JPH0532019B2 - - Google Patents
Info
- Publication number
- JPH0532019B2 JPH0532019B2 JP16004384A JP16004384A JPH0532019B2 JP H0532019 B2 JPH0532019 B2 JP H0532019B2 JP 16004384 A JP16004384 A JP 16004384A JP 16004384 A JP16004384 A JP 16004384A JP H0532019 B2 JPH0532019 B2 JP H0532019B2
- Authority
- JP
- Japan
- Prior art keywords
- culture
- cells
- hours
- euglena
- concentration
- 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.)
- Expired - Lifetime
Links
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 30
- 241000195620 Euglena Species 0.000 claims description 23
- 238000000034 method Methods 0.000 claims description 17
- 229910052757 nitrogen Inorganic materials 0.000 claims description 15
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 12
- 229910052799 carbon Inorganic materials 0.000 claims description 12
- 238000012258 culturing Methods 0.000 claims description 9
- 239000001963 growth medium Substances 0.000 claims description 6
- 230000003698 anagen phase Effects 0.000 claims description 3
- 210000004027 cell Anatomy 0.000 description 49
- 238000012136 culture method Methods 0.000 description 11
- 239000002609 medium Substances 0.000 description 11
- 238000003306 harvesting Methods 0.000 description 6
- 230000001954 sterilising effect Effects 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 150000001413 amino acids Chemical class 0.000 description 3
- 229920002678 cellulose Polymers 0.000 description 3
- 239000001913 cellulose Substances 0.000 description 3
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- 235000018102 proteins Nutrition 0.000 description 3
- 102000004169 proteins and genes Human genes 0.000 description 3
- 108090000623 proteins and genes Proteins 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 241000195493 Cryptophyta Species 0.000 description 2
- 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 2
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 2
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 2
- 235000011130 ammonium sulphate Nutrition 0.000 description 2
- 210000000170 cell membrane Anatomy 0.000 description 2
- 239000006285 cell suspension Substances 0.000 description 2
- 239000000306 component Substances 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- RMRCNWBMXRMIRW-BYFNXCQMSA-M cyanocobalamin Chemical compound N#C[Co+]N([C@]1([H])[C@H](CC(N)=O)[C@]\2(CCC(=O)NC[C@H](C)OP(O)(=O)OC3[C@H]([C@H](O[C@@H]3CO)N3C4=CC(C)=C(C)C=C4N=C3)O)C)C/2=C(C)\C([C@H](C/2(C)C)CCC(N)=O)=N\C\2=C\C([C@H]([C@@]/2(CC(N)=O)C)CCC(N)=O)=N\C\2=C(C)/C2=N[C@]1(C)[C@@](C)(CC(N)=O)[C@@H]2CCC(N)=O RMRCNWBMXRMIRW-BYFNXCQMSA-M 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 150000004676 glycans Chemical class 0.000 description 2
- 230000003834 intracellular effect Effects 0.000 description 2
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 2
- 238000010899 nucleation Methods 0.000 description 2
- 235000015097 nutrients Nutrition 0.000 description 2
- 229920001282 polysaccharide Polymers 0.000 description 2
- 239000005017 polysaccharide Substances 0.000 description 2
- 238000004659 sterilization and disinfection Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 235000013343 vitamin Nutrition 0.000 description 2
- 239000011782 vitamin Substances 0.000 description 2
- 229940088594 vitamin Drugs 0.000 description 2
- 229930003231 vitamin Natural products 0.000 description 2
- BJEPYKJPYRNKOW-REOHCLBHSA-N (S)-malic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O BJEPYKJPYRNKOW-REOHCLBHSA-N 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 241000195649 Chlorella <Chlorellales> Species 0.000 description 1
- ZGTMUACCHSMWAC-UHFFFAOYSA-L EDTA disodium salt (anhydrous) Chemical compound [Na+].[Na+].OC(=O)CN(CC([O-])=O)CCN(CC(O)=O)CC([O-])=O ZGTMUACCHSMWAC-UHFFFAOYSA-L 0.000 description 1
- 241000195619 Euglena gracilis Species 0.000 description 1
- 241000195623 Euglenida Species 0.000 description 1
- 241000206602 Eukaryota Species 0.000 description 1
- 239000007836 KH2PO4 Substances 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 241000080590 Niso Species 0.000 description 1
- 229920002984 Paramylon Polymers 0.000 description 1
- KDYFGRWQOYBRFD-UHFFFAOYSA-N Succinic acid Natural products OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 235000011054 acetic acid Nutrition 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- BJEPYKJPYRNKOW-UHFFFAOYSA-N alpha-hydroxysuccinic acid Natural products OC(=O)C(O)CC(O)=O BJEPYKJPYRNKOW-UHFFFAOYSA-N 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 235000021120 animal protein Nutrition 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- KDYFGRWQOYBRFD-NUQCWPJISA-N butanedioic acid Chemical compound O[14C](=O)CC[14C](O)=O KDYFGRWQOYBRFD-NUQCWPJISA-N 0.000 description 1
- 235000010216 calcium carbonate Nutrition 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 230000032823 cell division Effects 0.000 description 1
- 210000002421 cell wall Anatomy 0.000 description 1
- 230000001413 cellular effect Effects 0.000 description 1
- 210000003763 chloroplast Anatomy 0.000 description 1
- 235000015165 citric acid Nutrition 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 229960002104 cyanocobalamin Drugs 0.000 description 1
- 235000000639 cyanocobalamin Nutrition 0.000 description 1
- 239000011666 cyanocobalamin Substances 0.000 description 1
- 150000002016 disaccharides Chemical class 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000012010 growth Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000004677 hydrates Chemical class 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000004310 lactic acid Substances 0.000 description 1
- 235000014655 lactic acid Nutrition 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052943 magnesium sulfate Inorganic materials 0.000 description 1
- 235000019341 magnesium sulphate Nutrition 0.000 description 1
- 239000001630 malic acid Substances 0.000 description 1
- 235000011090 malic acid Nutrition 0.000 description 1
- 238000010907 mechanical stirring Methods 0.000 description 1
- 239000012533 medium component Substances 0.000 description 1
- 229910000402 monopotassium phosphate Inorganic materials 0.000 description 1
- 235000019796 monopotassium phosphate Nutrition 0.000 description 1
- 150000002772 monosaccharides Chemical class 0.000 description 1
- 235000008935 nutritious Nutrition 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 150000003904 phospholipids Chemical class 0.000 description 1
- GNSKLFRGEWLPPA-UHFFFAOYSA-M potassium dihydrogen phosphate Chemical compound [K+].OP(O)([O-])=O GNSKLFRGEWLPPA-UHFFFAOYSA-M 0.000 description 1
- 230000035755 proliferation Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 235000002639 sodium chloride Nutrition 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- DPJRMOMPQZCRJU-UHFFFAOYSA-M thiamine hydrochloride Chemical compound Cl.[Cl-].CC1=C(CCO)SC=[N+]1CC1=CN=C(C)N=C1N DPJRMOMPQZCRJU-UHFFFAOYSA-M 0.000 description 1
- 229960000344 thiamine hydrochloride Drugs 0.000 description 1
- 235000019190 thiamine hydrochloride Nutrition 0.000 description 1
- 239000011747 thiamine hydrochloride Substances 0.000 description 1
- 210000001519 tissue Anatomy 0.000 description 1
- 235000019155 vitamin A Nutrition 0.000 description 1
- 239000011719 vitamin A Substances 0.000 description 1
- 235000019154 vitamin C Nutrition 0.000 description 1
- 239000011718 vitamin C Substances 0.000 description 1
- 235000019165 vitamin E Nutrition 0.000 description 1
- 239000011709 vitamin E Substances 0.000 description 1
- 150000003722 vitamin derivatives Chemical class 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Description
産業上の利用分野
本発明は、ユーグレナの連続培養方法に関する
ものである。
従来の技術及び問題点
ユーグレナ細胞は、単細胞の真核生物であり、
生物分類学上では、動物および植物の両部門に属
する。細胞構成要素の最大の特徴は、葉緑体を持
つた植物的な面、及び柔らかい細胞膜で覆われて
いるという動物的な面の両面を備えていることで
ある。細胞たんぱく質を構成するアミノ酸は、動
物たんぱく質に類似しているので、栄養価が高
く、また細胞膜は、クロレラ等の藻類がセルロー
スを組織成分とした細胞壁で構成さている点に較
べ、ユーグレナ細胞は、まつたくセルロースを含
まず、柔らかなたんぱく質とリン脂質から構成さ
れているため、消化されやすく、更にビタミン
A、C、E等も、これら藻類に比して、多量に含
むという特徴を有している。従つて、ユーグレナ
は、将来の食用たんぱく源、ビタミン源として有
望視される。
従来行なわれているユーグレナ細胞の培養方法
は、密閉系回分法である。この方法では、まず培
養に必要とされる栄養成分を溶解し、培養槽に所
定量送入し、スチーム、加熱ヒーター等により滅
菌を行なつた後、水道水、工事用水などで培養温
度に冷却する。次いで、あらかじめ他の培養槽で
培養した種細胞を植種し、所定の条件下で最高細
胞数となるまで培養した後、細胞懸濁液を遠心分
離して細胞を収穫する。
この回分培養方法では、ユーグレナの細胞は、
培地適応期間である誘導期を経て、指数関数的に
細胞分裂を行なう対数増殖期に至り、増殖と死滅
の速度が等しい安定期に達し、最高細胞数とな
る。この期間は約4〜5日である。培養前後の滅
菌、収穫、洗浄等を考慮すると、植種から収穫ま
では6〜7日を要し、また収穫後は、再び新培地
を送入し、培地の滅菌から上記ステツプを繰り返
すことが必要である。このため、回分培養方法
は、培養期間に対する細胞収量が少ないという欠
点を有する。
問題点を解決するための手段
本発明は、上記した点に鑑みて種々研究を重ね
た結果、栄養剤溶解液である培地液を別途滅菌
し、連続的にユーグレナの培養槽に流入させ、槽
内に一定時間滞留させた後、細胞懸濁液として流
出させることにより、ユーグレナ細胞を長期に亘
つて連続的に収穫でき、この時の細胞濃度は、回
分培養法での最高細胞濃度に近いものであること
を見出した。本発明は、この知見に基くものであ
る。
即ち、本発明は、細胞濃度が5×106cells/ml
となつた時点から増殖安定期2日目までの期間内
に、炭素濃度1.2〜8.0g/、窒素濃度0.07〜4.5
g/の培地液を平均滞留時間が5〜96時間とな
るように培養槽に送給することを特徴とするユー
グレナの連続培養方法に係る。
本発明方法は、ユーグレナ・グラシリス、ユー
グレナ・ビリデ、ユーグレナ・インタミデイア等
のユーグレノイド及び河川、湖沼等に生育する野
生株等のユーグレナ属のいかなる種にも適用され
る。
本発明に於いては、これらのユーグレナ細胞を
純粋に培養したものを種細胞として用いることが
望ましい。
本発明で使用される培養培地は、回分法による
ものと同様でよく、例えば炭素源として単糖類、
二糖類、多糖類;酢酸、クエン酸、コハク酸、リ
ンゴ酸、乳酸等の有機酸類;メタノール、エタノ
ール等のアルコール類;各種アミノ酸、炭酸ガス
などが用いられ、窒素源として、硫酸アンノニウ
ム、リン酸アンモニウム、アンモニア、各種アミ
ノ酸なとが用いられる。また無機塩類としては、
MgSO4、CaCO3、KH2PO4、Na2EDTA、
FeSO4(NH4)2SO4、MnSO4、ZnSO4、
(NR4)6Mo7O24、CuSO4、NH4VO3、CoSO4、
H3BO3、NiSO4等またはこれらの水和物が用い
られ、ビタミンとしてシアノコバラミン、チアミ
ン塩酸等が用いられる。このような培地の代表例
を第1表に示す。
INDUSTRIAL APPLICATION FIELD The present invention relates to a method for continuous culturing of Euglena. Conventional techniques and problems Euglena cells are unicellular eukaryotes,
In terms of biological taxonomy, it belongs to both the animal and plant categories. The most distinctive feature of cellular components is that they have both a plant-like aspect, in which they have chloroplasts, and an animal-like aspect, in that they are covered with a soft cell membrane. The amino acids that make up cell proteins are similar to animal proteins, so they are highly nutritious.Algae such as Chlorella have cell walls made of cellulose, whereas Euglena cells have cell membranes that are composed of cellulose as a tissue component. Since it does not contain cellulose and is composed of soft proteins and phospholipids, it is easily digested, and it also contains large amounts of vitamins A, C, and E compared to other algae. There is. Therefore, Euglena is seen as a promising future edible protein and vitamin source. The conventional method for culturing Euglena cells is a closed batch method. In this method, the nutrients required for culture are first dissolved, and a predetermined amount is fed into a culture tank. After sterilization using steam, a heating heater, etc., the solution is cooled to culture temperature using tap water, construction water, etc. do. Next, seed cells previously cultured in another culture tank are inoculated, and after culturing under predetermined conditions until the maximum number of cells is reached, the cell suspension is centrifuged to harvest the cells. In this batch culture method, Euglena cells are
After a lag phase, which is a period of medium adaptation, cells reach a logarithmic growth phase in which cells divide exponentially, and then reach a stable phase in which the rate of proliferation and death are equal, reaching the maximum cell number. This period is approximately 4-5 days. Considering sterilization, harvesting, cleaning, etc. before and after cultivation, it takes 6 to 7 days from seeding to harvesting, and after harvesting, it is necessary to introduce a new medium again and repeat the above steps from sterilizing the medium. is necessary. For this reason, the batch culture method has the disadvantage that the cell yield is low for the culture period. Means for Solving the Problems As a result of various studies in view of the above points, the present invention has been developed by separately sterilizing a culture medium, which is a nutrient solution, and continuously flowing it into a Euglena culture tank. Euglena cells can be harvested continuously over a long period of time by retaining them for a certain period of time and then draining them as a cell suspension, and the cell concentration at this time is close to the maximum cell concentration in the batch culture method. I found that. The present invention is based on this knowledge. That is, in the present invention, the cell concentration is 5×10 6 cells/ml.
Within the period from the time when the growth stabilized to the second day, the carbon concentration was 1.2 to 8.0 g/, and the nitrogen concentration was 0.07 to 4.5.
The present invention relates to a method for continuous culturing Euglena, which is characterized in that a medium of 1.5 g/g/g of a medium is fed to a culture tank so that the average residence time is 5 to 96 hours. The method of the present invention is applicable to any species of the genus Euglena, such as euglenoids such as Euglena gracilis, Euglena viride, and Euglena intamideia, and wild strains growing in rivers, lakes, and marshes. In the present invention, it is desirable to use pure cultured Euglena cells as seed cells. The culture medium used in the present invention may be the same as that used in the batch method, for example, monosaccharides as the carbon source,
Disaccharides, polysaccharides; organic acids such as acetic acid, citric acid, succinic acid, malic acid, lactic acid; alcohols such as methanol and ethanol; various amino acids, carbon dioxide gas, etc. are used, and as nitrogen sources, amnonium sulfate, phosphoric acid, etc. Ammonium, ammonia, various amino acids, etc. are used. In addition, as inorganic salts,
MgSO4 , CaCO3 , KH2PO4 , Na2EDTA ,
FeSO 4 (NH 4 ) 2 SO 4 , MnSO 4 , ZnSO 4 ,
(NR 4 ) 6 Mo 7 O 24 , CuSO 4 , NH 4 VO 3 , CoSO 4 ,
H 3 BO 3 , NiSO 4 , etc., or hydrates thereof are used, and cyanocobalamin, thiamine hydrochloride, etc. are used as vitamins. Representative examples of such media are shown in Table 1.
【表】
本発明による培養方法では、ユーグレナの対数
増殖期の中間段階で細胞数濃度が5×106Cells/
mlとなつた時点以降で、細胞数が最高となる安定
期となつて2日目までの期間内に、炭素濃度が
1.2〜8.0g/、窒素濃度が0.07〜4.50g/で
あるあらかじめ滅菌処理した培地液を液ポンプま
たは加圧流出法等によつて培養槽へ連続的に送入
する。この時、培養槽での培地液の平均滞留時間
を5〜96時間の範囲内とすることにより、連続的
にユーグレナ細胞を収穫することができる。炭素
濃度が1.2g/未満では、細胞分裂に必要な炭
素源が不足し、連続培養開始後1〜2日目から培
養槽内の細胞数が急激に低下する。炭素濃度が8
g/をこえると、細胞が炭素源を急速に体内蓄
積し、貯蔵多糖のパラミロンに変換するが、逆に
分裂は極度に阻害され、更に流出液中に炭素源が
残留し、培地コストの経済性から好ましくない。
また、平均滞留時間が5時間未満では、培養槽内
からほとんどが流出し、96時間をこえると、ユー
グレナ細胞の減衰期となり槽内細胞数濃度が5〜
6×106Cells/mlと非常に少なくなるため、得ら
れる細胞収量も、回分培養法でのものと同程度と
なりメリツトがない。
本発明方法では、培地液の平均滞留時間を5〜
96時間として連続培養することにより、従来植種
から収穫まで6〜7日かかつた回分培養法での1
回の収穫量と同程度の量のユーグレナ細胞を5〜
96時間サイクルで連続的に収穫することができ
る。このため、従来の回分法と比較して同一培養
時間で1.5〜10倍量のユーグレナ細胞を得ること
ができ、また、この細胞内タンパク質含有率は、
従来の回分法によるものと同程度となる。
本発明に於いて、他の条件は、連続培養のため
の制限因子とはならにので、通常の培養条件で良
い。好ましい条件は、PH2〜5、温度10〜34℃、
培養液の溶存酸素温度は1ppm以上であり、撹拌
は槽内の細胞が底部に沈着しない程度で行ない、
通気曝気による撹拌で十分な場合には、機械撹拌
はしなくてもよい。
発明の効果
本発明による連続培養方法で、ユーグレナ細胞
を培養することにより、従来の回分式培養方法に
より培養した場合と比較して、同一培養時間で
1.5〜10倍のユーグレナ細胞が得られる。また得
られたユーグレナ細胞の細胞内タンパク質含有率
は、従来のものと同程度である。
実施例
次に実施例を示して本発明を更に詳細に説明す
る。
実施例 1
10ガラス培養槽でグルコース10g/(炭素
濃度4g/)、硫安2g/(窒素濃度0.2g/
)、その他の成分は第1表と同じ倍地を用いて、
第2表に示す環境条件下で、連続培養を行なつ
た。培養槽での培地液の平均滞留時間は、3〜
120時間の間で変化させた。[Table] In the culture method according to the present invention, the cell number concentration is 5 × 10 6 Cells/at the intermediate stage of the logarithmic growth phase of Euglena.
ml, the carbon concentration will increase within the period of 2 days after reaching the stable phase when the cell number reaches its maximum.
A previously sterilized culture medium having a nitrogen concentration of 1.2 to 8.0 g/ and a nitrogen concentration of 0.07 to 4.50 g/ is continuously fed into the culture tank using a liquid pump or pressurized outflow method. At this time, Euglena cells can be continuously harvested by keeping the average residence time of the medium in the culture tank within the range of 5 to 96 hours. If the carbon concentration is less than 1.2 g/2, the carbon source necessary for cell division will be insufficient, and the number of cells in the culture tank will rapidly decrease from the first to second day after the start of continuous culture. Carbon concentration is 8
When the concentration exceeds g/g, cells rapidly accumulate carbon sources and convert them into the storage polysaccharide paramylon, but on the other hand, division is severely inhibited, and the carbon sources remain in the effluent, reducing the cost of the medium. Undesirable due to gender.
In addition, if the average residence time is less than 5 hours, most of the cells will flow out from the culture tank, and if it exceeds 96 hours, the Euglena cells will enter a decay period and the cell number concentration in the tank will be 5 to 50%.
Since the amount is very small at 6×10 6 cells/ml, the cell yield obtained is also comparable to that obtained by the batch culture method, so there is no merit. In the method of the present invention, the average residence time of the culture medium is 5 to
By culturing continuously for 96 hours, it is possible to increase the productivity of the batch culture method, which conventionally takes 6 to 7 days from seeding to harvest.
5 to 5 times the same amount of Euglena cells as the harvest amount
It can be harvested continuously in a 96 hour cycle. Therefore, compared to the conventional batch method, it is possible to obtain 1.5 to 10 times the amount of Euglena cells in the same culture time, and this intracellular protein content is
It is about the same level as the conventional batch method. In the present invention, the other conditions are not limiting factors for continuous culture, so normal culture conditions may be used. Preferred conditions are PH2-5, temperature 10-34℃,
The dissolved oxygen temperature of the culture solution is 1 ppm or higher, and stirring is done to the extent that the cells in the tank do not settle to the bottom.
If stirring by aeration is sufficient, mechanical stirring may not be necessary. Effects of the invention By culturing Euglena cells using the continuous culture method of the present invention, compared to the case of culturing using the conventional batch culture method,
1.5-10 times more Euglena cells will be obtained. Furthermore, the intracellular protein content of the obtained Euglena cells is comparable to that of conventional Euglena cells. EXAMPLES Next, the present invention will be explained in more detail with reference to Examples. Example 1 In 10 glass culture tanks, glucose 10g/(carbon concentration 4g/), ammonium sulfate 2g/(nitrogen concentration 0.2g/
), the other ingredients are the same as those in Table 1,
Continuous culture was carried out under the environmental conditions shown in Table 2. The average residence time of the culture medium in the culture tank is 3~
It was varied over a period of 120 hours.
【表】
培養日数と培養槽1当りの細胞収量との関係
を第1図に示す。図中は平均滞留時間が9時間
と10時間、は平均滞留時間が15時間、は平均
滞留時間が20時間、は平均滞留時間が30時間、
は平均滞留時間が40時間、は平均滞留時間が
5時間と96時間の場合をそれぞれ表わす。また、
破線は回分法による培養日数と細胞収量との関係
を示す。尚、回分法の場合は、4日毎に得られる
細胞数を加算した値を結んだ直線である。その結
果、培地液の平均滞留時間が5〜96時間のとき
に、回分培養法により細胞収量と比べて同一培養
日数での収量は約1.5〜10倍量であつた。また細
胞内のタンパク含有率は、50〜65%で従来の回分
培養法により得られた細胞と同程度であつた。
実施例 2
10のガラス製培養槽で、グルコース濃度及び
硫安濃度を変数とし、他の培地成分は第1表と同
じ培地を用いて4日間連続培養を行なつた。培養
液の平均滞留時間は、20時間とし、環境条件は第
2表の通りとした。培地中の炭素濃度と培養槽1
当りの細胞収量との関係を第2図に示す。図
中、Aは窒素濃度が0.07〜4.5g/、Bは窒素
濃度が0.05g/、Cは窒素濃度が5g/の場
合であり、破線は窒素濃度が0.04〜5g/で回
分法により培養した場合を示す。第2図から本発
明方法により培養した場合は、回分法により培養
した場合と比較して細胞収量が多いことが明らか
である。また、細胞中のタンパク含有量は50〜65
%で従来の回分培養法による細胞と同程度であつ
た。[Table] Figure 1 shows the relationship between the number of culture days and the cell yield per culture tank. In the figure, average residence time is 9 hours and 10 hours, average residence time is 15 hours, average residence time is 20 hours, average residence time is 30 hours,
represents the average residence time of 40 hours, and represents the cases where the average residence time was 5 hours and 96 hours, respectively. Also,
The broken line shows the relationship between the number of culture days and cell yield using the batch method. In addition, in the case of the batch method, it is a straight line connecting the sum of the cell numbers obtained every 4 days. As a result, when the average residence time of the medium was 5 to 96 hours, the yield in the same number of culture days was about 1.5 to 10 times as much as the cell yield obtained by the batch culture method. In addition, the protein content in the cells was 50-65%, which was comparable to that of cells obtained by conventional batch culture. Example 2 Continuous culture was carried out for 4 days in 10 glass culture vessels using the same medium as shown in Table 1, with glucose concentration and ammonium sulfate concentration as variables, and other medium components as shown in Table 1. The average residence time of the culture solution was 20 hours, and the environmental conditions were as shown in Table 2. Carbon concentration in the medium and culture tank 1
The relationship with the cell yield per unit is shown in Figure 2. In the figure, A is the case where the nitrogen concentration is 0.07 to 4.5 g/, B is the case where the nitrogen concentration is 0.05 g/, C is the case where the nitrogen concentration is 5 g/, and the broken line is the case where the nitrogen concentration was 0.04 to 5 g/ and cultured by the batch method. Indicate the case. From FIG. 2, it is clear that when cultured according to the method of the present invention, the cell yield is higher than when cultured by the batch method. Also, the protein content in cells is 50-65
% was comparable to that of cells grown using the conventional batch culture method.
第1図は、培養日数と培養槽1当りの細胞収
量との関係を示すグラフである。第2図は、培地
中の炭素濃度と培養槽1当りの細胞収量との関
係を示すグラフである。第1図に於いて、は平
均滞留時間が9時間と10時間、は平均滞留時間
が15時間、は平均滞留時間が20時間、は平均
滞留時間が30時間、は平均滞留時間が40時間、
は平均滞留時間が5時間と96時間の場合をそれ
ぞれ示す。また、破線は回分培養法による場合を
示す。第2図に於いてAは窒素濃度が0.07〜4.5
g/Bは窒素濃度が0.05g/、Cは窒素濃度
が5g/の場合であり、破線は窒素濃度が0.04
〜5g/で回分法により培養した場合を示す。
FIG. 1 is a graph showing the relationship between the number of culture days and the cell yield per culture tank. FIG. 2 is a graph showing the relationship between carbon concentration in the medium and cell yield per culture tank. In Figure 1, the average residence time is 9 hours and 10 hours, the average residence time is 15 hours, the average residence time is 20 hours, the average residence time is 30 hours, the average residence time is 40 hours,
show the cases where the average residence time was 5 hours and 96 hours, respectively. Furthermore, the broken line indicates the case using the batch culture method. In Figure 2, A has a nitrogen concentration of 0.07 to 4.5.
g/B is when the nitrogen concentration is 0.05g/, C is when the nitrogen concentration is 5g/, and the broken line is when the nitrogen concentration is 0.04
This shows the case of culturing by batch method at ~5g/.
Claims (1)
ら増殖安定期2日目までの期間内に、炭素濃度
1.2〜8.0g/、窒素濃度0.07〜4.5g/の培地
液を平均滞留時間が5〜96時間となるように培養
槽に送給することを特徴とするユーグレナの連続
培養方法。1. Within the period from the time when the cell concentration reaches 5 × 10 6 cells/ml to the second day of the stable growth phase, the carbon concentration
A continuous culturing method for Euglena, which comprises feeding a culture medium with a nitrogen concentration of 1.2 to 8.0 g/, and a nitrogen concentration of 0.07 to 4.5 g/ to a culture tank such that the average residence time is 5 to 96 hours.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16004384A JPS6137091A (en) | 1984-07-30 | 1984-07-30 | Method of continuous cultivation of euglena |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16004384A JPS6137091A (en) | 1984-07-30 | 1984-07-30 | Method of continuous cultivation of euglena |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6137091A JPS6137091A (en) | 1986-02-21 |
| JPH0532019B2 true JPH0532019B2 (en) | 1993-05-14 |
Family
ID=15706689
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16004384A Granted JPS6137091A (en) | 1984-07-30 | 1984-07-30 | Method of continuous cultivation of euglena |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6137091A (en) |
-
1984
- 1984-07-30 JP JP16004384A patent/JPS6137091A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6137091A (en) | 1986-02-21 |
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