JPH0775550A - Cell culture apparatus - Google Patents

Cell culture apparatus

Info

Publication number
JPH0775550A
JPH0775550A JP24852193A JP24852193A JPH0775550A JP H0775550 A JPH0775550 A JP H0775550A JP 24852193 A JP24852193 A JP 24852193A JP 24852193 A JP24852193 A JP 24852193A JP H0775550 A JPH0775550 A JP H0775550A
Authority
JP
Japan
Prior art keywords
cells
cell culture
state
culture
culture tank
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
JP24852193A
Other languages
Japanese (ja)
Inventor
Tadashi Adachi
正 足立
Shin Taniguchi
紳 谷口
Akiko Miya
晶子 宮
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.)
Ebara Corp
Original Assignee
Ebara Corp
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 Ebara Corp filed Critical Ebara Corp
Priority to JP24852193A priority Critical patent/JPH0775550A/en
Publication of JPH0775550A publication Critical patent/JPH0775550A/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M41/00Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • C12M41/42Means for regulation, monitoring, measurement or control, e.g. flow regulation of agitation speed
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M27/00Means for mixing, agitating or circulating fluids in the vessel
    • C12M27/02Stirrer or mobile mixing elements
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M41/00Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M41/00Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • C12M41/30Means for regulation, monitoring, measurement or control, e.g. flow regulation of concentration
    • C12M41/36Means for regulation, monitoring, measurement or control, e.g. flow regulation of concentration of biomass, e.g. colony counters or by turbidity measurements

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Zoology (AREA)
  • Wood Science & Technology (AREA)
  • Microbiology (AREA)
  • Sustainable Development (AREA)
  • Biotechnology (AREA)
  • Biomedical Technology (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Analytical Chemistry (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)

Abstract

PURPOSE:To provide a cell culture tank which prevents the cells from being broken by a strong stress, can culture the cells growing in a fibrous form without pellet formation or lumping, and can prevent the cells immobilized to the support from being peeled off. CONSTITUTION:In a culture tank for mammalian or plant cells and/or cells of microorganisms, the culture tank is provided with a stirring mechanism which can arbitrarily vary the liquid flow rate and turn the flow direction. The mechanism is a cage type of rotor 2 in which the screw blades 10 fitted to the rotation shaft 3 for the rotor and the peripheral blades 9 have the structures to cause the flows reverse to each other. It is preferred that the cell culture installation is provided with a means for observation of the cell conditions and a system for controlling the flow rate and/or the flow direction of the stirring mechanism on the basis of the observation.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、動植物細胞及び/又は
微生物細胞の培養装置に係わり、特に細胞強度の弱い細
胞及び/又は糸状に生育する細胞を培養する装置に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for culturing animal and plant cells and / or microbial cells, and more particularly to an apparatus for culturing cells having weak cell strength and / or cells that grow into filaments.

【0002】[0002]

【従来の技術】浮遊性の動植物細胞及び/又は微生物細
胞の培養及び/又は浮遊性担体に固定化した付着性の動
植物細胞及び/又は微生物細胞の培養を目的とする培養
装置においては、該細胞の増殖に必要な酸素あるいは炭
酸ガスあるいはその他のガスを供給し、且つ培養液と該
細胞とを混合して細胞の代謝生産物の物質移動を促進す
るよう均一な懸濁状態を達成するために通気攪拌が行わ
れる。
2. Description of the Related Art In a culture apparatus for the purpose of culturing floating animal and plant cells and / or microbial cells and / or culturing adherent animal and plant cells and / or microbial cells immobilized on a floating carrier, Oxygen or carbon dioxide gas or other gas required for the growth of the cells is supplied, and the culture medium and the cells are mixed to achieve a uniform suspension state so as to promote the mass transfer of the metabolic products of the cells. Aeration and stirring is performed.

【0003】従来の培養装置にはこの通気攪拌を気体だ
けで行うものと、通気と機械的攪拌を併用するものとが
あるが、通常、気泡を微細化して分散させ、且つ培養液
の乱流状態を高めるために攪拌羽根が設けられ、通気と
併用されている。培養液中の物質移動速度は攪拌動力と
正の相関があるので、物質移動速度を大きくしようとす
る場合、攪拌強度を高める必要がある。
[0003] Conventional culture devices include those that perform aeration and stirring only with gas, and those that use aeration and mechanical stirring together. Usually, air bubbles are finely dispersed and turbulent flow of the culture solution is used. Stirrer blades are provided to enhance the condition and are used together with ventilation. Since the mass transfer rate in the culture solution has a positive correlation with the stirring power, it is necessary to increase the stirring strength in order to increase the mass transfer rate.

【0004】しかし、特に細胞強度の弱い細胞を培養す
る場合には攪拌強度をいたずらに高めると細胞にかかる
剪断力が増大し、細胞が破砕するに至る。このため従来
より、培養細胞に剪断力を与えずに物質移動速度を高め
るような攪拌羽根の形状が工夫されてきたが、細胞の状
態にきめ細かく対応できるまでには至っていない。一
方、かびや放線菌のような糸状に生育する細胞の場合
は、通気攪拌により菌体がペレット化したり、塊状にな
って物質移動が阻害される場合がしばしばある。また固
体表面に付着して増殖する細胞を浮遊性の担体の表面に
固定化して培養する場合は、攪拌強度をいたずらに高め
ると、担体表面にかかる剪断力により細胞が剥離すると
いう障害がある。
However, especially when culturing cells having weak cell strength, if the stirring strength is unnecessarily increased, the shearing force applied to the cells is increased and the cells are crushed. For this reason, conventionally, the shape of the stirring blade has been devised so as to increase the mass transfer rate without giving shearing force to the cultured cells, but it has not been possible to finely respond to the state of the cells. On the other hand, in the case of filamentous cells such as molds and actinomycetes, the cells are often pelletized or agglomerated by aeration and stirring to inhibit mass transfer. When cells that adhere to the solid surface and proliferate are immobilized and cultivated on the surface of a floating carrier, if the stirring strength is unnecessarily increased, the shearing force applied to the carrier surface causes the cells to peel off.

【0005】[0005]

【発明が解決しようとする課題】本発明は、細胞強度の
弱い細胞を培養するにあたり細胞に強い剪断力を与えて
細胞が破砕することを防ぐことができ、また、糸状に生
育する細胞を培養するにあたり、細胞ペレット化した
り、塊状になることを防ぐことができると共に、浮遊性
担体に固定化した細胞が剥離することを防ぐことができ
る細胞培養装置を提供することを課題とする。
DISCLOSURE OF THE INVENTION In the present invention, when culturing cells having weak cell strength, a strong shearing force can be applied to the cells to prevent the cells from crushing, and the cells that grow into filaments are cultivated. In doing so, it is an object of the present invention to provide a cell culture device capable of preventing cell pelletization or lump formation and preventing detachment of cells immobilized on a floating carrier.

【0006】[0006]

【課題を解決するための手段】上記課題を解決するため
に、本発明では、動植物細胞及び/又は微生物細胞を培
養する培養装置において、該培養装置内に流速を任意に
変動できると共に流れの方向を逆転させることが可能な
構造の機械的攪拌手段を備えていることとしたものであ
る。上記培養装置において、機械的攪拌手段は、かご型
ローターであり、回転軸に取付けられたスクリュー羽根
と周辺部の羽根が逆方向の流れを作ることができる構造
になっているのがよく、また該攪拌手段は、攪拌を停止
した状態を一定時間間隔で繰り返することが可能な構造
となっているのがよい。
In order to solve the above problems, in the present invention, in a culture device for culturing animal and plant cells and / or microbial cells, the flow velocity can be arbitrarily changed in the culture device and the flow direction can be changed. The mechanical stirring means having a structure capable of reversing the above is provided. In the above culturing device, the mechanical stirring means is a cage rotor, and it is preferable that the screw blades attached to the rotating shaft and the peripheral blades have a structure capable of forming a flow in the opposite direction. The stirring means preferably has a structure capable of repeating a state in which stirring is stopped at regular time intervals.

【0007】また、前記培養装置は、機械的攪拌手段の
流速及び/又は流れの方向を制御するための培養槽内の
細胞の状態を観察する手段とそれに基づいて制御する制
御系を備えているのがよい。前記培養槽内の細胞の状態
の観察手段は、培養槽内の細胞量をオンライン計測する
手段、又は培養槽内の細胞の破損状態をオンライン計測
する手段により行うのがよい。
Further, the culture apparatus comprises means for observing the state of cells in the culture tank for controlling the flow velocity and / or flow direction of the mechanical stirring means, and a control system for controlling based on the means. Is good. The means for observing the state of cells in the culture tank is preferably performed by means for online measuring the amount of cells in the culture tank or means for measuring online the broken state of cells in the culture tank.

【0008】上記のように、本発明では、培養槽内の細
胞の状態を観察しつつ、機械的攪拌により流速を適宜変
動させることにより、及び/又は流れの方向を適宜逆転
させることにより、及び適宜攪拌を停止させることによ
り細胞強度の弱い動植物細胞及び/又は微生物細胞及び
/又は糸状に生育する細胞及び/又は微生物細胞及び/
又は浮遊性担体に固定化した細胞を培養することができ
る。
As described above, according to the present invention, while observing the state of cells in the culture tank, the flow velocity is appropriately changed by mechanical stirring, and / or the flow direction is appropriately reversed, and Animal and plant cells and / or microbial cells with weak cell strength and / or cells and / or microbial cells that grow in a filamentous form and / or
Alternatively, cells immobilized on a floating carrier can be cultured.

【0009】次に本発明を詳細に説明する。培養槽内の
機械的攪拌手段は、かご型ローターがよく、回転軸に取
付けられたスクリュー羽根と周辺部の羽根が逆方向の流
れを作ることができる構造となっている。これにより、
槽内の細胞に強い剪断力を与えずに培養液を十分に乱流
状態にすることができ、物質移動速度を高く維持でき
る。また、流速を適宜変動させることにより、及び/又
は流れの方向を適宜逆転させることにより、及び適宜攪
拌を停止させることにより細胞強度の弱い細胞に過度の
剪断力を与えることなく、また糸状に生育する細胞がペ
レット化したり、塊状になることなく、また浮遊性担体
に固定化した細胞が剥離することなく培養することがで
きる。
Next, the present invention will be described in detail. The mechanical stirring means in the culture tank is preferably a squirrel-cage rotor, and has a structure in which the screw blades attached to the rotating shaft and the blades in the peripheral portion can make flows in opposite directions. This allows
The culture solution can be sufficiently turbulent without giving a strong shearing force to the cells in the tank, and the mass transfer rate can be kept high. In addition, by appropriately changing the flow rate and / or by reversing the flow direction as appropriate and stopping the agitation as appropriate, the cells with weak cell strength are not applied with excessive shearing force, and are grown into filaments. The cells to be cultured can be cultured without pelleting or clumping, and without detaching the cells immobilized on the floating carrier.

【0010】本発明の培養装置の機械的攪拌手段は、培
養槽内の細胞の状態を観察し、これを判定して流速及び
/又は流れの方向の逆転頻度を決定する制御系を備えて
いる。培養槽内の細胞の状態を観察する手段としては、
培養槽内の細胞量をモニターする方法及び/又は培養槽
内の細胞の破損状態をモニターする方法があるが、いず
れもオンラインで測定したデータを計測制御用コンピュ
ータに取り込むことが望ましい。
The mechanical stirring means of the culture apparatus of the present invention is equipped with a control system for observing the state of cells in the culture tank and judging the state of the cells to determine the flow velocity and / or the reversal frequency of the flow direction. . As means for observing the state of cells in the culture tank,
There is a method of monitoring the amount of cells in the culture tank and / or a method of monitoring the damage state of the cells in the culture tank. In both cases, it is desirable to import the data measured online into the measurement control computer.

【0011】培養槽内の細胞量をモニターする方法とし
ては、培養液の吸光度を測定する方法、培養液のアデノ
シン三リン酸(ATP)濃度を定量する方法、培養液中
の細胞数を計数する方法、培養液中の細胞重量を計測す
る方法、培養液中の蛍光物質を定量する方法等のいずれ
でもよいが、培養対象の細胞に最も適した方法を採用す
ることが望ましい。また、培養槽内の細胞の破損状態を
モニターする方法としては培養液の顕微鏡視野を画像解
析する方法、培養液のろ液中の核酸(DNA)量を測定
する方法、培養液の一部をとって静置し、上澄液の濁度
あるいは吸光度を測定する方法等のいずれでもよい。
As a method of monitoring the amount of cells in the culture tank, a method of measuring the absorbance of the culture solution, a method of quantifying the concentration of adenosine triphosphate (ATP) in the culture solution, and counting the number of cells in the culture solution Any of the method, the method of measuring the cell weight in the culture solution, the method of quantifying the fluorescent substance in the culture solution and the like may be used, but it is desirable to adopt the method most suitable for the cells to be cultured. In addition, as a method of monitoring the damage state of cells in the culture tank, a method of image analysis of a microscopic field of the culture solution, a method of measuring the amount of nucleic acid (DNA) in the filtrate of the culture solution, and a part of the culture solution are used. Any method such as measuring the turbidity or the absorbance of the supernatant by allowing it to stand still may be used.

【0012】上記の方法により測定された培養槽内の細
胞の状態を示すデータは、計測制御用のコンピュータに
取り込まれる。コンピュータではデータに基づき細胞の
状態を判定して、流速変動及び/又は流れ方向の変動の
条件を決定し、攪拌装置の運転状態を変更する。流速変
動における操作因子は流速即ち攪拌強度の回転速度、各
流速における継続時間、及び攪拌停止時間であり、ま
た、流れ方向の変動における操作因子は流れ方向変更頻
度、各流れの方向の継続時間、及び攪拌停止時間であ
る。
The data indicating the state of the cells in the culture tank measured by the above method is loaded into a computer for measurement control. The computer determines the state of the cells based on the data, determines the conditions of flow velocity fluctuation and / or flow direction fluctuation, and changes the operating state of the stirring device. The operation factors in the flow velocity fluctuation are the flow velocity, that is, the rotation speed of the stirring intensity, the duration at each flow velocity, and the stirring stop time, and the operation factors in the variation in the flow direction are the flow direction change frequency, the duration of each flow direction, And the stirring stop time.

【0013】[0013]

【作用】浮遊性の動植物細胞及び/又は微生物細胞の中
でも、特に細胞強度が弱い細胞の培養においては、物質
移動速度を高く維持することを目的とした通気攪拌、特
に機械的攪拌が細胞に強い剪断力を与えて細胞を破壊
し、細胞の増殖を阻害することが実用面で大きな障害に
なっている。また糸状に生育する細胞では通気攪拌によ
り細胞がペレット化したり、塊状になって正常な増殖が
阻害されることがしばしばある。
[Effect] Among floating animal and plant cells and / or microbial cells, particularly in the culture of cells having weak cell strength, aeration stirring for maintaining a high mass transfer rate, particularly mechanical stirring is strong for the cells. A major obstacle to practical use is applying a shearing force to destroy cells and inhibit cell growth. In the case of cells that grow in the form of filaments, the cells are often pelleted or agglomerated by aeration and agitation to prevent normal growth.

【0014】本発明は、機械的攪拌において、攪拌速度
及び方向が一定の状態で長時間維持された場合は細胞破
壊や糸状性細胞のペレット化が起きるが、流速を適宜変
動させたり、流れの方向を変化させ、また適宜攪拌を停
止することにより、細胞の破壊を防止でき、及び/又は
糸状性細胞のペレット化を防止でき、及び/又は浮遊性
担体に固定化した細胞の剥離を防止できることを見いだ
し完成するに至った。
In the present invention, in mechanical agitation, when the agitation speed and direction are kept constant for a long time, cell destruction and pelletization of filamentous cells occur, but the flow rate can be appropriately changed or the flow rate can be changed. By changing the direction and stopping the stirring as appropriate, it is possible to prevent the destruction of cells, and / or to prevent the pelletization of filamentous cells, and / or to prevent the detachment of cells immobilized on a floating carrier. I found it and came to complete it.

【0015】また本発明は、機械的攪拌の方法としては
かご型ローターが最も細胞に与える剪断力が少ないが、
特に回転軸にスクリュー羽根を設け、その羽根と周辺部
の羽根が逆方向の流れを作るような構造にした場合、極
めて少ない回転数で培養液を十分に乱流状態に維持する
ことができることを見いだし完成するに至った。一般に
物質移動速度は攪拌動力と正の相関があるので、物質移
動速度を高くするためには攪拌強度を上げる必要がある
が、細胞破壊を引き起こす可能性があるので安全側で攪
拌強度を小さく、即ち物質移動速度を低く維持せざるを
得ない。これに対し、本発明においては細胞の状態を把
握しながら攪拌条件を変動させるため、常に細胞が活発
に増殖する状態を維持できる。
Further, in the present invention, as a mechanical stirring method, the cage rotor gives the least shearing force to the cells,
In particular, if a screw blade is provided on the rotating shaft and the blade and the peripheral blades make a flow in the opposite direction, it is possible to maintain the culture solution in a sufficiently turbulent state at an extremely low rotational speed. Found and completed. Generally, since the mass transfer rate has a positive correlation with the stirring power, it is necessary to increase the stirring strength in order to increase the mass transfer rate, but since it may cause cell destruction, the stirring strength should be small on the safe side. That is, the mass transfer rate must be kept low. On the other hand, in the present invention, since the stirring conditions are changed while grasping the state of the cells, the state in which the cells are actively growing can be always maintained.

【0016】[0016]

【実施例】以下、本発明を図面を用いて具体的に説明す
るが、本発明はこれに限定されない。 実施例1 図1に本発明の一例である培養装置の断面概略図を示
す。図1は培養槽1内にかご型ローター2を備えた培養
装置の概略図であり、3は回転軸、4は散気管、5はマ
グネットカップリング、6は空気培養用ガス導入管、7
はセンサー挿入口である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be specifically described below with reference to the drawings, but the present invention is not limited thereto. Example 1 FIG. 1 shows a schematic cross-sectional view of a culture apparatus which is an example of the present invention. FIG. 1 is a schematic view of a culturing apparatus provided with a squirrel-cage rotor 2 in a culturing tank 1, 3 is a rotating shaft, 4 is an air diffuser, 5 is a magnet coupling, 6 is a gas introducing tube for air culture, and 7
Is a sensor insertion port.

【0017】前記ローター2は回転数を任意に変化させ
ることができ、また回転方向を適宜逆転させることがで
き、また回転を適宜停止することができるので、細胞強
度の弱い動植物細胞及び/又は微生物細胞を破壊するこ
となく培養することができる。また、糸状に生育する細
胞の場合には細胞がペレット化したり塊状になったりす
ることを防いで、安定した培養ができる。さらに固体表
面に付着して生育する細胞の場合には、浮遊性担体表面
に固定化した状態で、剥離することを防いで、安定した
培養ができる。
Since the rotor 2 can arbitrarily change the rotation speed, can reverse the rotation direction as appropriate, and can appropriately stop the rotation, the animal and plant cells and / or microorganisms having weak cell strength can be obtained. It can be cultured without destroying cells. Further, in the case of cells that grow in the form of filaments, it is possible to prevent the cells from being pelletized or clumped, and to perform stable culture. Further, in the case of cells that grow by adhering to a solid surface, they can be stably cultured by preventing them from peeling off while being immobilized on the surface of a floating carrier.

【0018】図2は攪拌用ローターの構造の一例を示し
た断面図である。回転軸3に取付けられたスクリュー羽
根10とローターの外枠に取付けられた羽根9によっ
て、正転時には、ローターの内側では回転軸に沿った上
昇流、またローターの外側では培養槽内壁に沿った下降
流が生じる。さらに回転軸上部に取付けられたタービン
羽根8により正転時には、遠心流が生じる。一方、逆転
時には、ローターの内側では回転に沿った下降流、ロー
ターの外側では培養槽内壁に沿った上昇流、さらに回転
軸上部に取付けられたタービン羽根8により求心流が生
じる。
FIG. 2 is a sectional view showing an example of the structure of the stirring rotor. By the screw blades 10 attached to the rotating shaft 3 and the blades 9 attached to the outer frame of the rotor, the forward flow along the rotating shaft inside the rotor and the inner wall of the culture tank outside the rotor at the time of normal rotation. Downflow occurs. Further, a centrifugal flow is generated at the time of normal rotation by the turbine blades 8 attached to the upper part of the rotating shaft. On the other hand, at the time of reverse rotation, a descending flow along the rotation inside the rotor, an ascending flow along the inner wall of the culture tank outside the rotor, and a centripetal flow due to the turbine blades 8 attached to the upper part of the rotating shaft.

【0019】図3は細胞の破砕状態を培養液上澄のDN
A量を測定することで観察し、ローターの回転数、方向
を制御する装置の一例の概略図である。培養液11の一
部を採取する配管系12の一部に沈降用セル13を設
け、ポンプ20で培養液を一定時間流した後、電磁弁1
9を閉じ、一定時間放置する。細胞が沈殿した上澄部分
の波長254nmにおける吸光度を吸光度計14で測定し
た後、電磁弁を開いて再びポンプで送液し、この操作を
繰り返す。
FIG. 3 shows the disrupted state of cells in DN of the supernatant of the culture solution.
It is a schematic diagram of an example of a device which observes by measuring the amount of A and controls the number of rotations and direction of a rotor. A settling cell 13 is provided in a part of a piping system 12 for collecting a part of the culture solution 11, and the culture solution is flowed by a pump 20 for a certain period of time.
Close 9 and leave for a certain time. After measuring the absorbance at a wavelength of 254 nm of the supernatant portion in which the cells are precipitated by the absorptiometer 14, the electromagnetic valve is opened and the solution is pumped again, and this operation is repeated.

【0020】吸光度計で測定されたデータはケーブル1
5を通じて計測制御用コンピュータ16に送られ、デー
タ解析が行われ、回転用モーター18に対する制御信号
がケーブル17を通じてモーターに送られ、ローターの
回転数、回転方向、時間等を適宜変化させる。なお、沈
降性が非常に悪い細胞に対しては、自然沈降ではなく遠
心分離等の機械的沈降やフィルターによるろ過で上澄液
を搾取してもよい。
The data measured by the absorptiometer is cable 1
5 is sent to the measurement control computer 16 for data analysis, and a control signal for the rotation motor 18 is sent to the motor through the cable 17 to appropriately change the rotation speed, rotation direction, time, etc. of the rotor. For cells having a very poor sedimentation property, the supernatant may be squeezed by mechanical sedimentation such as centrifugation or filtration by a filter instead of spontaneous sedimentation.

【0021】また、細胞の状態の観察方法としては図3
の沈降用セル13の代わりにフローセルを設け、吸光度
を測定して細胞量を観察する方法、図3の沈降用セル1
3の代わりに自動プレパラート作成装置を、また吸光度
計14の代わりに顕微鏡を設け、顕微鏡視野をコンピュ
ータに送り画像解析して細胞の破壊状態を観察する方法
等があり、いずれを用いてもよい。
As a method of observing the state of cells, FIG.
3 is a method for observing the cell amount by measuring the absorbance by providing a flow cell instead of the sedimentation cell 13 in FIG.
There is a method in which an automatic slide preparation device is used instead of 3, and a microscope is provided instead of the absorptiometer 14, and the microscope visual field is sent to a computer to analyze the image to observe the state of cell destruction, and any method may be used.

【0022】[0022]

【発明の効果】本発明によれば、細胞強度の弱い動植物
細胞及び/又は微生物細胞を破壊することなく培養する
ことができ、また糸状に生育する細胞の場合には細胞が
ペレット化したり塊状になったりすることを防いで、安
定した培養ができ、さらに固体表面に付着して生育する
細胞の場合には、浮遊性担体表面に固定化した状態で、
剥離することを防いで、安定した培養ができる。
INDUSTRIAL APPLICABILITY According to the present invention, animal and plant cells and / or microbial cells having weak cell strength can be cultured without destroying them, and in the case of cells that grow in a filamentous form, the cells are pelleted or aggregated. In the case of cells that can be grown stably by adhering to a solid surface while preventing them from becoming loose, in the state of being immobilized on the floating carrier surface,
Prevents peeling and enables stable culture.

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

【図1】本発明の培養槽の断面概略図。FIG. 1 is a schematic sectional view of a culture tank of the present invention.

【図2】図1の攪拌用ローターの拡大断面図。FIG. 2 is an enlarged sectional view of the stirring rotor of FIG.

【図3】本発明の細胞状態の観察装置及び攪拌制御装置
を備えた培養装置の概略図。
FIG. 3 is a schematic view of a culture device equipped with a cell state observation device and a stirring control device of the present invention.

【符号の説明】[Explanation of symbols]

1:培養槽、2:攪拌用ローター、3:回転軸、4:散
気管、5:マグネットカップリング、6:空気/培養用
ガス、7:センサー挿入口、8:回転軸タービン羽根、
9:外枠攪拌羽根、10:回転軸スクリュー羽根、1
1:培養液、12:試料採取配管、13:沈降用セル、
14:吸光度計、15:データ送信ケーブル、16:コ
ンピュータ、17:信号ケーブル、18:攪拌モータ
ー、19:電磁弁、20:ポンプ、
1: culture tank, 2: stirring rotor, 3: rotating shaft, 4: air diffuser, 5: magnet coupling, 6: air / culture gas, 7: sensor insertion port, 8: rotating shaft turbine blade,
9: Outer frame stirring blade, 10: Rotating shaft screw blade, 1
1: culture solution, 12: sampling pipe, 13: sedimentation cell,
14: Absorbance meter, 15: Data transmission cable, 16: Computer, 17: Signal cable, 18: Stirring motor, 19: Solenoid valve, 20: Pump,

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 動植物細胞及び/又は微生物細胞を培養
する培養装置において、該培養装置内に流速を任意に変
動できると共に流れの方向を逆転させることが可能な構
造の機械的攪拌手段を備えていることを特徴とする細胞
培養装置。
1. A culturing apparatus for culturing animal and plant cells and / or microbial cells, comprising a mechanical stirring means having a structure capable of arbitrarily changing the flow velocity and reversing the flow direction in the culturing apparatus. A cell culture device characterized in that
【請求項2】 前記機械的攪拌手段が、かご型ローター
であり、該ローターの回転軸に取付けられたスクリュー
羽根と周辺部の羽根が逆方向の流れを作る構造としたこ
とを特徴とする請求項1に記載の細胞培養装置。
2. The mechanical stirring means is a squirrel-cage rotor, and the structure is such that the screw blades attached to the rotary shaft of the rotor and the peripheral blades make a flow in the opposite direction. Item 2. The cell culture device according to item 1.
【請求項3】 前記培養装置は、機械的攪拌手段の流速
及び/又は流れの方向を制御するための培養槽内の細胞
の状態を観察する手段とそれに基づいて制御する制御系
を備えていることを特徴とする請求項1又は2記載の細
胞培養装置。
3. The culture device comprises means for observing the state of cells in the culture tank for controlling the flow velocity and / or flow direction of the mechanical stirring means, and a control system for controlling based on the means. The cell culture device according to claim 1, wherein the cell culture device is a cell culture device.
【請求項4】 前記機械的攪拌手段は、攪拌を停止した
状態を一定時間間隔で繰り返すことが可能な構造となっ
ていることを特徴とする請求項1、2又は3に記載の細
胞培養装置。
4. The cell culture device according to claim 1, 2 or 3, wherein the mechanical stirring means has a structure capable of repeating a state in which stirring is stopped at regular time intervals. .
【請求項5】 前記培養槽内の細胞の状態の観察手段
は、培養槽内の細胞量をオンライン計測する手段により
行うことを特徴とする請求項3に記載の細胞培養装置。
5. The cell culture device according to claim 3, wherein the means for observing the state of the cells in the culture tank is performed by means for measuring the amount of cells in the culture tank online.
【請求項6】 前記培養槽内の細胞の状態の観察手段
は、培養槽内の細胞の破損状態をオンライン計測する手
段により行うことを特徴とする請求項3に記載の細胞培
養装置。
6. The cell culture device according to claim 3, wherein the means for observing the state of the cells in the culture tank is a means for online measuring the state of damage of the cells in the culture tank.
JP24852193A 1993-09-10 1993-09-10 Cell culture apparatus Pending JPH0775550A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24852193A JPH0775550A (en) 1993-09-10 1993-09-10 Cell culture apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24852193A JPH0775550A (en) 1993-09-10 1993-09-10 Cell culture apparatus

Publications (1)

Publication Number Publication Date
JPH0775550A true JPH0775550A (en) 1995-03-20

Family

ID=17179427

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24852193A Pending JPH0775550A (en) 1993-09-10 1993-09-10 Cell culture apparatus

Country Status (1)

Country Link
JP (1) JPH0775550A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100370049B1 (en) * 2001-02-22 2003-02-05 백기엽 the medium animate of air floating drum
JP2009000013A (en) * 2007-06-19 2009-01-08 Nitto Denko Corp Method for culturing plant cell mass
JP2014161266A (en) * 2013-02-25 2014-09-08 Dainippon Printing Co Ltd Culture bag
JP2018050550A (en) * 2016-09-29 2018-04-05 佐竹化学機械工業株式会社 Spinner culture device
WO2019131626A1 (en) * 2017-12-28 2019-07-04 オリンパス株式会社 Cell culture control method, cell culture control device, cell culturing device and cell culturing system
US11365382B2 (en) 2016-03-14 2022-06-21 Omnibrx Biotechnologies Private Limited Bioreactor system and method thereof

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100370049B1 (en) * 2001-02-22 2003-02-05 백기엽 the medium animate of air floating drum
JP2009000013A (en) * 2007-06-19 2009-01-08 Nitto Denko Corp Method for culturing plant cell mass
JP2014161266A (en) * 2013-02-25 2014-09-08 Dainippon Printing Co Ltd Culture bag
US11365382B2 (en) 2016-03-14 2022-06-21 Omnibrx Biotechnologies Private Limited Bioreactor system and method thereof
JP2018050550A (en) * 2016-09-29 2018-04-05 佐竹化学機械工業株式会社 Spinner culture device
WO2019131626A1 (en) * 2017-12-28 2019-07-04 オリンパス株式会社 Cell culture control method, cell culture control device, cell culturing device and cell culturing system

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