JPH0286773A - Production and separation of secondary metabolite of plant cell utilizing polymer adsorbing substance - Google Patents

Production and separation of secondary metabolite of plant cell utilizing polymer adsorbing substance

Info

Publication number
JPH0286773A
JPH0286773A JP63307947A JP30794788A JPH0286773A JP H0286773 A JPH0286773 A JP H0286773A JP 63307947 A JP63307947 A JP 63307947A JP 30794788 A JP30794788 A JP 30794788A JP H0286773 A JPH0286773 A JP H0286773A
Authority
JP
Japan
Prior art keywords
cells
shikonin
plant
production
separation
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP63307947A
Other languages
Japanese (ja)
Other versions
JPH0475756B2 (en
Inventor
Young-Hun Park
朴 英薫
Jang-Ryul Ryu
劉 長烈
Won-Tak Suh
徐 源澤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Korea Advanced Institute of Science and Technology KAIST
Korea Institute of Science and Technology KIST
Original Assignee
Korea Advanced Institute of Science and Technology KAIST
Korea Institute of Science and Technology KIST
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Filing date
Publication date
Application filed by Korea Advanced Institute of Science and Technology KAIST, Korea Institute of Science and Technology KIST filed Critical Korea Advanced Institute of Science and Technology KAIST
Publication of JPH0286773A publication Critical patent/JPH0286773A/en
Publication of JPH0475756B2 publication Critical patent/JPH0475756B2/ja
Granted legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/66Preparation of oxygen-containing organic compounds containing the quinoid structure

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  • Organic Chemistry (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Zoology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Microbiology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Biotechnology (AREA)
  • Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Abstract] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〈産業上の利用分野〉 本発明は、高分子吸着物質を利用した植物細胞の二次代
謝産物の生産及び分離方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to a method for producing and separating secondary metabolites of plant cells using a polymer adsorbent.

〈従来の技術〉 昔から植物は医薬品類や食品添加物質など人間が生活を
営む上で、いろいろと重要な化学物質を与えてきた。
<Conventional technology> Since ancient times, plants have provided various important chemical substances for human life, such as pharmaceuticals and food additives.

1970年代以後、植物細胞の組織培養の技術の発展と
ともに植物体自体より植物細胞を分離培養し、各種有用
物質の資源として利用しようとさまざまな試みが行われ
てきた。
Since the 1970s, with the development of plant cell tissue culture technology, various attempts have been made to separate and culture plant cells from the plant itself and use them as resources for various useful substances.

その結果、80年年代類、ナフトキノン系の植物性色素
の一つであるシコニン(Shikonin)を初めて産
業的に生産することができた。
As a result, in the 1980s, it was possible to industrially produce Shikonin, a naphthoquinone-based plant pigment, for the first time.

シコニンはりソスパーマムイリスロリゾン(Litho
spermum erythrorhizon)の根の
コルク(cork )層に蓄積される1、4−ナフトキ
ノン(1,4−naphthoquinone)系の色
素である。
Litho
It is a 1,4-naphthoquinone pigment that accumulates in the cork layer of the roots of Spermum erythrorhizon.

このシコニンは、以前はシルクの染色などの染料として
使われたが、最近では火傷や皮膚再生用の医薬品、ある
いはバイオ化粧品の色素原料として最も脚光を浴び、産
業的にも以前より重要な物質であると認められている。
Shikonin was previously used as a dye for silk dyeing, but recently it has received the most attention as a pigment raw material for burns, skin regeneration medicine, and bio-cosmetics, and is an industrially more important substance than before. It is recognized that there is.

く本発明が解決しようとする間頭点〉 現在、産業的にシコニンは主に植物細胞の液比培養(s
ubmerged cullure)によって生産され
ている。
The key points to be solved by the present invention At present, industrially, shikonin is mainly used in liquid culture (s) of plant cells.
It is produced by ubmerged cullure).

培養された細胞を回受した後、溶媒を使って細胞の中に
生成されたシコニンが分離される。
After the cultured cells are collected, shikonin produced in the cells is separated using a solvent.

このような工程においては主に細胞の中にシコニンが分
布されているので、効果的に目的産物を分離するために
は細胞の破壊をともない、その後培養液へ流出されたシ
コニンを分離するために多量の溶媒を処理するなど、工
程上の原価上昇の要因が含まれている。
In such a process, shikonin is mainly distributed within the cells, so in order to effectively separate the target product, the cells must be destroyed, and then the shikonin leaked into the culture medium must be separated. This includes factors that increase costs in the process, such as processing a large amount of solvent.

〈本発明の目的〉 本発明は上記のような欠点を改善するためになされたも
ので、目的産物をより効果的に生産する方法を提供する
ことを目的とする。
<Objective of the present invention> The present invention was made in order to improve the above-mentioned drawbacks, and an object of the present invention is to provide a method for producing a target product more effectively.

さらに、細胞に損傷を与えることなく培養物から高分子
物質へ吸着された目的産物だけを簡単に分離、回受し、
溶媒で抽出するといった工程上の利点を有する方法を提
供することを目的とする。
In addition, only the target product adsorbed from the culture to the polymer substance can be easily separated and recycled without damaging the cells.
The purpose is to provide a method that has process advantages such as extraction with a solvent.

さらに、回分工程時の培養時間を短縮できるような方法
を提供することを目的とする。
Furthermore, it is an object of the present invention to provide a method that can shorten the culture time during a batch process.

また吸着物質の再使用で一度培養した細胞から半連続式
、あるいは連続式で目的産物の分離生産が可能な方法を
提供することを目的とする。
Another object of the present invention is to provide a method that enables the separation and production of target products from cells once cultured by reusing adsorbed substances in a semi-continuous or continuous manner.

さらに効果的にナフトキン類を含む植物細胞の二次代謝
産物の生産原価を下げることができる方法を提供するこ
とを目的とする。
Another object of the present invention is to provide a method that can more effectively reduce the production cost of secondary metabolites of plant cells, including naphtokins.

〈本発明の構成〉 この発明の詳細な説明すると次のようになる。<Configuration of the present invention> The detailed explanation of this invention is as follows.

〈イ〉細胞培養 5HND培地(SHND−medium)を使って、リ
ンスバーマムイリスロリゾン細胞を殖す。
<B> Cell culture Using 5HND medium (SHND-medium), grow rinse vermum iris lorizon cells.

KNO32500mg/L  Inositol   
 1000mg/LMgSO47)(20400Thi
amine IIcI   5Mn5O4H2010N
1cotinic acid  51nsO47fI2
0  1    Pyridoxine    O,5
CIISO45H200,2CPA        2
C’aC122Hx0 200    Kinetin
e     O,IKl       l    5u
crose   30.000COC126H200,
1pH5,8 N)+4H2PO4300Cu1ture temp、
  25 CthP045  1100rp in r
otary shakerNa2Mo042H200,
l Fe50+71120   15 Na2−EDTA    20 〈口〉シコニンの生産条件と方法は次のとおりである。
KNO32500mg/L Inositol
1000mg/LMgSO47) (20400Thi
amine IIcI 5Mn5O4H2010N
1cotinic acid 51nsO47fI2
0 1 Pyridoxine O,5
CIISO45H200,2CPA 2
C'aC122Hx0 200 Kinetin
e O, IKl l 5u
close 30.000COC126H200,
1pH5,8N)+4H2PO4300Cu1ture temp,
25 CthP045 1100rp in r
otary shakerNa2Mo042H200,
l Fe50+71120 15 Na2-EDTA 20 <Example> The conditions and method for producing shikonin are as follows.

前記〈イ〉の方法によって増殖された細胞を洗った後、
高分子吸着剤が含まれているM−9培地(呂−9med
ium)でシコニンを吸着分離生産する。
After washing the cells grown by the method of <A> above,
M-9 medium containing polymer adsorbent (Ro-9med
ium) to adsorb and separate shikonin.

M9培地の造成と生産条件は次のとおりである。The preparation and production conditions of M9 medium are as follows.

Ca(NO3)24t120 694mg/L  3−
IAA    1.75mg/LKNO3805ucr
osc   30.000CuSfl+7t120  
 0.3 バgsO,+71h0  750    pit s、
sNa!!SO41480culture temp、
 25 C2n5O47t120   3 1100r
p in rotary 5hakerKCl    
   65 112803     4.5 N a 112 P 042 Il 20   19F
eSO471(201J7 Na2EDTA       1.83〈ハ〉シコニン
の定量および固定 シコニンの定量は培養された細胞の中、あるいは高分子
物質に吸着されたシコニン色素をクロロホルム(chl
oroform)で抽出した後、減圧蒸発機でクロロホ
ルムを除き、2.5%水酸化カリウム(KO2)を加え
、発色させた後スペクトロホトメタで吸光度(OD6B
)を7111+って標準曲線から比較定量した。
Ca(NO3)24t120 694mg/L 3-
IAA 1.75mg/LKNO3805ucr
osc 30.000CuSfl+7t120
0.3 bugsO, +71h0 750 pits,
sNa! ! SO41480culture temp,
25 C2n5O47t120 3 1100r
p in rotary 5hakerKCl
65 112803 4.5 N a 112 P 042 Il 20 19F
eSO471 (201J7 Na2EDTA 1.83 <c> Quantification of shikonin and fixed shikonin are carried out by quantification of shikonin in cultured cells or adsorbed to a polymeric substance in chloroform (chl).
oroform), chloroform was removed using a vacuum evaporator, 2.5% potassium hydroxide (KO2) was added, color was developed, and absorbance (OD6B) was extracted using a spectrophotometer.
) was comparatively quantified using a standard curve using 7111+.

(参考文献: Mizukami 、Il、et、al
 、(1977)、Phytochemistry、1
6:1183−1186)。
(References: Mizukami, Il, et al.
, (1977), Phytochemistry, 1
6:1183-1186).

シコニンの固定は抽出した試料をシリカゲル(sili
cagel)板に点滴しクロロホルムを可動状にして、
薄層のクロマトグラフィー法(Thin layerc
hromatography )によって行った。
For fixation of shikonin, the extracted sample was immobilized on silica gel (sili
Make the chloroform mobile by dripping it onto the plate (cagel),
Thin layer chromatography method
chromatography).

ここで標準試料はアセチルシコニン(acetylsh
iconin)を使った。
Here, the standard sample is acetylshikonin (acetylsh
iconin) was used.

この方法によると生産された試料のクロマトグラフ上の
Rf値は標準試料のアセチルシコニンのRf値と同じ所
にあり、その外Rf値と少し差のある4つの僅かな跡が
発見できたが、これらはシコニン誘導体であることがわ
かった。
According to this method, the Rf value on the chromatograph of the sample produced was at the same location as the Rf value of the standard sample acetylshikonin, and four slight traces were found that were slightly different from the Rf value. These were found to be shikonin derivatives.

これは質量スペクトロメトリー(Mass spect
rometry)分析方法によっても再び確認された。
This is mass spectrometry.
It was also confirmed again by the analytical method (rometry).

(実施例1) 吸着剤としてのポリウレタンフォーム(Polyure
than foam)を使った場合(表−1)布中で手
軽に求めることのできるポリウレタンフォーム(座布団
スポンジ)を直径1 cm以内の適当な大きさで切って
、5HND培地で殖した細胞と一緒にM−9培地で回分
式半連続式、あるいは連続式で培養すると細胞の増殖と
ともに生成されたシコニンの大部分がポリウレタンに吸
若さ、れる。
(Example 1) Polyurethane foam as an adsorbent
(Table 1) Cut polyurethane foam (cushion sponge), which can be easily obtained from cloth, into a suitable size with a diameter of 1 cm or less, and add it together with the cells grown in 5HND medium. When cultured in M-9 medium in a batchwise semi-continuous manner or in a continuous manner, most of the shikonin produced as the cells proliferate is absorbed into the polyurethane.

培地より分離されたポリウレタンフォームから吸着され
たクロロホルム(chloroform)で抽出して表
1の結果を得た。
The results shown in Table 1 were obtained by extraction with chloroform adsorbed from the polyurethane foam separated from the medium.

表−1 (実施例2)吸着剤としてのシリコンラバー(sili
cone rubber)を使った場合(表−2)シリ
コンラバー(商品名:マスターフレックス(Maste
rflex)、アメリカ、コウルパ−7−(ColeP
ermer )社の製品)を適当な大きさで切って、5
HND培地で殖された細胞と一緒にM−9培地で回分式
、半連続式あるいは連続式で培養すると細胞の増殖とと
もに生成されたシコニンの大部分がシリコンラバーに吸
着される。
Table 1 (Example 2) Silicone rubber (sili) as an adsorbent
(Table 2) When using silicone rubber (product name: Masterflex) (Table 2)
rflex), America, ColeP-7- (ColeP
ermer) product) to an appropriate size, and
When cells grown in HND medium are cultured in M-9 medium in a batch, semi-continuous or continuous manner, most of the shikonin produced as the cells grow is adsorbed to the silicone rubber.

シリコンラバーに吸着されたシコニンをクロロホルムで
抽出して表2の結果が得られた。
Shikonin adsorbed on silicone rubber was extracted with chloroform and the results shown in Table 2 were obtained.

ア、湿体重ffi(g/40m1)  イ、細胞内のシ
コニンウニ培地へ流離されたシコニン エ;ポリウレタンフォームに吸着されたシコニン※シコ
ニン g/40m1、IQ6ポリウレタンフオーム便用 表−2 ア:、゛2体重蚤(g/40m1)  イ:細胞内のシ
コニンウニ培地へ流離されたシコニン 工:シリコンラバーに吸着されたシコニン二北シコニン
: g/40m1.1%シリコンラバー使川用本発明の
効果〉 この発明はVi物細胞の培養時に、適当な高分子吸着物
質を加え、目的産物のシコニンを含むナフトキノン類物
質の細胞外へ流出を誘導した後、この高分子物質に効果
的に吸着させることで植物細胞に対する生産物阻害(p
roduct 1nhibition)を減らすもので
ある。
A. Wet weight ffi (g/40m1) B. Shikonin released into the sea urchin culture medium in the cells; Shikonin adsorbed to polyurethane foam *Shikonin g/40m1, IQ6 polyurethane foam stool table-2 A: ゛2 body weight Fleas (g/40m1) A: Shikonin released into the intracellular sea urchin culture medium: Shikonin adsorbed to silicone rubber Nikita Shikonin: g/40m 1.1% silicone rubber used for use Effects of the present invention> This invention During the culture of plant cells, an appropriate polymeric adsorbent is added to induce the flow of naphthoquinones containing the target product shikonin out of the cells. Product inhibition (p
It is intended to reduce the product 1nhibition).

さらにこの発明は生物反応器でムラサキ科に属するリソ
スパーマムイリスロリゾン(Lithospermum
  erythrorhizon)などの植物細胞を大
量に培養し、シコニンを含むナフトキノン類の植物の二
次代謝産物を生産する際に、疎水性高分子吸着物質を利
用し、生産目的物の分離、回受を易しくすることはいわ
ずもがな、植物細胞自体の二次代謝産物の生産能力を向
上させる方法に関したものてらある。
Furthermore, this invention is a bioreactor that uses Lithospermum iris lorhizon (Lithospermum iris, which belongs to the family Murasaceae).
When producing plant secondary metabolites such as naphthoquinones, including shikonin, by culturing large amounts of plant cells such as A. Needless to say, there are many ways to improve the ability of plant cells to produce secondary metabolites.

その結果、目的産物をより効果的に生産することができ
るようになる。
As a result, the desired product can be produced more effectively.

さらに、潮積に撰j寡を与えるこ七なく培養物から高分
子物質へ吸着された目的産物だけを簡単に分離、回受し
、溶媒で抽出するといった工程上の利点とともに、回分
工程時の培養時間を短縮できるなど、多目的の効果を期
待することができるといった特徴をもっている。
Furthermore, in addition to the process advantages of easily separating, recycling, and extracting with a solvent only the target product adsorbed from the culture to the polymeric substance, without giving a variety to the tidal volume, it also has the advantage of It has the characteristics that it can be expected to have multipurpose effects, such as being able to shorten culture time.

また吸着物質の再使用で一度培養した細胞から半連続式
、あるいは連続式で目的産物の分離生産が可能という点
も大きい利点といえる。
Another great advantage is that by reusing adsorbed substances, it is possible to separate and produce the target product from cells once cultured in a semi-continuous or continuous manner.

さらにこの発明はこのような工程上の利点を提供し、そ
れによって効果的にナフトキン頚を含む植物細胞の二次
代謝産物の生産原価を下げることができるものである。
Furthermore, the present invention provides such process advantages, thereby effectively reducing the production cost of secondary metabolites of plant cells, including naphtoquine necks.

出願人 韓国科墨技術院 院長全墨済Applicant: Korea Institute of Science and Technology, Director Jeon Mok Jae

Claims (4)

【特許請求の範囲】[Claims] (1)植物細胞の培養による二次代謝産物の生産におい
て、 ポリウレタンやシリコンラバー及び関連性のある疎水性
高分子物質の中の一つ以上をその生物反応器に添加し、 植物細胞の中で生産される二次代謝産物の細胞外への流
出を誘導、あるいは促進させることによって同じ二次産
物の生産性を増加させる方法。
(1) In the production of secondary metabolites by culturing plant cells, one or more of polyurethane, silicone rubber, and related hydrophobic polymeric substances are added to the bioreactor and cultured in the plant cells. A method of increasing the productivity of secondary metabolites by inducing or promoting their flow out of cells.
(2)特許請求の第(1)項で生産される二次代謝産物
の一部、または全部を、 第(1)項の高分子物質に吸着させ、回分式、半連続式
、あるいは連続式で分離、生産する方法。
(2) Part or all of the secondary metabolites produced according to claim (1) are adsorbed onto the polymeric substance according to claim (1), and a batch system, semi-continuous system, or continuous system is used. How to separate and produce.
(3)植物がムラサキ(Boraginaceal)科
の植物であることを特徴とする特許請求の範囲の第(1
)項、または第(2)項による方法。
(3) Claim (1) characterized in that the plant is a plant of the Boraginaceal family.
) or the method according to paragraph (2).
(4)植物の二次代謝産物がシコニンを含むナフトキノ
ン系の化合物であることを特徴とする特許請求の範囲の
第(1)項、第(2)項及び第(3)項のいずれか一つ
による方法。
(4) Any one of claims (1), (2), and (3), characterized in that the secondary metabolite of the plant is a naphthoquinone compound containing shikonin. One method.
JP63307947A 1988-09-20 1988-12-07 Production and separation of secondary metabolite of plant cell utilizing polymer adsorbing substance Granted JPH0286773A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR1988P12155 1988-09-20
KR1019880012155A KR900005770B1 (en) 1988-09-20 1988-09-20 Production and Separation Method of Plant Cell Secondary Metabolites Using Polymeric Adsorbents

Publications (2)

Publication Number Publication Date
JPH0286773A true JPH0286773A (en) 1990-03-27
JPH0475756B2 JPH0475756B2 (en) 1992-12-01

Family

ID=19277884

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63307947A Granted JPH0286773A (en) 1988-09-20 1988-12-07 Production and separation of secondary metabolite of plant cell utilizing polymer adsorbing substance

Country Status (2)

Country Link
JP (1) JPH0286773A (en)
KR (1) KR900005770B1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006223202A (en) * 2005-02-18 2006-08-31 Toyo Univ Plant secondary metabolite adsorbent and plant cell secondary metabolite recovery method

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6253699U (en) * 1985-09-24 1987-04-03

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6253699U (en) * 1985-09-24 1987-04-03

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006223202A (en) * 2005-02-18 2006-08-31 Toyo Univ Plant secondary metabolite adsorbent and plant cell secondary metabolite recovery method

Also Published As

Publication number Publication date
KR900005770B1 (en) 1990-08-11
JPH0475756B2 (en) 1992-12-01
KR900004941A (en) 1990-04-13

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