JPH025856A - Production of vincamin and epivincamin by cell culture of vinca rosea - Google Patents
Production of vincamin and epivincamin by cell culture of vinca roseaInfo
- Publication number
- JPH025856A JPH025856A JP1023660A JP2366089A JPH025856A JP H025856 A JPH025856 A JP H025856A JP 1023660 A JP1023660 A JP 1023660A JP 2366089 A JP2366089 A JP 2366089A JP H025856 A JPH025856 A JP H025856A
- Authority
- JP
- Japan
- Prior art keywords
- vincamine
- epivincamine
- culture
- produced
- cells
- 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
- RXPRRQLKFXBCSJ-GIVPXCGWSA-N vincamine Chemical compound C1=CC=C2C(CCN3CCC4)=C5[C@@H]3[C@]4(CC)C[C@](O)(C(=O)OC)N5C2=C1 RXPRRQLKFXBCSJ-GIVPXCGWSA-N 0.000 title claims abstract description 91
- RXPRRQLKFXBCSJ-UHFFFAOYSA-N dl-Vincamin Natural products C1=CC=C2C(CCN3CCC4)=C5C3C4(CC)CC(O)(C(=O)OC)N5C2=C1 RXPRRQLKFXBCSJ-UHFFFAOYSA-N 0.000 title claims abstract description 46
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- 238000004113 cell culture Methods 0.000 title claims description 3
- 240000001829 Catharanthus roseus Species 0.000 title 1
- WKACQPMBGWZDMR-UHFFFAOYSA-N Vincamin Natural products CC=C1/CN2CCC34CC2C1C(=C3Nc5ccccc45)C=O WKACQPMBGWZDMR-UHFFFAOYSA-N 0.000 title 1
- 229960002726 vincamine Drugs 0.000 claims abstract description 45
- RXPRRQLKFXBCSJ-HLAWJBBLSA-N 16-epivincamine Chemical compound C1=CC=C2C(CCN3CCC4)=C5[C@@H]3[C@]4(CC)C[C@@](O)(C(=O)OC)N5C2=C1 RXPRRQLKFXBCSJ-HLAWJBBLSA-N 0.000 claims abstract description 11
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000007788 liquid Substances 0.000 claims abstract description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 5
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 5
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 5
- 150000003839 salts Chemical class 0.000 claims abstract description 4
- 238000012258 culturing Methods 0.000 claims abstract description 3
- 238000000034 method Methods 0.000 claims description 14
- 239000003937 drug carrier Substances 0.000 claims description 2
- 239000008194 pharmaceutical composition Substances 0.000 claims description 2
- 239000004480 active ingredient Substances 0.000 claims 1
- 239000003085 diluting agent Substances 0.000 claims 1
- 241000196324 Embryophyta Species 0.000 abstract description 4
- 241000863486 Vinca minor Species 0.000 abstract 2
- 210000004748 cultured cell Anatomy 0.000 abstract 1
- 239000002609 medium Substances 0.000 description 21
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 14
- 241000238557 Decapoda Species 0.000 description 13
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 10
- 229930013930 alkaloid Natural products 0.000 description 9
- 206010020649 Hyperkeratosis Diseases 0.000 description 5
- 241000863480 Vinca Species 0.000 description 4
- 150000003797 alkaloid derivatives Chemical class 0.000 description 4
- 238000000855 fermentation Methods 0.000 description 4
- 230000004151 fermentation Effects 0.000 description 4
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 3
- 229920001817 Agar Polymers 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 239000008272 agar Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 235000015097 nutrients Nutrition 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 239000005720 sucrose Substances 0.000 description 3
- 239000006228 supernatant Substances 0.000 description 3
- 238000004114 suspension culture Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- 229930091371 Fructose Natural products 0.000 description 2
- 239000005715 Fructose Substances 0.000 description 2
- RFSUNEUAIZKAJO-ARQDHWQXSA-N Fructose Chemical compound OC[C@H]1O[C@](O)(CO)[C@@H](O)[C@@H]1O RFSUNEUAIZKAJO-ARQDHWQXSA-N 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
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 229930006000 Sucrose Natural products 0.000 description 2
- 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 2
- FEWJPZIEWOKRBE-UHFFFAOYSA-N Tartaric acid Natural products [H+].[H+].[O-]C(=O)C(O)C(O)C([O-])=O FEWJPZIEWOKRBE-UHFFFAOYSA-N 0.000 description 2
- MCUPLASQAWQHIW-UHFFFAOYSA-N Vinkamin Natural products CCC12C3CCCN1CCc4c2n(c5ccccc45)C(O)(C3)C(=O)OC MCUPLASQAWQHIW-UHFFFAOYSA-N 0.000 description 2
- 239000003929 acidic solution Substances 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 238000004128 high performance liquid chromatography Methods 0.000 description 2
- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 description 2
- 239000002054 inoculum Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 235000002906 tartaric acid Nutrition 0.000 description 2
- 239000011975 tartaric acid Substances 0.000 description 2
- OWEGMIWEEQEYGQ-UHFFFAOYSA-N 100676-05-9 Natural products OC1C(O)C(O)C(CO)OC1OCC1C(O)C(O)C(O)C(OC2C(OC(O)C(O)C2O)CO)O1 OWEGMIWEEQEYGQ-UHFFFAOYSA-N 0.000 description 1
- IOIIFUWXIINNKX-UHFFFAOYSA-N 5-(5-chloro-2-ethoxyphenyl)-1-methyl-3-propyl-6H-pyrazolo[4,3-d]pyrimidin-7-one Chemical compound CCCc1nn(C)c2c1[nH]c(nc2=O)-c1cc(Cl)ccc1OCC IOIIFUWXIINNKX-UHFFFAOYSA-N 0.000 description 1
- FBPFZTCFMRRESA-KVTDHHQDSA-N D-Mannitol Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-KVTDHHQDSA-N 0.000 description 1
- WQZGKKKJIJFFOK-QTVWNMPRSA-N D-mannopyranose Chemical compound OC[C@H]1OC(O)[C@@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-QTVWNMPRSA-N 0.000 description 1
- 229920001353 Dextrin Polymers 0.000 description 1
- 239000004375 Dextrin Substances 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- GUBGYTABKSRVRQ-PICCSMPSSA-N Maltose Natural products O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@@H]1O[C@@H]1[C@@H](CO)OC(O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-PICCSMPSSA-N 0.000 description 1
- 229930195725 Mannitol Natural products 0.000 description 1
- 108010009736 Protein Hydrolysates Proteins 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 235000016477 Taralea oppositifolia Nutrition 0.000 description 1
- 241001358109 Taralea oppositifolia Species 0.000 description 1
- 241000209140 Triticum Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 229940122803 Vinca alkaloid Drugs 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- GUBGYTABKSRVRQ-QUYVBRFLSA-N beta-maltose Chemical compound OC[C@H]1O[C@H](O[C@H]2[C@H](O)[C@@H](O)[C@H](O)O[C@@H]2CO)[C@H](O)[C@@H](O)[C@@H]1O GUBGYTABKSRVRQ-QUYVBRFLSA-N 0.000 description 1
- 239000002775 capsule Substances 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 235000019425 dextrin Nutrition 0.000 description 1
- 230000004069 differentiation Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003480 eluent Substances 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 150000004678 hydrides Chemical class 0.000 description 1
- 238000011534 incubation Methods 0.000 description 1
- 229910001959 inorganic nitrate Inorganic materials 0.000 description 1
- 239000000594 mannitol Substances 0.000 description 1
- 235000010355 mannitol Nutrition 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 229960002523 mercuric chloride Drugs 0.000 description 1
- LWJROJCJINYWOX-UHFFFAOYSA-L mercury dichloride Chemical compound Cl[Hg]Cl LWJROJCJINYWOX-UHFFFAOYSA-L 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000000877 morphologic effect Effects 0.000 description 1
- 150000002823 nitrates Chemical class 0.000 description 1
- 230000005305 organ development Effects 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000003375 plant hormone Substances 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 102000004196 processed proteins & peptides Human genes 0.000 description 1
- 108090000765 processed proteins & peptides Proteins 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000013587 production medium Substances 0.000 description 1
- 230000002062 proliferating effect Effects 0.000 description 1
- 235000018102 proteins Nutrition 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 238000010898 silica gel chromatography Methods 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- -1 sucrose Chemical class 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 235000013343 vitamin Nutrition 0.000 description 1
- 239000011782 vitamin Substances 0.000 description 1
- 229940088594 vitamin Drugs 0.000 description 1
- 229930003231 vitamin Natural products 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N5/00—Undifferentiated human, animal or plant cells, e.g. cell lines; Tissues; Cultivation or maintenance thereof; Culture media therefor
- C12N5/04—Plant cells or tissues
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D461/00—Heterocyclic compounds containing indolo [3,2,1-d,e] pyrido [3,2,1,j] [1,5]-naphthyridine ring systems, e.g. vincamine
Abstract
Description
【発明の詳細な説明】
本発明は、ビンカミンおよびエピビンカミンの製造方法
に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing vincamine and epivincamine.
この数年来、人工培地中での発酵法によってとンカアル
カ11イドを製造することについて研究が進められてい
る。仏国特許出願早期公開FR−A2300131号に
は、未同定のビンカアルカロイドの混合物の製造方法が
開示されている。これによると、好ましくは連続的に光
照射しながら、細胞懸濁培養にて20日間以上発酵する
ことによってアルカロイドの複雑な混合物が約20〜4
5■/1の収量で製造されることが示されている。For the past several years, research has been underway to produce tonka alkaloid by fermentation in an artificial medium. French patent application FR-A2300131 discloses a method for producing a mixture of unidentified vinca alkaloids. According to this, a complex mixture of alkaloids is produced by fermentation in cell suspension culture for 20 days or more, preferably under continuous light irradiation.
It has been shown that it can be produced with a yield of 5/1.
本発明に於いては、驚くべきことに、ツルニチニチソウ
(L■ca m1nor L、 )由来の新規細胞培
養株が、他のアルカロイドを生成することなく、収率良
くビンカミンおよびその異性体であるエビビカミンを産
生じ得ることが知見された。そこで、本発明は、資化し
つる炭素源、資化しうる窒素源および無機塩類を含む液
体培地中で、好気性条件下に培養株F I CE−V3
(DSM 4365)[111培養することよりな
るビンカミンおよびエビビンカミンの製造方法を提供す
るものである。In the present invention, surprisingly, a new cell culture strain derived from Periwinkle (L.camlnor L.) can produce vincamine and its isomer Ebivicamine in good yield without producing other alkaloids. It was found that it can be produced. Therefore, the present invention aims to cultivate the culture strain FI CE-V3 under aerobic conditions in a liquid medium containing an assimilable carbon source, an assimilable nitrogen source, and inorganic salts.
(DSM 4365) [111] Provides a method for producing vincamine and shrimp vincamine, which comprises culturing.
本発明によって、培養物を光照射するしないにかかわら
ず、液体培地中において約1 g/j!あるいはそれ以
上の収量でビンカミンおよびエビビンカミンを1!!J
造することができる。本発明の最大の特徴は、収率が高
いこと、通常の工業規模の発M槽においても実施しうる
ような簡単なプロセス−Cあることおよびビンカミンと
エビビンカミンの二つの異性体のみが生成することであ
り、ツルニブーニチソウ植物体よりアルカロイドを抽出
する方法および前記仏国特許出願早期公開F r<−八
−2300131の半合成的製造方法に比べて有利であ
る。According to the present invention, approximately 1 g/j in liquid medium, regardless of whether or not the culture is irradiated with light! Or higher yield of vinkamin and shrimp vinkamin 1! ! J
can be built. The most important features of the present invention are that the yield is high, that it is a simple process that can be carried out even in a normal industrial-scale M generation tank, and that only two isomers, vincamine and shrimp vincamine, are produced. This method is more advantageous than the method of extracting alkaloids from the Periwinkle plant and the semi-synthetic production method of the French patent application F r<-8-2300131.
このようにして得られたビンカミンおよびエビビンカミ
ンは細胞および/または培養ブロスから回収される。こ
れらは各々分難することができる。なお、ビンカミンと
エビごンカミンは、16位の立体配置が異なる立体異性
体である。Vincamine and shrimp vincamine thus obtained are recovered from the cells and/or culture broth. Each of these can be separated. Incidentally, vincamine and vincamine are stereoisomers that differ in the configuration at the 16th position.
文献上、酸性溶液中でビンカミンからエビビンカミンに
轟収率で変換しうろことが知られている(G、 5zo
ntay et al、、Tetrahedron
1ett。In the literature, it is known that vincamine can be converted to shrimp vincamine in an acidic solution with a high yield (G, 5zo).
Tetrahedron
1ett.
191頁、 1973年)。したがって本発明によって
製造したビンカミンをこの方法に従ってエビビンカミン
−に変換することができる。p. 191, 1973). Therefore, vincamine produced according to the present invention can be converted to shrimp vincamine according to this method.
本発明のビンカミンおよびエビビンカミンを生産する新
規培養株をFICE−V3株と称する。このものは、微
生物の寄託に関する国際的なブダペスト条約下、 19
81年12J:J23日にドイツ微生物寄託機関< o
eutche s ammlung VOnM i
kroorganismen、 D S M )に寄託
番号DSM4365が付されて寄託されている。The new culture strain producing vincamine and shrimp vincamine of the present invention is referred to as the FICE-V3 strain. 19 under the international Budapest Treaty on the Deposit of Microorganisms.
12J, 1981: German Microbiological Depository on J23rd
eutche s ammlung VOnM i
kroorganismen, DSM) with the deposit number DSM4365.
FICE−V3細胞の形態学的特徴は次の通りである。The morphological characteristics of FICE-V3 cells are as follows.
固形培地上で生育した培養物(カルス培養物)は無色で
容易に解集合しうる細胞集団である。細胞は直径50〜
100−の円形ないし楕円形の形状を有している。試験
した培養条件下で、カルス培養物は器官形成あるいはい
かなる分化過程をも示さない。2000ルクスの光に露
光すると、カルス培養物はクロ[lフィルの生合成によ
り緑色となる。しかしながら、光露光はアルカロイドの
生合成には影費を及ぼさない。Cultures grown on solid media (callus cultures) are colorless and easily disaggregated cell populations. Cells are 50~
It has a 100-circular or elliptical shape. Under the culture conditions tested, callus cultures do not exhibit organogenesis or any differentiation process. When exposed to 2000 lux of light, the callus culture becomes green due to the biosynthesis of Chlorofil. However, light exposure has no effect on alkaloid biosynthesis.
液体培地にて生育した場合、未分化培養物は5から50
細胞よりなる小さな集塊として成長する。When grown in liquid medium, undifferentiated cultures have 5 to 50
Grows as small clumps of cells.
このm胞は固体培地上で生育したものと同じ形状と大き
さを有している。This m cell has the same shape and size as that grown on a solid medium.
他の特性は、ビンカミンとエビビンカミンの二つのアル
カ[lイド(以後簡単にl゛粗ビンカミンJと称する)
を産生ずることである。Other characteristics are the two alkali hydrides of vincamine and shrimp vincamine (hereinafter simply referred to as ``crude vincamine J'').
It is to produce.
この新規1m物は、レッコ(l ecco) [イタ
リア国コモ(Como) ] +I近で採取されたツル
ニチニヂンウ(V 1nca m1nor)の植物体由
来のものである。この植物体の一部(菓、新芽および根
)を70%エタノールで5分間、2%次次亜塩素酸上ト
リウム2分間、さらに0.5%塩化第二水銀で45秒間
洗浄することにより滅菌した。各々の洗浄のあと、i滅
菌蒸留水ですすいだ。This new 1 m product is derived from a plant of a periwinkle (V 1nca m1nor) collected near Lecco [Como, Italy] +I. Sterilize the plant parts (capsules, shoots, and roots) by washing them with 70% ethanol for 5 minutes, 2% epithorium hypochlorite for 2 minutes, and 0.5% mercuric chloride for 45 seconds. did. After each wash, rinse with sterile distilled water.
その後、葉と新芽と根を小さな片に切り、1mg/dの
ナフタレン酸II(NAA)と7g/!の寒天を補足し
たギャンボルグB5培地(0゜し、Gamborget
al、 EXD、 Ce1l Res、、50゜p
151(1968))に無菌的に固定し、暗所で28
℃に保った。10〜15日後、未分化組織(カルス)は
成長しはじめ、20〜30日後にそれを同じ培地の寒天
斜面上に移した。通常、十分に成長した培養物を得るに
は、暗所28℃で約20日間を要する。2ないし3回移
したのち、安定な培養物が得られ、振とうフラスコにお
ける接種材料として用いた。The leaves, shoots and roots were then cut into small pieces and treated with 1 mg/d of naphthalene II (NAA) and 7 g/! Gamborgh B5 medium supplemented with agar (0°, Gamborget
al, EXD, Ce1l Res, 50゜p
151 (1968)) and in a dark place for 28 hours.
It was kept at ℃. After 10-15 days, undifferentiated tissue (callus) began to grow, and after 20-30 days it was transferred onto agar slants in the same medium. Typically, approximately 20 days in the dark at 28°C are required to obtain a fully grown culture. After two to three transfers, stable cultures were obtained and used as inoculum in shake flasks.
新鮮重計約1〜2gのカルスをガラス棒で均質化したの
ら、1m9/ItのNAAを追加した50#1e(7)
液状ギャンボルグ培地を含む300m容の三角フラスコ
に移した。回転振とう器(120rpm)上で暗所28
℃にて7日間培養したのち、培養物は乾燥重量的10m
y/ln1.となり、ついで5rdの増殖型培養物を、
309/Itのショ糖と1■/1のNAAを入れた45
dのギャンボルグB5培地(G30培地)を含む300
In1容の三角フラスコに接種づ°る。これらの培養物
を12Orpmの回転振とう器上で、暗所23℃にて1
0〜14日間培養する。After homogenizing about 1-2 g of fresh callus with a glass rod, 50#1e (7) was added with 1 m9/It of NAA.
Transferred to a 300 m Erlenmeyer flask containing liquid Gamborg's medium. 28 hours in the dark on a rotary shaker (120 rpm)
After 7 days of incubation at ℃, the culture had a dry weight of 10 m
y/ln1. Then, the 5th proliferative culture,
45 with 309/It sucrose and 1/1 NAA
300 containing Gamborg B5 medium (G30 medium) of d.
Inoculate an Erlenmeyer flask with a volume of In1. These cultures were grown for 1 hour in the dark at 23°C on a 12Orpm rotary shaker.
Culture for 0-14 days.
本発明の方法においては、FICE−V3111111
を液体培地中で培養する。ガラスあるいは例えばステン
レススチールのようなその他の一般に使用される材料の
フラスコまたは発酵槽を使用することができる。液体培
地としては、資化しうる有機炭素源、資化しうる有機ま
たは無機の窒素源、無機塩類、および必要に応じて植物
ホルモン類および/またはビタミン類を含有する栄養溶
液をあげることができる。資化しうる有機炭素源として
は、シヨ糖、ブト・り糖、フラクトース、でんぷん、デ
キストリン、グリセリン、マンニトールおよびマンノー
スのような炭水化物をあげることができる。In the method of the present invention, FICE-V3111111
is cultured in liquid medium. Flasks or fermenters of glass or other commonly used materials such as stainless steel can be used. The liquid medium may include a nutrient solution containing an assimilable organic carbon source, an assimilable organic or inorganic nitrogen source, inorganic salts, and optionally plant hormones and/or vitamins. Assimilable organic carbon sources can include carbohydrates such as sucrose, buto-sucrose, fructose, starch, dextrin, glycerin, mannitol and mannose.
資化しうる有機または無機の窒素源としては、アミノ酸
類やその混合物、ペプチド類とタンパク質もしくはこれ
らの加水分解物、カゼインの加水分解物、アルコール合
成におけるトウモ【ココシや小麦の蒸留残渣のような穀
類の水溶性画分や酵素および無機硝酸塩や無機のアンモ
ニウム塩をあげることができる。Organic or inorganic nitrogen sources that can be assimilated include amino acids and their mixtures, peptides and proteins or their hydrolysates, casein hydrolysates, and grains such as corn [cocose and wheat distillation residue] for alcohol synthesis. Examples include water-soluble fractions of enzymes, inorganic nitrates, and inorganic ammonium salts.
本発明の方法は、典型的には懸濁培養により、例えば撹
拌しながらフラスコ中で、あるいは通気発酵槽中で、p
Hが4.4〜7.0の範囲好ましくはpH6,5にて、
温度が18−36℃の範囲好ましくは23℃で行なわれ
る。−膜内で好ましい培養条件は、暗所、5.1〜6.
8 (7) I)H範囲、18〜30’C(7) m度
範囲かつ8〜16日間の期間である。粗ビンカミンの産
生は2〜3日の生育侵に始まり、10〜14日後に最高
に達する。The process of the invention typically involves plating by suspension culture, for example in a flask with stirring or in an aerated fermenter.
H is in the range of 4.4 to 7.0, preferably at pH 6.5,
The temperature range is 18-36°C, preferably 23°C. - Preferred culture conditions within the membrane are dark, 5.1-6.
8(7) I)H range, 18-30'C(7)m degree range and duration of 8-16 days. Production of crude vincamine begins after 2-3 days of growth and reaches its peak after 10-14 days.
粗ピンカミンは細胞および培養ブロスの双方より抽出す
ることができる。濾過した細胞から、典型的にはメタノ
ール、エタノールあるいはアセトンのような水と混和し
うる有機溶媒を用いて粗ビンカミンを抽出することがで
きる。細胞を除去してpH8〜9のアルカリ性とした培
養ブロスからは、通常クロロホルム、二塩化メヂレン、
エテルニーデルのような水と混和しない溶媒により粗ビ
ンカミンを抽出することができる。Crude pinkamine can be extracted from both cells and culture broth. Crude vincamine can be extracted from the filtered cells, typically using a water-miscible organic solvent such as methanol, ethanol or acetone. Culture broth that has been made alkaline to pH 8-9 after removing cells is usually treated with chloroform, methylene dichloride,
Crude vincamine can be extracted with a water-immiscible solvent such as ethernidel.
このようにして製造したビンカミンもしくはエピビンカ
ミンは、医薬上許容しつる担体または希粗剤と共に医薬
組成物とすることができる。Vincamine or epivincamine thus produced can be made into a pharmaceutical composition together with a pharmaceutically acceptable carrier or diluted crude agent.
以F1実施例により本発明をさらに詳細に説明する。た
だし、以下の説明はなんら本発明を限定するものではな
い。The present invention will be explained in more detail below using Example F1. However, the following description does not limit the present invention in any way.
実施例1
希アンモニアでI)Hを6.5に調整した50dの03
0栄養培地を含む300d容の三角フラスコ中で行ない
、これを回転振どう器(回転数120rpm、偏心距!
!18cm)によって振とうした。最良の培養温度は2
3℃であった。このフラスコに85寒天培地中で14日
経たFICピー■3培養物により得られた細胞を接種し
た。Example 1 50d 03 with I)H adjusted to 6.5 with dilute ammonia
This was carried out in a 300 d Erlenmeyer flask containing 0 nutrient medium, and this was carried out using a rotating shaker (rotation speed: 120 rpm, eccentric distance).
! 18 cm). The best culture temperature is 2
The temperature was 3°C. The flask was inoculated with cells obtained from a 14 day old FIC Pei 3 culture in 85 agar medium.
高速液体クロマトグラフィー(Hplc)での測定から
、14日後に約750rng/jのビンカミンと340
■/j!のエビビンカミンが生成していることが判つた
。200個のフラスコより得られた101の細胞懸濁培
養物を遠心分離し、細胞と上澄みとを別個に抽出した。After 14 days, high performance liquid chromatography (HPLC) measurements revealed that approximately 750 rng/j of vincamine and 340 rng/j of vincamine were detected.
■/j! It was found that shrimp binkamine was produced. 101 cell suspension cultures from 200 flasks were centrifuged and the cells and supernatant were extracted separately.
上澄みを炭酸ナトリウムを加えてpH9とし、101の
塩化メチレンで2回抽出した。The supernatant was adjusted to pH 9 with sodium carbonate and extracted twice with 101 methylene chloride.
有機性抽出物を次いで2%の酒石酸水溶液で抽出した。The organic extract was then extracted with 2% aqueous tartaric acid.
得られた酸性溶液をpH9へ・10としたのち、塩化メ
チレンで抽出した。The resulting acidic solution was adjusted to pH 9/10 and then extracted with methylene chloride.
遠心分離した細胞は2%の酒石酸を含む50%アヒトン
水溶液で均質化し、濾過した。P液を減圧下溌縮し、得
られた水溶液を1))−19〜10のアルカリ性とした
のら塩化メチレンで抽出した。The centrifuged cells were homogenized with a 50% ahitone aqueous solution containing 2% tartaric acid and filtered. The P solution was compressed under reduced pressure, and the resulting aqueous solution was made alkaline to 1)) -19 to 10, and then extracted with methylene chloride.
細胞および上澄みの有機抽出物を合ねゼ蒸発乾固さける
ことにより、8.8gの粗ビンカミンN−1plc測定
によれば、6.0gのビンカミンと2.83のエビビン
カミンよりなる)を得た。二つのアルカロイドはシリカ
ゲルカラムクロマトグラフィーにより分離した。この際
、溶離液として、含有するエタノールの量を徐々に増や
した塩化メチレンを用いた。カラムより5.69の純粋
なビンカミンと2.5gのエビビンカミンを回収した。The organic extracts of the cells and supernatant were combined and evaporated to dryness, yielding 8.8 g of crude vincamine (N-1, consisting of 6.0 g of vincamine and 2.83 g of shrimp vincamine as determined by plc). The two alkaloids were separated by silica gel column chromatography. At this time, methylene chloride containing gradually increased amount of ethanol was used as the eluent. 5.69 g of pure vincamine and 2.5 g of shrimp vincamine were recovered from the column.
実施例2
本発明の方法を二段発酵法によりフラスコ中で行なった
。最初に、209/lのブドウ糖と1■/lのNAAを
含むムラシゲ培地(T 、 M urashiaeet
al、、Physiol、 Plant、 誌
15巻、413頁。Example 2 The method of the invention was carried out in a flask by a two-stage fermentation method. First, Murashige medium (T, Murashiage medium) containing 209/l glucose and 1/l NAA was used.
al, Physiol, Plant, Magazine
Volume 15, page 413.
1962年)上で実施例1と同様条件にて生育を行なっ
た。8日後に乾燥Φ母は10〜13勺/lに達しており
、培養物を無菌的に遠心分離し、細胞は生産培地G30
中に再懸濁した。6〜8日間の発酵によって粗ビンカミ
ンは1050mg/ l生成した。Hplc分析により
、ビンカミンは全アルカロイドの73%、エビビンカミ
ンは25%であることが判った。実施例1に記載したと
同様に100個の三角フラスコを用いて操作したところ
、3.6gの純粋なビンカミンと1.09のエビビンカ
ミンが単離された。ブドウ糖の代りにフラクトースある
いはマルトースを培地中に用いた場合にも殆んど同じ収
量であった。(1962) under the same conditions as in Example 1. After 8 days, the dry Φ mother had reached 10-13 μg/l, the culture was centrifuged aseptically, and the cells were transferred to production medium G30.
resuspended in Fermentation for 6-8 days produced 1050 mg/l of crude vincamine. Hplc analysis showed that vincamine was 73% of the total alkaloids and shrimp vincamine was 25%. Using 100 Erlenmeyer flasks as described in Example 1, 3.6 g of pure vincamine and 1.09 g of shrimp vincamine were isolated. Almost the same yield was obtained when fructose or maltose was used in the medium instead of glucose.
実施例3
61のG30栄養培地を含むIJの培養槽中で行なった
。ツルニチニヂソウ培養株FICE−v3の培養は実施
例1に従って、50rdの85培地を入れた300d容
の三角フラス」中で行なった。1〜10日後(乾燥if
邑12rftg/d) 、培養物を450meの85培
地を含む20007容の丸底フラスコに接種し、暗所2
8℃にて回転数1100rpの回転振どう器上で培養し
た。7〜10日後充分に成長した培養物(乾燥lff1
10ay/d)を、6j!(7)G30培地を含ム10
R1の培養槽への接種材料として用いた。1100rp
の初期撹拌速度かつ0.5容量/容出/分の通気速度で
、暗所27℃にて増殖を行なった。溶存酸素濃度が20
%低下した場合には、撹拌速度を20rpm増加させた
。Example 3 It was carried out in an IJ culture tank containing 61 g of G30 nutrient medium. Cultivation of the periwinkle culture strain FICE-v3 was carried out in accordance with Example 1 in a 300 d Erlenmeyer flask containing 50 rd of 85 medium. 1-10 days later (drying
12rftg/d), the culture was inoculated into a 20007 volume round bottom flask containing 450me of 85 medium and incubated in the dark for 2 hours.
Culture was carried out at 8°C on a rotating shaker with a rotational speed of 1100 rpm. After 7-10 days fully grown culture (dried lff1
10ay/d), 6j! (7) M10 containing G30 medium
It was used as an inoculum for the R1 culture tank. 1100rp
Growth was carried out in the dark at 27° C. with an initial stirring rate of 0.5 vol/vol/min and an aeration rate of 0.5 vol/vol/min. Dissolved oxygen concentration is 20
% decrease, the stirring speed was increased by 20 rpm.
10−〜14日後培養物は乾燥型部で20η/dとなり
、粗ビンカミンとして表わしたアルカロイド含量は7G
OIng/βてあった。このアルカロイドを実施例1に
記したと同様に抽出し、精製して、3.39/lのビン
カミンおよびoJg/ j2のエピビンカミンを得た。After 10-14 days the culture had a dry part of 20 η/d and an alkaloid content of 7 G expressed as crude vincamine.
There was OIng/β. This alkaloid was extracted and purified as described in Example 1 to yield 3.39/l of vincamine and oJg/j2 of epivincamine.
Claims (1)
塩類とを含む液体培地にて、好気性条件下で培養株FI
CE−V3(DSM4365)の細胞を培養することを
特徴とするビンカミンおよびエピビンカミンの製造方法
。 (2)細胞を暗所で5.1〜6.8のpH、18〜30
℃の温度にて8〜16日間培養することを特徴とする請
求項1に記載の方法。 (3)製造されたビンカミンおよびエピビンカミンを細
胞および/または培養ブロスから回収することを特徴と
する請求項1または請求項2に記載の方法。 (4)製造されたビンカミンおよびエピビンカミンをお
互いに分離することを特徴とする請求項1から請求項3
のいずれかに記載の方法。 (5)製造されたビンカミンをエピビンカミンに変換す
ることを特徴とする請求項1から請求項4のいずれかに
記載の方法。 (6)発酵槽中で行なうことを特徴とする請求項1から
請求項5のいずれかに記載の方法。 (7)実質的にいずれかの実施例に記載のビンカミンま
たはエピビンカミンの製造方法。(8)医薬上許容しう
る担体あるいは希釈剤、および活性成分として請求項1
から請求項6のいずれかに記載の方法によって製造され
るビンカミンあるいはエピビンカミンより成る医薬組成
物。 (9)細胞培養株FICE−V3(DSM4365)。[Scope of Claims] (1) Culture strain FI under aerobic conditions in a liquid medium containing an assimilated carbon source, an assimilated nitrogen source, and inorganic salts.
A method for producing vincamine and epivincamine, which comprises culturing CE-V3 (DSM4365) cells. (2) Cells were grown in the dark at a pH of 5.1-6.8, 18-30
The method according to claim 1, characterized in that the culture is carried out at a temperature of 8 to 16 days. (3) The method according to claim 1 or 2, characterized in that the produced vincamine and epivincamine are recovered from cells and/or culture broth. (4) Claims 1 to 3 characterized in that the produced vincamine and epivincamine are separated from each other.
The method described in any of the above. (5) The method according to any one of claims 1 to 4, characterized in that the produced vincamine is converted to epivincamine. (6) The method according to any one of claims 1 to 5, which is carried out in a fermenter. (7) A method for producing vincamine or epivincamine as described in substantially any of the Examples. (8) Claim 1 as a pharmaceutically acceptable carrier or diluent and an active ingredient.
A pharmaceutical composition comprising vincamine or epivincamine produced by the method according to claim 6. (9) Cell culture line FICE-V3 (DSM4365).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB8802591A GB2214913B (en) | 1988-02-05 | 1988-02-05 | Production of vincamine and epivincamine by cell cultures of vinca minor |
GB8802591 | 1988-02-05 |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH025856A true JPH025856A (en) | 1990-01-10 |
Family
ID=10631128
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1023660A Pending JPH025856A (en) | 1988-02-05 | 1989-02-01 | Production of vincamin and epivincamin by cell culture of vinca rosea |
Country Status (4)
Country | Link |
---|---|
JP (1) | JPH025856A (en) |
DE (1) | DE3902980A1 (en) |
GB (1) | GB2214913B (en) |
IT (1) | IT1233453B (en) |
-
1988
- 1988-02-05 GB GB8802591A patent/GB2214913B/en not_active Expired - Fee Related
-
1989
- 1989-02-01 DE DE3902980A patent/DE3902980A1/en not_active Withdrawn
- 1989-02-01 JP JP1023660A patent/JPH025856A/en active Pending
- 1989-02-03 IT IT8919307A patent/IT1233453B/en active
Also Published As
Publication number | Publication date |
---|---|
GB2214913A (en) | 1989-09-13 |
IT1233453B (en) | 1992-04-01 |
IT8919307A0 (en) | 1989-02-03 |
GB2214913B (en) | 1991-10-16 |
DE3902980A1 (en) | 1989-08-17 |
GB8802591D0 (en) | 1988-03-02 |
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