775556A JPH0775556A JP5248849A JP24884993A JPH0775556A JP H0775556 A JPH0775556 A JP H0775556A JP 5248849 A JP5248849 A JP 5248849A JP 24884993 A JP24884993 A JP 24884993A JP H0775556 A JPH0775556 A JP H0775556A
- Authority
- JP
- Japan
- Prior art keywords
- culture
- algae
- alga
- docosahexaenoic acid
- dha
- 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
- MBMBGCFOFBJSGT-KUBAVDMBSA-N all-cis-docosa-4,7,10,13,16,19-hexaenoic acid Chemical compound CC\C=C/C\C=C/C\C=C/C\C=C/C\C=C/C\C=C/CCC(O)=O MBMBGCFOFBJSGT-KUBAVDMBSA-N 0.000 title claims abstract description 38
- 235000020669 docosahexaenoic acid Nutrition 0.000 title claims abstract description 32
- 229940090949 docosahexaenoic acid Drugs 0.000 title claims abstract description 6
- 230000012010 growth Effects 0.000 claims abstract description 18
- 238000000034 method Methods 0.000 claims abstract description 11
- 241000195493 Cryptophyta Species 0.000 claims description 31
- 238000012258 culturing Methods 0.000 claims description 16
- 238000012136 culture method Methods 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 8
- 230000003698 anagen phase Effects 0.000 abstract description 4
- 230000035425 carbon utilization Effects 0.000 abstract description 2
- 241000199912 Crypthecodinium cohnii Species 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 22
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 15
- 235000014113 dietary fatty acids Nutrition 0.000 description 8
- 229930195729 fatty acid Natural products 0.000 description 8
- 239000000194 fatty acid Substances 0.000 description 8
- 150000004665 fatty acids Chemical class 0.000 description 8
- 239000000243 solution Substances 0.000 description 8
- 239000000203 mixture Substances 0.000 description 7
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 239000007864 aqueous solution Substances 0.000 description 6
- 241000199913 Crypthecodinium Species 0.000 description 5
- 238000005119 centrifugation Methods 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 239000003925 fat Substances 0.000 description 4
- 235000019197 fats Nutrition 0.000 description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- YBJHBAHKTGYVGT-ZKWXMUAHSA-N (+)-Biotin Chemical compound N1C(=O)N[C@@H]2[C@H](CCCCC(=O)O)SC[C@@H]21 YBJHBAHKTGYVGT-ZKWXMUAHSA-N 0.000 description 2
- 241000200158 Amphidinium Species 0.000 description 2
- 241000321369 Cephalopholis fulva Species 0.000 description 2
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- 230000005526 G1 to G0 transition Effects 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 241000144181 Thraustochytrium aureum Species 0.000 description 2
- 238000005273 aeration Methods 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 229940088594 vitamin Drugs 0.000 description 2
- 229930003231 vitamin Natural products 0.000 description 2
- 235000013343 vitamin Nutrition 0.000 description 2
- 239000011782 vitamin Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 241000195628 Chlorophyta Species 0.000 description 1
- 241000199914 Dinophyceae Species 0.000 description 1
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 241001501885 Isochrysis Species 0.000 description 1
- 241000199911 Peridinium Species 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- 229930006000 Sucrose Natural products 0.000 description 1
- JZRWCGZRTZMZEH-UHFFFAOYSA-N Thiamine Natural products CC1=C(CCO)SC=[N+]1CC1=CN=C(C)N=C1N JZRWCGZRTZMZEH-UHFFFAOYSA-N 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 1
- 229960002685 biotin Drugs 0.000 description 1
- 235000020958 biotin Nutrition 0.000 description 1
- 239000011616 biotin Substances 0.000 description 1
- 239000007853 buffer solution Substances 0.000 description 1
- 229940041514 candida albicans extract Drugs 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 239000012533 medium component Substances 0.000 description 1
- 239000013028 medium composition Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000004702 methyl esters Chemical class 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000012046 mixed solvent Substances 0.000 description 1
- 235000014593 oils and fats Nutrition 0.000 description 1
- 230000001766 physiological effect Effects 0.000 description 1
- 102220201851 rs143406017 Human genes 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 239000005720 sucrose Substances 0.000 description 1
- 235000019157 thiamine Nutrition 0.000 description 1
- KYMBYSLLVAOCFI-UHFFFAOYSA-N thiamine Chemical compound CC1=C(CCO)SCN1CC1=CN=C(C)N=C1N KYMBYSLLVAOCFI-UHFFFAOYSA-N 0.000 description 1
- 229960003495 thiamine Drugs 0.000 description 1
- 239000011721 thiamine Substances 0.000 description 1
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 1
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 1
- 150000003722 vitamin derivatives Chemical class 0.000 description 1
- 239000012138 yeast extract Substances 0.000 description 1
Abstract
Description
【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を効率良
く、高濃度に蓄積せしめる前記藻類の培養法に関する。The present invention relates to the cultivation of algae capable of producing docosahexaenoic acid (hereinafter abbreviated as DHA), which grows under heterotrophic conditions, and efficiently accumulates DHA in the algal body at a high concentration. 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、1970年)、またイソクリシス(Isochrysis)属
のDHA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D
HA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1679〜1683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 (Amphidinium) and the like have been reported (J. Protozoal, Volume 17 (2), 213-219).
Page, 1970), and the production of DHA-producing algae belonging to the genus Isochrysis has been attempted (Japanese Patent Laid-Open No. 4-410).
346760). However, all of them are algae that grow autotrophically, and not only the culture cost is high, but the oil content in the alga body is low, and the satisfactory D
It has not been possible to produce HA-containing fats and oils. On the other hand, algae belonging to the genus Crypthecodinium are known as DHA-producing algae that grow by heterotrophy (Phytochemistry, Vol. 27 (6),
Pp. 1679-1683, 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の
油脂分の蓄積方法として、培地組成のC/N比率の調
節、培地の更新等の、主に培地成分の窒素源の調整によ
る培養管理方法が用いられてきた(例えば「油脂」、第
24巻(5)、第126〜135頁、1971年)。し
かし、これらの方法は、微生物や藻類の生育状態によっ
て油脂類を蓄積するステージの開始時間にばらつきが出
たり、培地の更新の際の雑菌汚染、菌体あるいは藻体収
量や油分含量が不安定になる等の問題点があり、工業的
生産の点からは望ましい方法ではなかった。Conventionally, in the production of fats and oils by microorganisms and algae that grow heterotrophically, methods for accumulating fats and oils in fungi or algae include adjusting the C / N ratio of the medium composition and updating the medium. A culture control method has been used mainly by adjusting the nitrogen source of the medium components (for example, "oil and fat", Vol. 24 (5), 126-135, 1971). However, in these methods, the start time of the stage of accumulating oils and fats varies depending on the growth state of microorganisms and algae, contamination of various bacteria at the time of renewal of the medium, the yield of microbial cells or algae and the oil content are unstable. However, it was not a desirable method from the viewpoint of industrial production.
【0004】[0004]
【発明が解決しようとする課題】これまでのDHA産生
藻類の培養においては、上記のような問題点があり、効
率が良く、生産コストの低いDHA含有藻類の生産は困
難であった。したがって本発明の目的は、従属栄養で生
育するDHA産生藻類を培養するにあたり、油分および
DHAを効率的に前記藻類の細胞内に高濃度に蓄積せし
めることのできる培養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。In the conventional culture of DHA-producing algae, there are the above problems, and it has been difficult to produce DHA-containing algae which are efficient and have a low production cost. Therefore, an object of the present invention is to provide a culture method capable of efficiently accumulating oil and DHA at a high concentration in the cells of the alga in culturing a DHA-producing alga growing in heterotrophic, Consequently, it is to provide an efficient industrial method for producing DHA-containing algae with low production cost.
【0005】[0005]
【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、培地のpHを上昇させることにより、任意
の培養時期に、藻体中の油分および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DH
A産生能のある藻類を培養するにあたり、培養中、培養
液のpHを藻類の生育に好適なpHより0.1〜7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法に
係わるものである。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 it is possible to remarkably increase the oil content and DHA content in the alga at any culture time by increasing the pH of the medium, and completed the present invention. That is, the present invention relates to DH grown in heterotrophic
In culturing an alga capable of producing A, during the culturing, the pH of the culture solution is set to a value 0.1 to 7 higher than the pH suitable for the growth of the alga, and the culturing is performed to the alga. It is related.
【0006】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 1
992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(Crypthecod
inium cohnii)、トラウストキトリウム アウレウム
(Thraustochytrium 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
30336、同50052、また後者ではATCC28
211、同34304等がある。The alga used in the present invention is an alga that can be heterotrophically cultivated and capable of producing and accumulating DHA in the alga body, and its species or strain is not particularly limited. Examples of algae corresponding to this include "Microbiology Dictionary 1
According to "1992 edition" (Gihodo Publishing), Crypthecodium corny (Crypthecod) belonging to the genus Chlorophyta, Dinoflagellate, Peridinium, and genus Crypthecodinium.
inium cohnii), and Thraustochytrium aureum. These algae are from the American Type Culture Collection (US,
Easily available from algae research institutes such as the abbreviation ATCC),
For example, ATCC30021, 30334, 30336, 50052 in the former, and ATCC28 in the latter.
211, 34304 and the like.
【0007】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pHを
上昇させる。すなわち、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、この
pHを5〜7好ましくは6〜7とし、20〜35℃好ま
しくは25〜32℃で、好適にはその藻類の増殖曲線に
おける指数増殖中期ないし定常期まで培養する。この初
期の培養時のpHおよび温度がこの範囲を外れると、藻
類の増殖が阻害される傾向が大きくなる。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pH
値を上昇せしめる。このときのpH上昇値は、その藻類
の生育に好適なpHよりも0.1〜7好ましくは1〜4
高い値に設定し、そのpH値で培養を継続する。pHの
上昇幅が0.1に満たないと藻体中の油分およびDHA
含量を増加せしめることができず、7を超えてpH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。In the practice of 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 pH of the medium is raised at an arbitrary time. That is, using a natural or artificial seawater medium, or a medium containing a carbon source such as glucose and sucrose, a nitrogen source such as an ammonium salt, a yeast extract, an amino acid or a salt thereof, various vitamins and minerals, and adjusting the pH to 5 The culture is preferably carried out at 7 to 6 and preferably at 20 to 35 ° C., preferably 25 to 32 ° C., suitably from the middle stage of exponential growth to the stationary phase in the growth curve of the alga. If the pH and temperature during this initial culture deviate from these ranges, the growth of algae tends to be inhibited. Then, at any culture time, preferably at or after the mid-exponential phase, for example, any phase from the logarithmic growth phase to the stationary phase, the pH of the culture solution
Increase the value. The pH increase value at this time is 0.1 to 7 preferably 1 to 4 than the pH suitable for the growth of the algae.
Set to a higher value and continue culturing at that pH value. If the increase in pH is less than 0.1, the oil content and DHA in the alga
The content cannot be increased, and raising the pH above 7 is not preferable because it inhibits the growth of algae.
【0008】かかる培養液のpH上昇は、例えば水酸化
ナトリウム、水酸化カリウム等のアルカリ水溶液、ある
いは適当な緩衝液の添加によって行うことができるが、
本発明はこれらに限定されるものではない。またアルカ
リ水溶液の濃度は、0.1〜10規定として用いるのが
よい。培地のpHを上昇させる時期は、前記のとおり任
意の培養時でよく、例えば藻体の増殖量が所望の量に達
したとき、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、例えばpH
0.1〜1程度の若干の上昇ならばさしつかえないが、
急激な大幅上昇は藻類の増殖自体を阻害する場合があ
る。The pH of the culture solution can be increased by adding an alkaline aqueous solution such as sodium hydroxide or potassium hydroxide, or by adding an appropriate buffer solution.
The present invention is not limited to these. The concentration of the alkaline aqueous solution is preferably 0.1 to 10N. The time for raising the pH of the medium may be any culture as described above, for example, when the growth amount of the alga body reaches a desired amount, or when it is necessary in the work of the culture process, etc. It is any stage after the middle stage of exponential growth of algae. In the culture stage before this, for example, pH
If it is a slight rise of about 0.1 to 1, it will be okay,
A sharply large rise may inhibit the growth of algae itself.
【0009】かくしてpH値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油分およびDHA含量の高い藻
体を得ることができる。なお、pH上昇後の培養時間が
3時間に満たないと藻体中のDHA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。本発明において、培地のpHを上昇させて培養して
得られる藻体の脂質濃度は、培養時間やpH上昇を開始
した時期等によっても異なるが、例えばpH上昇開始後
およそ24時間で、油分含量が15〜45重量%、油分
の構成脂肪酸のうちDHA含量は30〜50重量%とな
る。これに対し、pHを上昇させずに培養を行うと、油
分含量は10〜15重量%、同じく構成脂肪酸中のDH
A含量は20重量%程度にとどまる。[0009] In this way, although it depends on the kind of algae in the culture solution of which the pH value is raised, it is usually cultivated for about 3 to 50 hours to obtain an algal body having a high oil content and DHA content, which is the object of the present invention. it can. If the culture time after raising the pH is less than 3 hours, the DHA content in the alga is small, and conversely, if the culture is continued for a long time exceeding 50 hours, the alga body yield is reduced. In the present invention, the lipid concentration of the algal cells obtained by culturing by raising the pH of the medium varies depending on the culturing time and the timing of starting the pH increase. For example, the oil content is about 24 hours after the start of the pH increase. Is 15 to 45% by weight, and the DHA content of the constituent fatty acids of the oil is 30 to 50% by weight. On the other hand, when the culture is carried out without increasing the pH, the oil content is 10 to 15% by weight, and DH in the constituent fatty acids is the same.
The A content remains around 20% by weight.
【0010】[0010]
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、1N水酸化ナトリウム水溶液を用いて培地のp
Hを6.8から10.0に上昇させ、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60g得た。なお、この
乾燥藻体6.0gをクロロホルム/メタノール=1:1
(重量)混合溶媒中でヒスコトロンにより細胞破砕後抽
出し、1.8gの油分を得た。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
ラフィーで分析したところ、総脂肪酸中のDHA含量は
40重量%であった。なお藻体中の油分含量は30重量
%であった。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, 100 hours after the start of the culture, which corresponds to the mid-logarithmic growth phase, the p of the medium was diluted with 1N sodium hydroxide aqueous solution.
H was increased from 6.8 to 10.0 and the culture was continued for another 24 hours. After that, the cultured algal cells are collected by centrifugation,
The algal cells were freeze-dried to obtain 60 g of dried algal cells. It should be noted that 6.0 g of this dried algal cell was mixed with chloroform / methanol = 1: 1.
(Weight) After crushing the cells with a hyscotron in a mixed solvent, extraction was performed to obtain 1.8 g of oil. About 5 ml of sulfuric acid / methanol mixture was added to 200 mg of extracted oil, and the mixture was refluxed for 1.5 hours in a hot water bath to make methyl ester, and then 5 ml of hexane and 5 ml of water were added for extraction, and the fatty acid composition was analyzed by gas chromatography. When analyzed, the DHA content in the total fatty acids was 40% by weight. The oil content in the algal cells was 30% by weight.
【0011】[0011]
【表1】 [Table 1]
【0012】 *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 〃[0012] * 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 〃
【0013】実施例2 クリプセコディニウム コーニー(Crypthecodinium co
hnii)ATCC30021を、実施例1と同条件下で培
養し、その対数増殖終期に相当する培養開始後125時
間目に1N水酸化ナトリウム水溶液を用いて培地のpH
を6.8から11.0に上昇させ、さらに36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、さ
らに凍結乾燥して乾燥藻体を55g得た。この乾燥藻体
の一部を用い、実施例1と同様に油分を抽出し、その総
脂肪酸中のDHA含量を分析したところ、油分含量は3
3重量%、総脂肪酸中のDHA含量は39重量%であっ
た。Example 2 Crypthecodinium co
hnii) ATCC30021 was cultivated under the same conditions as in Example 1, and the pH of the medium was adjusted 125 hours after the start of culture corresponding to the end of logarithmic growth thereof with a 1N aqueous sodium hydroxide solution.
Was increased from 6.8 to 11.0, and the culture was continued for further 36 hours. Then, the cultured algal cells were collected by centrifugation and freeze-dried to obtain 55 g of dried algal cells. Using a part of the dried algal cells, the oil content was extracted in the same manner as in Example 1, and the DHA content in the total fatty acid was analyzed. As a result, the oil content was 3
The content of DHA in the total fatty acids was 3% by weight and 39% by weight.
【0014】比較例1 クリプセコディニウム コーニー(Crypthecodinium co
hnii)ATCC30336を、培地のpHを6.8に維
持したまま、それ以外は実施例1と同条件で124時間
培養した。その後、培養藻体を遠心分離して集め、藻体
を凍結乾燥したところ乾燥藻体は20gしか得られなか
った。さらにこの乾燥藻体の一部を用い、実施例1と同
様に分析した結果、油分含量およびDHA含量はいずれ
も10重量%と低いものであった。Comparative Example 1 Crypthecodinium coney
hnii) ATCC30336 was cultivated for 124 hours under the same conditions as in Example 1 except that the pH of the medium was maintained at 6.8. Then, the cultured algal cells were collected by centrifugation and freeze-dried to obtain only 20 g of dried algal cells. Further, using a part of the dried algal cells, the same analysis as in Example 1 revealed that the oil content and the DHA content were both as low as 10% by weight.
【0015】実施例3 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終期に相当する培養開始後13
8時間目に、1N水酸化ナトリウム水溶液を用いて培地
のpHを6.8から10.0に上昇させ、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65g得た。なお、
この乾燥藻体の一部を用い、実施例1と同様の方法によ
り求めた藻体中の油分含量は35重量%、また総脂肪酸
中のDHA含量は50重量%であった。Example 3 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 with time, and from the growth curve thereof, the end of the logarithmic growth corresponding to the start of the culture 13
At 8 hours, the pH of the medium was raised from 6.8 to 10.0 using a 1N aqueous sodium hydroxide solution, and the culture was continued for another 24 hours. Thereafter, the cultured algal cells were collected by centrifugation, and the algal cells were freeze-dried to obtain 65 g of dried algal cells. In addition,
Using a part of this dried alga body, the oil content in the alga body determined by the same method as in Example 1 was 35% by weight, and the DHA content in the total fatty acids was 50% by weight.
【0016】実施例4 実施例3と同じ藻株(ATCC34304)を、実施例
3と同条件下で培養し、その対数増殖中期に相当する培
養開始後115時間目に、1N水酸化ナトリウム水溶液
を用いて培地のpHを6.8から10.0に上昇させ、
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56g
得た。この乾燥藻体の一部を用い、実施例1と同様の方
法により求めた藻体中の油分含量は30重量%、また総
脂肪酸中のDHA含量は51重量%であった。Example 4 The same alga strain (ATCC34304) as in Example 3 was cultivated under the same conditions as in Example 3, and 1N sodium hydroxide aqueous solution was added at 115 hours after the start of culture corresponding to the middle logarithmic growth phase. Used to raise the pH of the medium from 6.8 to 10.0,
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 56 g of dried algal cells.
Obtained. Using a part of this dried alga, the oil content in the alga determined by the same method as in Example 1 was 30% by weight, and the DHA content in the total fatty acids was 51% by weight.
【0017】[0017]
【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、藻体中に油分およびDHAを多く含む藻類細胞を得
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となる。INDUSTRIAL APPLICABILITY According to the present invention, DH grown in heterotrophic
In culturing an alga capable of producing A, since it is possible to obtain an algal cell containing a large amount of oil and DHA in the algal body at an arbitrary culturing time, it is possible to efficiently produce a DHA-containing alga with low production cost. Is possible.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 (C12P 7/64 C12R 1:89) ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification number Office reference number FI technical display location (C12P 7/64 C12R 1:89)
Claims (4)
産生能のある藻類を培養するにあたり、培養中、培養液
のpHを前記藻類の生育に好適なpHより0.1〜7高
い値に設定して培養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法。1. When culturing algae capable of producing docosahexaenoic acid that grows in heterotrophic culture, the pH of the culture solution is set to a value 0.1 to 7 higher than the pH suitable for growth of the algae during culturing. A method for culturing algae containing docosahexaenoic acid, which comprises culturing.
請求項1に記載の培養法。2. The culture method according to claim 1, wherein the pH suitable for the growth of algae is 5 to 7.
中期以降である請求項1または2に記載の培養法。3. The culture method according to claim 1 or 2, wherein the time of increasing the pH value is after the middle exponential growth of the culture.
odinium )属に属する単細胞藻類である請求項1ないし
3のいずれかに記載の培養法。4. The algae is Crypthec
The culturing method according to any one of claims 1 to 3, which is a single cell alga belonging to the genus odinium).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5248849A JPH0775556A (en) | 1993-09-09 | 1993-09-09 | Culture of alga containing docosahexaenoic acid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5248849A JPH0775556A (en) | 1993-09-09 | 1993-09-09 | Culture of alga containing docosahexaenoic acid |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0775556A true JPH0775556A (en) | 1995-03-20 |
Family
ID=17184342
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5248849A Pending JPH0775556A (en) | 1993-09-09 | 1993-09-09 | Culture of alga containing docosahexaenoic acid |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0775556A (en) |
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