JPS5959187A - Method and apparatus for cell culture - Google Patents

Method and apparatus for cell culture

Info

Publication number
JPS5959187A
JPS5959187A JP57169734A JP16973482A JPS5959187A JP S5959187 A JPS5959187 A JP S5959187A JP 57169734 A JP57169734 A JP 57169734A JP 16973482 A JP16973482 A JP 16973482A JP S5959187 A JPS5959187 A JP S5959187A
Authority
JP
Japan
Prior art keywords
culture
cells
culture solution
support
gas
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
Application number
JP57169734A
Other languages
Japanese (ja)
Inventor
Hironori Murakami
浩紀 村上
Fumiyasu Tsuchiya
土屋 文安
Michio Kanbe
道雄 神辺
Yoshihiro Yoshiyama
吉山 良博
Munehiro Oda
宗宏 小田
Junichi Hayazaki
早崎 淳一
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.)
Meiji Dairies Corp
Original Assignee
Meiji Milk Products Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Meiji Milk Products Co Ltd filed Critical Meiji Milk Products Co Ltd
Priority to JP57169734A priority Critical patent/JPS5959187A/en
Publication of JPS5959187A publication Critical patent/JPS5959187A/en
Pending legal-status Critical Current

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  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Abstract

PURPOSE:To culture adherent cells in high efficiency, by proliferating the cells on the substrate without immersing the substrate in culture liquid while contacting the substrate with the culture liquid. CONSTITUTION:The substrate container 3 is fully packed with the substrates 1, the culture liquid is sprayed from the sprayer 4 placed at the top of the culture tank 2 to effect the thorough contact of the liquid with the substrates 1, and the culture liquid dripped to the bottom of the container 3 is collected in the tank 20 and circulated to the sprayer 4 with a pump. The substrate container 3 is aerated with a gas having necessary composition simultaneously to the initiation of the culture. The gas is introduced into the culture tank 2 from the gas diffuser 17 attached at the top or bottom of the culture tank and made to contact countercurrently or concurrently with the culture liquid. The adherent cells can be proliferated on the substrate which is not immersed in but contacted with the culture liquid, in high efficiency.

Description

【発明の詳細な説明】 本発明は、接着性を有する細胞の培養方法及び装置に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for culturing adhesive cells.

更に詳細には、本発明は、支持体表面の広い面積で接着
性を有する細胞を効率よく培養する方法及び装置に関す
るものである。
More specifically, the present invention relates to a method and apparatus for efficiently culturing adherent cells over a wide area of the surface of a support.

一般に、細胞培養は、植物細胞由来のサントニン々どの
製造や、動物細胞内′来のインターフェロン、ウロキナ
ーゼ、各種ホルモン々どの製造に利用されている。
In general, cell culture is used for the production of santonins derived from plant cells, and for the production of interferon, urokinase, and various hormones derived from animal cells.

また、細胞培養は種々の生物学的物質の生産あるいは生
体に関する基礎研究には有効な技術である。
Furthermore, cell culture is an effective technique for producing various biological substances or for basic research on living organisms.

しかしながら、細胞培養においてに、目的物質を産生す
る細胞そのものを大量に増殖させることが必須であり、
そのために細胞にとっての成長因子の検索あるいは細胞
の大量培養に関する技術への検討が多くなされている。
However, in cell culture, it is essential to grow the cells that produce the target substance in large quantities.
For this reason, much research has been done into searching for growth factors for cells and into techniques for mass culturing cells.

従来性なわれている細胞培養法には、大別して、浮遊培
養法と単層培養法がある。浮遊培養法に於ては、細胞の
沈降を防ぐべく攪拌操作が行われるものであるが、攪拌
による細胞の損傷の影響が犬きく、また、深部培養であ
ることから細胞の生育に必須である酸素を供給する際に
泡立ちが生じて培養が困難になったり、培養を汚染から
守る手段を講じるなど煩雑な操作を必要とするものであ
る。
Conventional cell culture methods can be broadly classified into suspension culture methods and monolayer culture methods. In the suspension culture method, agitation is performed to prevent cells from settling, but agitation does not damage the cells, and since it is a deep culture, stirring is essential for cell growth. Bubbling occurs when oxygen is supplied, making culturing difficult, and requires complicated operations, such as taking measures to protect the culture from contamination.

一方、単層培養法には現在知られているものにローラー
培養法、多層平板法等があるが、これらの方法はいずれ
も細胞の生育面積に制限があり、また、細胞への気体の
接触に難点があった。
On the other hand, currently known monolayer culture methods include the roller culture method and the multilayer plate method, but all of these methods have limitations on the area in which cells can grow, and they also prevent gas from coming into contact with the cells. There were some difficulties.

本発明者らは、有効かつ簡便な細胞培養法を求めて研究
した結果、細胞培養に支持体を採用することによって解
決することができた。
As a result of research for an effective and simple cell culture method, the present inventors were able to solve the problem by employing a support for cell culture.

本発明は、接着性を有する細胞を、培養液中に浸漬され
々い支持体上に増殖させ、該支持体上には培養液を接着
せしめて培養することを特徴とする細胞培養方法及び装
置に関するものである。
The present invention provides a cell culture method and device, characterized in that cells having adhesive properties are grown on a support that is immersed in a culture solution, and the culture solution is adhered to the support and cultured. It is related to.

本発明は、マイクロキャリアー法等に見られる攪拌によ
る細胞の損傷や通気による泡立ち等の短所を克服し、し
かも培養が連続的に実施でき、培養液の交換、補給、あ
るいは通気量やガス成分のコントロールが極めて容易に
行なうことができる細胞の大量培養方法及び装置である
The present invention overcomes the disadvantages of the microcarrier method, such as damage to cells caused by agitation and foaming caused by aeration, and allows for continuous culture, with no need to change or replenish the culture solution, or adjust the amount of aeration or gas components. This is a method and device for mass culturing cells that can be extremely easily controlled.

本発明は、細胞培養において支持体を用いた点が大きな
特色となっている。支持体には、ポリスチレン、スチー
ル、ガラス、アルミニウム、ゴム、ポリプロピレン、ポ
リカーボネイト、ポリエチレン、テフロンその他細胞が
接着可能な材料を用いればよく、寸だ、非接着性の支持
体を用いる場合あるいはより接着を容易にするためKは
、有効な物質で支持体のコーティングを行なってもよい
A major feature of the present invention is that a support is used in cell culture. The support may be made of polystyrene, steel, glass, aluminum, rubber, polypropylene, polycarbonate, polyethylene, Teflon, or any other material to which cells can adhere. To facilitate this, K may also carry out coating of the support with an effective substance.

支持体の形状としては、棒状、球状、板状、繊維状、各
種変形状などあらゆる形状のものが使用されるが、本発
明において有効なものの1つに第1図に示されるたいこ
橋状の支持体がある。このたいこ橋状支持体は、単位容
積当りの表面積が極めて大きく、捷だ、充填して使用し
た際、培養液かたするような個所がなく、きわめて有効
である。
The support may be of any shape, such as a rod, sphere, plate, fiber, or various deformed shapes, but one of the shapes that are effective in the present invention is the tassel-bridge shape shown in FIG. There is a support. This tassel-shaped support has an extremely large surface area per unit volume, and when it is used after being broken or filled, there is no place where the culture solution gets mixed up, making it extremely effective.

この支持体は培養槽内の支持体収容容器に収容される。This support is housed in a support storage container within the culture tank.

培養液は培養槽上部に設けられた培養液撒布装置から支
持体にく捷なく接触されるように撒布され、下方に落下
した培養液はタンクに集りポンプで撒布装置に送られ、
循環されるようになっている。
The culture solution is sprayed from the culture solution dispersion device installed at the top of the culture tank so as to be in direct contact with the support, and the culture solution that falls downward collects in the tank and is sent to the spraying device by a pump.
It is designed to be circulated.

培養開始時には、培養槽を細胞の増殖に適した温度の2
0〜40℃に保温しておいて、所定の細胞を分散させた
培養液を満たし、一定の時間を経過した後循環を開始し
支持体表面に細胞を付着させて増殖を開始する。
At the start of culture, set the culture tank to a temperature suitable for cell growth.
While keeping the temperature at 0 to 40°C, it is filled with a culture medium in which predetermined cells are dispersed, and after a certain period of time, circulation is started and the cells are attached to the support surface to start proliferation.

培養開始と同時に、必要によって、必要なガス組成を有
する気体が通気される。通気は培養槽下部もI〜〈は上
部に設けた気体分散装置を通して通気されるが、そのガ
ス組成あるいは通気量は目的の細胞に有効々ものに設定
される。培養槽に導入されたガスは支持体の空隙を流れ
培養液とは向流的もしくは並流的に移動することに々る
。この際、循環撒布される培養液は支持体上の細胞表面
を薄層状に落下するが、この培養液とガスは効率よく接
触することになり、細胞の接着面積と同面積のガス接触
面積を有することから、ガス成分の培養液中への移行が
極めて効率よく行なわれる。
Simultaneously with the start of culture, a gas having a required gas composition is aerated, if necessary. The lower part of the culture tank is also vented through a gas dispersion device provided at the upper part, and the gas composition or the amount of aeration is set to be effective for the target cells. The gas introduced into the culture tank flows through the pores of the support and moves countercurrently or cocurrently with the culture solution. At this time, the circulating culture solution falls on the cell surface on the support in a thin layer, but this culture solution and gas come into contact with each other efficiently, and the gas contact area is the same as the cell adhesion area. Because of this, the gas components are transferred into the culture solution extremely efficiently.

培養が進行すれば、細胞は支持体全面に増殖し、それと
同時に各種生産物が培養液中に溶出してくるようになる
As the culture progresses, cells proliferate over the entire surface of the support, and at the same time various products begin to be eluted into the culture medium.

ここで培養液の一部は常に引き抜きながら、同量の新鮮
な培養液が添加され、更に培養は続けられる。
Here, a portion of the culture solution is constantly withdrawn, and the same amount of fresh culture solution is added, and the culture is continued.

旧培養液と新鮮培養液との交換を適当な量に設定すれば
、培養槽中の細胞が活性を有するかなり長期間連続運転
が可能となる。
If the amount of exchange between old culture solution and fresh culture solution is set to an appropriate amount, continuous operation can be performed for a fairly long period of time while the cells in the culture tank remain active.

細胞培養液に於ては血清が利用される場合が多いが、血
清を添加することにより、細胞が産生じた少量の生物学
的物質の回収が極めて困難である。
Serum is often used in cell culture media, but adding serum makes it extremely difficult to recover small amounts of biological substances produced by cells.

しかし、本発明においては、培養液の交換がきわめて簡
単に行うことができるので、物質生産用培養液に途中か
ら切り換え、生産物の分離を容易にすることができるも
のである。また、通気に関しては、細胞の性状によって
ガス組成を変更する必要があるが、本発明においては、
このガス組成は自由に設定できるとともに、支持体空隙
を通過することから従来のように泡立ちを心配する必要
がなく、1だ培養液中にガスを通気する際に問題となる
気泡の分散、表面積の増大等に関する考慮は全く不要と
なるのである。
However, in the present invention, since the culture solution can be exchanged very easily, it is possible to switch to the culture solution for substance production midway through the process, making it easy to separate the product. Regarding ventilation, it is necessary to change the gas composition depending on the properties of the cells, but in the present invention,
The gas composition can be freely set, and since it passes through the support voids, there is no need to worry about foaming as in the conventional case, and there is no need to worry about bubble dispersion or surface area, which is a problem when gas is aerated into the culture solution. There is no need to consider the increase in

一般に、細胞は活性を有する期間には限度があるために
、細胞の不活性化とともに別の活性を有する細胞の増殖
が必要となる。本発明においては目的生産物の生産量の
低下とともに培養液の代りに例えばトリプシン溶液のよ
うな細胞剥離作用を有する液を撒布し、続いて新鮮培養
液を循環撒布することにより支持体上に残存する一部細
胞の増殖を行なわせ新たな増殖細胞により培養槽の連続
利用が可能と々るのである。
Generally, cells have a limited period of activity, so it is necessary to inactivate the cells and to proliferate cells with other activities. In the present invention, when the production amount of the target product decreases, a solution having a cell detachment effect, such as a trypsin solution, is sprayed in place of the culture solution, and then a fresh culture solution is circulated and the cells remain on the support. By allowing some of the cells to proliferate, the culture tank can be used continuously by newly proliferating cells.

1だ、目的とする物質を多量生産させる場合は、多槽式
にして、順次細胞の活性化を行なえば、効率的に培養を
行って全体の生産性を定常化することが可能となる。
1. If you want to produce a large amount of a target substance, use a multi-vessel system and sequentially activate the cells, making it possible to culture efficiently and stabilize the overall productivity.

本発明の装置を図面によって説明すれば、第1図は支持
体1を示す。第2図は培養装置の概略図で、第6図は培
養装置の縦断物、明図である。
To explain the device of the invention with reference to the drawings, FIG. 1 shows a support 1. In FIG. FIG. 2 is a schematic diagram of the culture device, and FIG. 6 is a longitudinal cross-sectional view of the culture device.

?は培養槽を示し、3は支持体収容室で、これは支持体
1が一杯に充填されている。4け培養液撒布装置で、細
孔5.5・・・・・・が多数あけられ、送られて来た培
養液がシャワー状に支持体にふりかかるように々つてい
る。6は目皿で、これには気体吹出ロアが適宜設けられ
ている。8は培養槽壁で、9は金網で、これらによって
支持体収容室6を形成している。10はジャケットで、
温水人口11から温水を入れ、温水出口12から排出し
て、培養槽を加温するようになっている。、15は目皿
で、これには気体吹出口14が適宜設けられている。培
養槽底部15中央部には気体吹出本管16が設けられ、
気体導入管17から入れられた気体を吹出すようになっ
ている。18は培養液導入管で、19は培養液排出管で
、タンク20に入れられた培養液は培養液導入管18か
ら培養槽に送られ、培養液排出管19を通ってタンク2
0に循環する。タンク20は温水機21から送られてく
る温水によって20〜40℃程度に加温されるようにな
っている。抜き取りタンク22には循環培養液の一部を
抜き取って入れられ、また培養液タンク23には新鮮な
培養液が入れられ、抜き取られた部分が補充されるよう
になっている。
? 3 indicates a culture tank, and 3 is a support housing chamber, which is completely filled with the support 1. A large number of pores 5, 5, etc. are opened using a 4-cell culture solution dispersing device, and the culture solution sent therein is sprinkled onto the support in a shower-like manner. Reference numeral 6 denotes a perforated plate, on which a gas blowing lower is appropriately provided. Reference numeral 8 represents a culture tank wall, and reference numeral 9 represents a wire mesh, which together form a support housing chamber 6. 10 is a jacket,
Hot water is introduced from a hot water outlet 11 and discharged from a hot water outlet 12 to heat the culture tank. , 15 is a perforated plate, in which a gas outlet 14 is appropriately provided. A gas blowing main pipe 16 is provided in the center of the culture tank bottom 15,
The gas introduced through the gas introduction pipe 17 is blown out. 18 is a culture solution introduction pipe, 19 is a culture solution discharge pipe, and the culture solution put in the tank 20 is sent from the culture solution introduction pipe 18 to the culture tank, passes through the culture solution discharge pipe 19, and is transferred to the tank 2.
Cycles to 0. The tank 20 is heated to about 20 to 40°C by hot water sent from a water heater 21. A part of the circulating culture solution is drawn out and put into the sampling tank 22, and a fresh culture solution is put into the culture solution tank 23, so that the part that has been drawn out is replenished.

また、炭酸ガスボンベ24からは炭酸ガスが流量計25
を経て、ポンプ26から取入れ、流量計27を経て、酸
28、アルカリ29で洗滌された空気と混合され、加温
機31で67℃程度に加温されて、気体導入管17を軽
て培養槽に導入される。排出される気体は排出管32を
紗て循環され、一部はフィルター33を経て外気中へ放
出される。
In addition, carbon dioxide gas flows from the carbon dioxide gas cylinder 24 to the flowmeter 25.
It is taken in from the pump 26, passed through the flow meter 27, mixed with air washed with acid 28 and alkali 29, heated to about 67°C by the warming machine 31, and then gently inserted into the gas introduction pipe 17 to culture. introduced into the tank. The discharged gas is circulated through the discharge pipe 32, and a portion passes through the filter 33 and is discharged into the outside air.

次に本発明の実施例を示す。Next, examples of the present invention will be shown.

実施例1 プラスチックシャーレにEagles’ minimu
messential medium(MEM )に牛
血清1%添加した培養液で培養したL細胞を0,125
%トリプシン溶液(BDTAを含む)で細胞を剥離し、
同培養液で細胞の洗浄を行う。
Example 1 Eagles' minimu in a plastic petri dish
L cells cultured in messential medium (MEM) with 1% bovine serum added to 0.125
Detach the cells with % trypsin solution (containing BDTA),
Wash the cells with the same culture solution.

洗浄したL細胞を同培養液に懸濁させた後、ガス滅菌し
た充填材を含む大型プラスチックシャーレに無菌的に注
入し5%CO2を含むふ卵器中で24時間培養する。
After suspending the washed L cells in the same culture solution, they are aseptically injected into a large plastic petri dish containing gas-sterilized filling material and cultured for 24 hours in an incubator containing 5% CO2.

その後、第1図の支持体を充填した第2図、第3図の培
養槽に、同培養液を循環撒布するとともK 5 % C
O2を通気する。この際、同培養液を37℃に保温する
とともにジャケットに37℃の温水を循環し保温する。
Thereafter, the same culture solution was circulated in the culture tanks shown in FIGS. 2 and 3 filled with the support shown in FIG. 1, and K 5 % C.
Vent with O2. At this time, the culture solution is kept warm at 37°C and warm water at 37°C is circulated through the jacket.

5%CO2通気下で同培養液を循環撒布して約1週間後
には充填材表面が細胞で被われる。なお、培養液の循環
撒布量はQ、1V/V/M、通気量は0.05 V /
V 7M トLJ、=。
Approximately one week after circulating the same culture solution under 5% CO2 aeration, the surface of the filling material is covered with cells. The amount of circulating culture solution is Q, 1 V/V/M, and the amount of aeration is 0.05 V/
V 7M To LJ,=.

実施例2 プラスチックシャーレにDulbeccos’ Mod
ifiedEagle Medium(D M B )
に牛血清10チ添加した培養液で培養した3T3細胞を
0.125%)IJプシン溶液(EDTAを含む)で細
胞を剥離し、同培養液で細胞の洗浄を行う。洗浄した6
T3細胞を同培養液に懸濁させた後、ガス滅菌した充填
材を含む大型プラスチックシャーレに無菌的に注入し5
%C02を含むふ卵器中で24時間培養する。
Example 2 Dulbeccos' Mod in a plastic petri dish
ifiedEagle Medium (DMB)
3T3 cells cultured in a culture solution containing 10 g of bovine serum (0.125%) were detached with an IJ pushin solution (containing EDTA), and the cells were washed with the same culture solution. washed 6
After suspending T3 cells in the same culture solution, they were aseptically injected into a large plastic petri dish containing gas-sterilized filling material.
Culture in an incubator containing %C02 for 24 hours.

その後、第1図の支持体を充填した第2図、第3図の培
養槽に同培養液を循環撒布するとともに5% Co、を
通気する。この際同培養液を37℃に保温するとともに
ジャケット[37℃の温水を循環し保温する。
Thereafter, the same culture solution was circulated in the culture tank shown in FIGS. 2 and 3 filled with the support shown in FIG. 1, and 5% Co was aerated therein. At this time, the culture solution was kept warm at 37°C and kept warm by circulating warm water at 37°C in a jacket.

5 % CO2通気下で同培養液を循環撒布して約1週
間後には充填材表面が細胞で被われる。なお、培養液の
循環撒布量は0.1 ’J/V/M、通気量は0.05
 V/V/Mとした。
Approximately one week after circulating the same culture solution under 5% CO2 aeration, the surface of the filling material is covered with cells. The amount of circulating culture solution was 0.1'J/V/M, and the amount of aeration was 0.05.
V/V/M.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は支持体の一例を示す図で、 第2図は本発明装置の概略図で、 第3図は本発明装置の一部断面訣1明図である。 1・・・支持体、?・・・培養槽、5・・・細孔、6・
・・目皿、?・・・金網 代理人 弁理士 戸 1)親 男 第  11!l
FIG. 1 is a diagram showing an example of a support, FIG. 2 is a schematic diagram of the device of the present invention, and FIG. 3 is a partially sectional view of the device of the present invention. 1... Support? ... Culture tank, 5... Pore, 6.
...eye plate? ... wire mesh agent patent attorney door 1) parent male number 11! l

Claims (3)

【特許請求の範囲】[Claims] (1)接着性を有する細胞を、培養液中に浸漬されてい
ない支持体上に増殖させ、該支持体上には培養液を接触
せしめて培養することを特徴とする細胞培養方法。
(1) A cell culture method, which comprises growing adhesive cells on a support that is not immersed in a culture solution, and culturing the support by bringing the culture solution into contact with the support.
(2)支持体上に、必要なガス組成を有する気体を培養
液と向流的もしくは並流的に通気接触せしめる特許請求
範囲第一項記載の細胞培養方法。
(2) The cell culture method according to claim 1, wherein a gas having a necessary gas composition is brought into contact with the culture solution by aeration on the support in a countercurrent or cocurrent manner.
(3)培養液及び気体を通過可能とした支持体収容室を
有する培養槽と該培養槽上部に設けた培養液撒布装置及
び該培養槽下部もしくは上部に設けた気体分散装置から
なる細胞培養装置。
(3) A cell culture device consisting of a culture tank having a support housing chamber through which culture solution and gas can pass, a culture solution spreading device installed at the top of the culture tank, and a gas dispersion device installed at the bottom or top of the culture tank. .
JP57169734A 1982-09-30 1982-09-30 Method and apparatus for cell culture Pending JPS5959187A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57169734A JPS5959187A (en) 1982-09-30 1982-09-30 Method and apparatus for cell culture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57169734A JPS5959187A (en) 1982-09-30 1982-09-30 Method and apparatus for cell culture

Publications (1)

Publication Number Publication Date
JPS5959187A true JPS5959187A (en) 1984-04-04

Family

ID=15891854

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57169734A Pending JPS5959187A (en) 1982-09-30 1982-09-30 Method and apparatus for cell culture

Country Status (1)

Country Link
JP (1) JPS5959187A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62171670A (en) * 1985-10-20 1987-07-28 イエダ リサ−チ アンド デベロツプメント コンパニ− リミテツド Packing material for culture container
US5376548A (en) * 1990-06-29 1994-12-27 Fuji Photo Film Co., Ltd. Bioreactor apparatus
WO2000068357A1 (en) * 1999-05-06 2000-11-16 Universite Laval Scalable bioreactor culture process and system for the maturation of conifer somatic embryos
JP2003529362A (en) * 2000-04-03 2003-10-07 ローテック ゲゼルシャフト フュア ビオアクティーヴェ ヴィルクシュトッフェ ミット ベシュレンクテル ハフツング Culture device for plant or animal tissue culture

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62171670A (en) * 1985-10-20 1987-07-28 イエダ リサ−チ アンド デベロツプメント コンパニ− リミテツド Packing material for culture container
US5376548A (en) * 1990-06-29 1994-12-27 Fuji Photo Film Co., Ltd. Bioreactor apparatus
WO2000068357A1 (en) * 1999-05-06 2000-11-16 Universite Laval Scalable bioreactor culture process and system for the maturation of conifer somatic embryos
US7235402B2 (en) 1999-05-06 2007-06-26 Universite Laval Scalable bioreactor culture process and system for the maturation of conifer somatic embryos
JP2003529362A (en) * 2000-04-03 2003-10-07 ローテック ゲゼルシャフト フュア ビオアクティーヴェ ヴィルクシュトッフェ ミット ベシュレンクテル ハフツング Culture device for plant or animal tissue culture

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