JPH0534944B2 - - Google Patents
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- JPH0534944B2 JPH0534944B2 JP60180983A JP18098385A JPH0534944B2 JP H0534944 B2 JPH0534944 B2 JP H0534944B2 JP 60180983 A JP60180983 A JP 60180983A JP 18098385 A JP18098385 A JP 18098385A JP H0534944 B2 JPH0534944 B2 JP H0534944B2
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- 239000007788 liquid Substances 0.000 claims abstract description 103
- 239000002245 particle Substances 0.000 claims description 30
- 230000001419 dependent effect Effects 0.000 claims description 15
- 238000012136 culture method Methods 0.000 claims description 2
- 230000002062 proliferating effect Effects 0.000 claims 2
- 239000006185 dispersion Substances 0.000 abstract description 17
- 230000005484 gravity Effects 0.000 abstract description 12
- 239000002609 medium Substances 0.000 description 99
- 210000004027 cell Anatomy 0.000 description 90
- 241000196324 Embryophyta Species 0.000 description 50
- 238000000034 method Methods 0.000 description 17
- 238000012258 culturing Methods 0.000 description 10
- 210000004748 cultured cell Anatomy 0.000 description 7
- 238000007599 discharging Methods 0.000 description 5
- 238000010008 shearing Methods 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 239000013543 active substance Substances 0.000 description 4
- 239000000758 substrate Substances 0.000 description 4
- 206010020649 Hyperkeratosis Diseases 0.000 description 3
- 241001071917 Lithospermum Species 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 238000004113 cell culture Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000001963 growth medium Substances 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 108091003079 Bovine Serum Albumin Proteins 0.000 description 1
- 241000699802 Cricetulus griseus Species 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000010261 cell growth Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000012091 fetal bovine serum Substances 0.000 description 1
- 210000002950 fibroblast Anatomy 0.000 description 1
- 239000012737 fresh medium Substances 0.000 description 1
- 238000009630 liquid culture Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 210000004072 lung Anatomy 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 230000008635 plant growth Effects 0.000 description 1
- 238000004161 plant tissue culture Methods 0.000 description 1
- 230000011514 reflex Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/50—Means for positioning or orientating the apparatus
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS 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
- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/10—Rotating vessel
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- Health & Medical Sciences (AREA)
- Wood Science & Technology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Organic Chemistry (AREA)
- Chemical & Material Sciences (AREA)
- Zoology (AREA)
- Biomedical Technology (AREA)
- Sustainable Development (AREA)
- Microbiology (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Biotechnology (AREA)
- Clinical Laboratory Science (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Abstract
Description
〔産業上の利用分野〕
本発明は細胞もしくは植物組織の培養方法およ
び装置に関するものであり、さらに詳しくは生理
活性物質等を製造するために好適な細胞もしくは
植物組織の培養方法おおよび装置に関するもので
ある。
〔従来の技術〕
一般に生理活性物質は、細胞もしくは植物組織
にある種の活性を与えて当該細胞もしくは植物組
織に特定の生理反応を生じさせるものであり、人
工的に合成され得るものもあるが、通常は生体の
細胞もしくは植物組織の生存維持による産生に待
たなければならない。
従来における生理活性物質の製造方法として
は、目的とする生理活性物質を産生する細胞もし
くは植物組織を生存維持させるために培養せしめ
る方法が知られている。
一般に細胞もしくは植物組織の培養において
は、培養対象が浮遊増殖性細胞もしくは植物組
織、すなわち液体培地中に細胞もしくは植物組織
自体が浮遊した状態で増殖することが可能である
場合には、その栄養源である液体培地中に浮遊さ
せることにより培地と接触させることが必要であ
り、また培養対象が接着依存性細胞、すなわち液
体培地中において生育および増殖するために基質
に対する接着が必須の細胞である場合には、適当
な基質の表面に当該細胞を接着させたうえで液体
培地と接触させることが必要である。そして接着
依存性細胞を接着させる基質としては、大きな接
着面積を容易に得ることができることから、最近
においては小径の担体粒子が用いられるようにな
つてきている。
〔発明が解決しようとする問題点〕
しかして目的とする細胞の培養を高い効率で行
うためには、培養対象細胞を常に新しい培地と接
触させることが肝要であり、そのためには浮遊増
殖性細胞、または接着依存性細胞が接着した担体
粒子(以下これらを合わせて単に「細胞」ともい
う。)を液体培地中に高い分散度で分散せしめる
ことが必要である。
また接着依存性細胞を基質である担体粒子に接
着させる際にも、当該細胞が混合された液体培地
中において担体粒子を高い分散度で分散せしめる
ことができれば、当該細胞の接着に利用すること
ができる担体粒子の表面の有効利用面積が大きく
なり、したがつて高い接着率で細胞を担体粒子に
接着することが可能となり、培養効率を高めるう
えで極めて有利である。
従来において、培養対象細胞を常に新しい液体
培地に接触させるための方法としては、液体培地
中に培養対象細胞を混合した系を回転翼によつて
撹拌する方法が一般的であるが、しかしながらこ
の方法は液体培地と細胞との混合系に剪断力を加
えて当該細胞を分散する方法であるため、回転翼
との衝突によりあるいは大きな剪断力の作用によ
り培養中の細胞が損傷されることを回避すること
ができず、結局培養効率が低く、また細胞の種類
によつてはこの方法を用いることができない場合
もあるという問題点を有する。
また上記の如き方法を実施するために、大量培
養を目的として大容量の細胞培養装置を構成する
場合には、撹拌のために大型の撹拌機が必要とな
り、したがつて必然的に剪断力も大きくなり、そ
のため培養効率がさらに低下するようになるとい
う問題点点をも有する。
そして培養対象細胞を常に新しい液体培地と接
触させるためには、培養期間中において培養容器
内の液体培地を適宜新しいものと交換することが
必要であり、したがつて液体培地の交換を有利に
行うことができる状態に細胞を液体培地中に分散
させることが好ましい。
上記状況は植物組織の培養においても同様であ
る。
このような問題点を解消するために種々の方策
が研究されてはいるが、かかる問題点を本質的に
解決する細胞もしくは植物組織の培養方法および
装置は未だ開発されていないのが現状である。
本発明は、以上の如き事情に基づき鋭意研究を
重ねた結果完成されたものであつて、その目的と
するところは、液体培地と培養対象細胞もしくは
植物組織との混合系に本質的に剪断力を与えるこ
となく、液体培地中に細胞もしくは植物組織を良
好な分散度でしかも液体培地の交換に有利な状態
で分散させることができ、高い効率で細胞もしく
は植物組織の培養を行なうことのできる方法およ
び装置を提供することにある。
〔問題点を解決するための手段〕
本発明方法の特徴とするところは、細胞もしく
は植物組織との混合系を実質的に充満するように
充填した培養容器を水平面に対し5〜55゜の範囲
の角度に傾斜させた軸の周りに自転するように回
転させて当該混合系を前記培養容器と共に定常的
に回転させ、これにより当該混合系内において前
記被分散粒子、浮遊増殖性細胞もしくは植物組織
を、前記液体培地に、好ましくは上部と下部にお
ける分散濃度に差が生じた状態で分散せしめる工
程を有する点にある。
また本発明装置の特徴とするところは、水平面
に対し5〜55゜の範囲の角度に傾斜するよう軸支
された回転軸を有する培養容器と、この培養容器
を前記回転軸の周りに自転するよう回転せしめる
駆動機構とを有してなり、前記駆動機構は、前記
培養容器内に実質的に充満するように充填された
液体培地と細胞もしくは植物組織との混合系を前
記培養容器と共に定常的に回転せしめる機能を有
するものである。
かかる技術手段によれば、培養容器内におい
て、細胞もしくは植物組織を実質上剪断力を与え
ずに高い分散度で分散させることができ、例えば
液体培地より比重の高い細胞もしくは植物組織を
用いることによつて培養容器内の液体培地の上部
と下部における分散濃度に差が生じた状態で分散
せしめることができるので、この分散濃度の差を
利用して古くなつた液体培地を新しい液体培地と
有利に交換することが可能となる。すなわち培養
容器には、通常、細胞もしくは植物組織は透過せ
ずに液体培地のみを透過するフイルター部材が設
けられ、このフイルター部材を介して液体培地の
交換を行うようにするが、上記の技術手段によれ
ば、液体培地における細胞もしくは植物組織の分
散濃度が低い部分から培地の交換を行うことがで
きるので、フイルター部材の目詰まりを伴うこと
なく効率的に液体培地の交換を行うことが可能と
なり、結局高い効率で細胞もしくは植物組織の培
養を達成することができる。
以下本発明について具体的に説明する。
本発明においては、第1図に示すように、例え
ば円筒状の密閉された培養容器1内に、細胞もし
くは植物組織2を混合した液体培地3を、培養容
器1の内部空間に実質的に充満されるように充填
し、培養容器1の軸Xを水平面(H)に対し5〜55゜、
好ましくは5〜45゜、さらに好ましくは20〜45゜の
範囲の角度(α)に傾斜させた状態で、この軸X
の周りに培養容器1を一定の回転速度で自転せし
める。このとき角度(α)が5゜より小さいと、例
えば液体培地より比重の高い細胞もしくは植物組
織を用いても、培養容器内における細胞もしくは
植物組織の分散濃度に差が生じないので、液体培
地のどの部分から液体培地を交換してもフイルタ
ー部材の目詰まりを伴い、効率的に液体培地の交
換を行うことが困難な場合が生じ、角度(α)が
55゜より大きいと液体培地と比重の異なる細胞も
しくは植物組織がほとんど液体培地中に分散せず
効率的な培養を行うことが難しくなる。
このように培養容器1を自転させることによつ
て、自転開始直後の初期期間を経過した後は、培
養容器1内の液体培地3と細胞もしくは植物組織
2との混合系が液体培地3の粘性により培養容器
1といわば一体的に機械的な流れのない状態で軸
Xの周りに定常的に回転するようになり、したが
つて細胞もしくは植物組織2は培養容器1内の液
体培地3に対する相対的位置をほとんど変えるこ
となく培養容器1外に対する存在位置を変えるこ
ととなり、このため培養容器1内の細胞もしくは
植物組織2には順次異なる方向から重力が作用す
る状態となつてこれにより細胞もしくは植物組織
2が液体培地3中に良好な分散度で分散するよう
になる。
細胞もしくは植物組織の培養においては、通常
液体培地の交換が必要とされる。本発明において
も長期間にわたる培養においては、液体培地の交
換が必要とされる。液体培地の交換方法として
は、例えば培養容器の回転を止めて液体培地の一
部または全部を交換する方法、培養容器に液体培
地の供給管および排出管を設置し、培養期間中に
連続的に新しい液体培地を供給すると共に古い液
体培地を排出する方法などを挙げることができ
る。このようにして新しい液体培地を供給するこ
とによつて、通常、数日以上の期間を必要とする
培養を良好に行うことができる。新しい液体培地
の供給は、上記のように供給管を通じて培養期間
中常時行うようにすれば、単位時間当りの供給量
および排出量は僅かでよいから、培養容器内の液
体培地に層流、乱流などの機械的な流れを実質上
生ぜしめない状態とすることが可能であり、した
がつて細胞もしくは植物組織の所期の分散状態を
妨げることなく液体培地の交換を行うことができ
る。培養効率を高めるためにも、液体培地の供給
は供給管を通じて常時行うことが好ましい。
そして培養容器1の軸Xを水平面に対して上記
の如き範囲の角度に傾斜させた状態で培養容器1
を自転させることにより、重力もしくは浮力の作
用により培養容器1内の液体培地3の上部と下部
における細胞もしくは植物組織2の分散濃度に差
が生ずるようになり、例えば細胞もしくは植物組
織2の比重が液体培地3の比重より高い場合には
液体培地3の上部における分散濃度は低く下部に
おける分散濃度は高い状態に分散させることがで
きる。したがつて培養容器1内の液体培地3を必
要に応じて新しい液体培地と交換するときには、
分散濃度の低い部分から古くなつた液体培地を排
出させ分散濃度の高い部分に新しい液体培地を供
給するようにすることにより、細胞もしくは植物
組織を効率的に新しい液体培地と接触させること
ができると共に、古くなつた液体培地を排出する
際には細胞もしくは植物組織2によるフイルター
部材の目詰まりの発生を抑制することができるの
で、安定にまた培養期間中において連続的に液体
培地の交換を行うことが可能となり、結局長期間
に亘り高い効率で細胞もしくは植物組織の培養を
行うことが可能となる。
本発明において、培養容器内に液体培地と細胞
もしくは植物組織とを充填するためには特殊な方
法を必要とするものではなく、例えば事前に混合
された液体培地と細胞もしくは植物組織との混合
系を充填すればよい。しかし接着依存性細胞を培
養する場合においては、事前に接着依存性細胞を
接着した担体粒子を培養容器内に充填するより
も、既述の如き培養容器内に液体培地と担体粒子
と接着依存性細胞との混合系を充填し、本発明方
法と同様にして培養容器を自転させ、これにより
液体培地中に担体粒子および接着依存性細胞を剪
断力を与えることなく分散させて、細胞を各担体
粒子の表面に平均にかつ効率的に接着させること
が望ましい。この場合には前記接着工程に引き続
き本発明を実施することができる。
また本発明により接着依存性細胞を培養する場
合において、供給管を通じて常時培養容器内に新
しい液体培地を供給し排出管を通じて古い液体培
地を常時排出する方法を適用するときには、供給
する新しい液体培地と共に新しい担体粒子および
接着依存性細胞を培養容器内に供給し、培養容器
から排出する古い液体培地と共に増殖した接着依
存性細胞がその表面に接着している担体粒子の一
部を抜出す方法を用いることにより、液体培地の
交換、担体粒子への接着依存性細胞の接着、培養
および増殖した接着依存性細胞の抜出しを連続的
に行うことができる。
本発明の適用においては、培養されるべき細胞
は何ら制限されるものではなく、例えば第1表に
示す細胞を例示することができる。
[Industrial Application Field] The present invention relates to a method and apparatus for culturing cells or plant tissues, and more particularly to a method and apparatus for culturing cells or plant tissues suitable for producing physiologically active substances, etc. It is. [Prior Art] In general, physiologically active substances are substances that impart a certain kind of activity to cells or plant tissues and cause them to produce specific physiological reactions, and some of them can be artificially synthesized. , which usually has to be produced by maintaining the survival of living cells or plant tissues. As a conventional method for producing a physiologically active substance, a method is known in which cells or plant tissues that produce the desired physiologically active substance are cultured to keep them alive. In general, when culturing cells or plant tissues, if the culture target is a suspension-propagating cell or plant tissue, that is, when the cells or plant tissue itself can grow in a suspended state in a liquid medium, the nutrient source is It is necessary to contact the culture medium by suspending it in a liquid medium, and when the culture target is an adhesion-dependent cell, that is, a cell that requires adhesion to a substrate in order to grow and proliferate in the liquid medium. For this purpose, it is necessary to attach the cells to the surface of a suitable substrate and then contact the cells with a liquid medium. Recently, small-diameter carrier particles have come to be used as substrates for adhesion-dependent cells because they can easily provide a large adhesion area. [Problems to be solved by the invention] However, in order to culture the target cells with high efficiency, it is important to constantly contact the cells to be cultured with a fresh medium. , or carrier particles to which adhesion-dependent cells have adhered (hereinafter also simply referred to as "cells") are required to be dispersed with a high degree of dispersion in a liquid medium. Furthermore, when adhesion-dependent cells are attached to carrier particles as a substrate, if the carrier particles can be dispersed with a high degree of dispersion in a liquid medium in which the cells are mixed, they can be used for adhesion of the cells. The effective surface area of the resulting carrier particles becomes larger, and therefore cells can be attached to the carrier particles with a high adhesion rate, which is extremely advantageous in increasing culture efficiency. Conventionally, a common method for keeping cells to be cultured in constant contact with a fresh liquid medium has been to use a rotary blade to stir a system in which cells to be cultured are mixed in a liquid medium; however, this method Since this method applies shear force to a mixed system of liquid culture medium and cells to disperse the cells, it avoids damage to the cells being cultured due to collisions with rotary blades or the action of large shear forces. However, there are problems in that the culture efficiency is low, and this method may not be applicable depending on the type of cells. Furthermore, when constructing a large-capacity cell culture device for the purpose of mass culture in order to carry out the method described above, a large-sized stirrer is required for stirring, which inevitably results in a large shearing force. Therefore, there is also the problem that the culture efficiency further decreases. In order to keep the cells to be cultured constantly in contact with a new liquid medium, it is necessary to replace the liquid medium in the culture container with a new one as appropriate during the culture period.Therefore, it is advantageous to replace the liquid medium. Preferably, the cells are dispersed in a liquid medium in a state where they can be dispersed. The above situation is the same in culturing plant tissues. Although various measures have been researched to solve these problems, the current situation is that no cell or plant tissue culture method or device that essentially solves these problems has been developed. . The present invention was completed as a result of intensive research based on the above circumstances, and its purpose is to apply shearing force to the mixed system of a liquid medium and cells or plant tissues to be cultured. A method capable of culturing cells or plant tissues with high efficiency by dispersing cells or plant tissues in a liquid medium with a good degree of dispersion and in a state that is advantageous for exchange of the liquid medium without providing and equipment. [Means for Solving the Problems] The method of the present invention is characterized in that the culture vessel filled with the mixed system with cells or plant tissues is placed at an angle of 5 to 55 degrees with respect to the horizontal plane. The mixed system is constantly rotated together with the culture vessel by rotating around an axis inclined at an angle of is dispersed in the liquid medium, preferably with a difference in dispersion concentration in the upper and lower parts. The apparatus of the present invention is also characterized by a culture container having a rotating shaft supported so as to be inclined at an angle of 5 to 55 degrees with respect to a horizontal plane, and a culture container that rotates around the rotating shaft. and a drive mechanism that rotates a mixed system of cells or plant tissue and a liquid medium filled so as to substantially fill the culture container together with the culture container. It has the function of rotating the According to such technical means, cells or plant tissues can be dispersed with a high degree of dispersion in a culture container without applying substantially shearing force. For example, cells or plant tissues having a higher specific gravity than a liquid medium can be used. Therefore, it is possible to disperse the liquid medium in the culture container with a difference in dispersion concentration between the upper and lower parts, so this difference in dispersion concentration can be used to advantageously replace an old liquid medium with a new liquid medium. It becomes possible to exchange. That is, the culture container is usually provided with a filter member that allows only the liquid medium to pass through without passing through cells or plant tissues, and the liquid medium is exchanged through this filter member, but the above technical means According to , it is possible to exchange the medium from the part of the liquid medium where the dispersed concentration of cells or plant tissue is low, making it possible to exchange the liquid medium efficiently without clogging the filter member. As a result, culturing of cells or plant tissues can be achieved with high efficiency. The present invention will be specifically explained below. In the present invention, as shown in FIG. 1, for example, a cylindrical sealed culture container 1 is filled with a liquid medium 3 in which cells or plant tissues 2 are mixed, and the inner space of the culture container 1 is substantially filled. Fill the culture container so that the axis
This axis
The culture container 1 is rotated at a constant rotational speed around the . At this time, if the angle (α) is smaller than 5°, for example, even if cells or plant tissues with higher specific gravity than the liquid medium are used, there will be no difference in the dispersed concentration of cells or plant tissues in the culture container. No matter where you replace the liquid medium, the filter member will become clogged, making it difficult to exchange the liquid medium efficiently.
If the angle is larger than 55°, cells or plant tissues having a different specific gravity from the liquid medium will hardly be dispersed in the liquid medium, making it difficult to perform efficient culture. By rotating the culture container 1 in this way, after an initial period immediately after the start of rotation, the mixed system of the liquid medium 3 and the cells or plant tissues 2 in the culture container 1 becomes viscous. As a result, the culture container 1 rotates steadily around the axis X without any mechanical flow, so that the cells or plant tissues 2 are rotated relative to the liquid medium 3 in the culture container 1. As a result, the cell or plant tissue 2 in the culture container 1 is subjected to gravity from different directions sequentially, and as a result, the cell or plant tissue 2 in the culture container 1 is subjected to gravity from different directions. The tissue 2 becomes dispersed in the liquid medium 3 with a good degree of dispersion. In culturing cells or plant tissues, replacement of the liquid medium is usually required. In the present invention, the liquid medium also needs to be replaced during long-term culture. Methods for replacing the liquid medium include, for example, stopping the rotation of the culture container and replacing part or all of the liquid medium, or installing a supply pipe and a discharge pipe for the liquid medium in the culture container and continuously replacing it during the culture period. Examples include a method of supplying a new liquid medium and discharging the old liquid medium. By supplying a new liquid medium in this manner, culture, which normally requires a period of several days or more, can be carried out satisfactorily. If new liquid medium is constantly supplied through the supply pipe during the culture period as described above, the amount of supply and discharge per unit time will be small, so the liquid medium in the culture container will have a laminar flow and turbulence. It is possible to create a state in which substantially no mechanical flow such as a flow occurs, and therefore the liquid medium can be exchanged without disturbing the desired dispersion state of cells or plant tissues. In order to improve culture efficiency, it is preferable to constantly supply the liquid medium through a supply pipe. Then, with the axis X of the culture container 1 inclined at an angle within the above range with respect to the horizontal plane, the culture container
By rotating the cell or plant tissue 2, a difference will occur in the dispersed concentration of the cells or plant tissue 2 in the upper and lower parts of the liquid medium 3 in the culture container 1 due to the action of gravity or buoyancy. When the specific gravity is higher than that of the liquid medium 3, the dispersion concentration in the upper part of the liquid medium 3 can be low and the dispersion concentration in the lower part can be high. Therefore, when replacing the liquid medium 3 in the culture container 1 with a new liquid medium as necessary,
By discharging the old liquid medium from the area where the dispersion concentration is low and supplying new liquid medium to the area where the dispersion concentration is high, cells or plant tissues can be efficiently brought into contact with the new liquid medium. When discharging an old liquid medium, clogging of the filter member by cells or plant tissue 2 can be suppressed, so the liquid medium can be replaced stably and continuously during the culture period. This makes it possible to culture cells or plant tissues with high efficiency over a long period of time. In the present invention, no special method is required to fill a culture container with a liquid medium and cells or plant tissues; for example, a mixed system of a liquid medium and cells or plant tissues that have been mixed in advance. All you have to do is fill it up. However, when culturing adhesion-dependent cells, rather than filling a culture container with carrier particles to which adhesion-dependent cells have been attached in advance, it is preferable to fill a culture container with a liquid medium, carrier particles, and adhesion-dependent cells as described above. Fill the mixed system with cells and rotate the culture container in the same manner as in the method of the present invention. As a result, the carrier particles and adhesion-dependent cells are dispersed in the liquid medium without applying shearing force, and the cells are transferred to each carrier. It is desirable to have an even and efficient adhesion to the surface of the particles. In this case, the present invention can be carried out subsequent to the adhesion step. Furthermore, when culturing adhesion-dependent cells according to the present invention, if a method is applied in which a new liquid medium is constantly supplied into the culture container through a supply pipe and an old liquid medium is constantly discharged through a discharge pipe, the new liquid medium is A method is used in which new carrier particles and adhesion-dependent cells are supplied into a culture vessel, and the adhesion-dependent cells that have grown together with the old liquid medium that is discharged from the culture vessel extract part of the carrier particles that have adhered to the surface. By doing so, it is possible to continuously exchange the liquid medium, adhere the adhesion-dependent cells to the carrier particles, and extract the cultured and proliferated adhesion-dependent cells. In the application of the present invention, the cells to be cultured are not limited in any way, and for example, the cells shown in Table 1 can be exemplified.
【表】【table】
以下本発明に基づいて実際に行つた培養実施例
について説明する。
実施例 1
培養細胞:チヤイニーズハムスター肺繊維芽細胞
由来の「V−79」
液体培地:酸素および炭酸ガスを溶存する
10V/V%牛胎児血清を含む「Eagle−
MEM」
(粘度:0.01poise、比重:1.01)
担体粒子:「Cytodex 」(Pharmacia社製)
(粒径:180μm、比重:1.03)
容量300mlの筒状培養容器中に乾燥重量で900mg
(約3×106個)の上記担体粒子を入れると共に上
記液体培地を満し、これに6×106個の上記培養
細胞を播種し、空気が入らないように密閉した
後、培養容器の回転軸の角度を水平面に対して
45゜とした状態で、温度37℃の環境下において4
時間に亘り回転数15r.p.m.で培養容器を回転させ
て細胞の担体粒子への接着を行つた。
その結果、細胞が接着しなかつた担体粒子の割
合は約5%であり、細胞接着のあつた担体粒子の
個々における細胞数は2〜4個で平均2.5個であ
り、全担体粒子上の細胞数は4.8×106個であつ
た。
引き続き、培養容器を上記と同様の条件下で72
時間に亘り回転させて細胞の培養を行つた。この
間において24時間毎に培養容器の回転を止めて液
体培地を全量交換した。この結果、全担体粒子上
の細胞は7.2×107個に増殖していた。
実施例 2
第2図に示した構成の内容積が1の培養容器
を有する培養装置を用い、実施例1におけると同
様の培養細胞、液体培地および担体粒子を用いて
細胞の培養を行なつた。すなわち液体培地1に
対して乾燥重量で3g(約1.0×107個)の担体粒
子を用い、液体培地1ml当り1×104個の培養細
胞を播種し、培養容器内に空気が入らないように
してこれら培養細胞、液体培地および担体粒子の
混合系を充填し、培養容器の回転軸の角度を水平
面に対して45゜とした状態で、温度37℃の環境下
において144時間に亘り回転数12r.p.m.で培養容
器を回転せしめながら、培養容器内に新しい液体
培地を80ml/hrの割合で供給し、また同量の古い
液体培地を排出させた。その結果、担体粒子上の
細胞数は液体培地1ml当り平均2.5×106個であつ
た。また液体培地の交換においては、培養容器に
設けられているフイルター部材に目詰まりを起こ
すことなく、最後まで安定して液体培地の交換を
行うことができた。
比較例 1
内容積2のスピンナービンを用い、実施例1
におけると同様の培養細胞、液体培地および担体
粒子を用いて細胞の培養を行なつた。すなわちス
ピンナービンに液体培地1に対して乾燥重量で
3gの担体粒子を加え、ついで液体培地1ml当り
1×104個の培養細胞を播種し、温度37℃の環境
下において回転子の回転数を30r.p.m.で回転せし
めながら144時間に亘り培養を行なつた。この間
5%の炭酸ガスを含む空気をスピンナービンの上
部に供給し続け、液体培地が常に該空気に接触す
るようにした。その結果、担体粒子上の細胞数
は、液体培地1ml当り平均5.1×105個であつた。
実施例 3
内容積100mlの円筒状培養容器にリンスマイヤ
−スクーグの液体培地(比重1.0)を満し、これ
にさらに乾燥重量で0.5gのムラサキ
(Lithospermum erythrorhizon Sieb.et,Zucc)
の湿潤カルスを入れて密封した後、培養容器の回
転軸の角度を水平面に対して30゜とした状態で、
温度25℃の環境下において14日間に亘り回転数
15r.p.m.で培養容器を回転せしめながら植物組織
の培養を行つた。
この間において、24時間毎に培養容器の回転を
止めて液体培地を全量交換した。
かくして得られた植物組織を乾燥してその重量
を測定したところ、1.3gであつた。
実施例 4
第2図に示した構成の内容積が120mlの培養容
器を有する培養装置を用い、実施例3におけると
同様の植物組織および液体培地を用いて植物組織
の培養を行つた。
すなわち液体培地120mlに対して乾燥重量で0.6
gのムラサキ(Lithospermum erythrorhizon
Sieb.et,Zucc)の湿潤カルスを入れて密封した
後、培養容器の回転軸の角度を水平面に対して
30゜とした状態で、温度25℃の環境下において14
日間に亘り回転数15r.p.m.で培養容器を回転さ
せ、培養容器内に新しい液体培地を120ml/24時
間の割合で供給すると共に同様の割合で古くなつ
た液体培地を排出させながら、植物組織の培養を
行つた。
かくして得られた植物組織を乾燥してその重量
を測定したところ、1.7gであつた。
比較例 2
内容積200mlのスピンナービンを用い、実施例
3におけると同様の液体培地100mlおよびカルス
0.5gを用い、回転翼の回転数15r.p.m.として実施
例3と同様にして植物組織の培養を行つた。その
結果得られた植物組織の乾燥重量は1.0gであつ
た。
〔発明の効果〕
以上詳細に説明したように本発明によれば、培
養容器内に液体培地と細胞もしくは植物組織との
混合系を実質的に充満するよう充填した状態で培
養容器を回転させるので、細胞もしくは植物組織
を実質上剪断力を与えずに良好な分散度で分散さ
せることができ、しかも培養容器を水平面に対し
5〜55゜の範囲の角度に傾斜させた軸の周りに自
転するように回転させるので、例えば液体培地よ
り比重の高い細胞もしくは植物組織を用いること
によつて培養容器内の液体培地の上部と下部にお
ける細胞もしくは植物組織の分散濃度に差が生じ
た状態で分散させることができ、したがつて分散
濃度の低い部分から古くなつた液体培地を排出さ
せることにより培養容器に設けられるフイルター
部材の目詰まりを伴うことなく安定に液体培地の
排出を行うことができると共に、分散濃度の高い
部分に新しい液体培地を供給するようにすること
により多数の細胞もしくは植物組織を効率的に新
しい液体培地と接触させることができ、結局長期
間に亘り安定して細胞もしくは植物組織の培養を
行うことができて高い効率で培養を達成すること
ができる培養方法および装置を提供することがで
きる。
Examples of culturing actually carried out based on the present invention will be described below. Example 1 Cultured cells: "V-79" derived from Chinese hamster lung fibroblasts Liquid medium: "Eagle-" containing 10V/V% fetal bovine serum dissolving oxygen and carbon dioxide gas
MEM” (viscosity: 0.01 poise, specific gravity: 1.01) Carrier particles: “Cytodex” (manufactured by Pharmacia) (particle size: 180 μm, specific gravity: 1.03) 900 mg dry weight in a cylindrical culture vessel with a capacity of 300 ml
Add (approximately 3 x 10 6 pieces) of the above carrier particles and fill the liquid medium, seed 6 x 10 6 pieces of the above cultured cells, and seal it to prevent air from entering. The angle of the rotation axis relative to the horizontal plane
45° in an environment with a temperature of 37°C.
The culture vessel was rotated at a rotational speed of 15 rpm for a period of time to allow the cells to adhere to the carrier particles. As a result, the proportion of carrier particles to which cells did not adhere was approximately 5%, and the number of cells in each carrier particle to which cells did adhere was 2 to 4, with an average of 2.5, and the number of cells on all carrier particles was 2.5. The number was 4.8× 106 . Continue to incubate the culture vessel under the same conditions as above.
Cells were cultured by rotating for hours. During this period, the rotation of the culture container was stopped and the entire liquid medium was replaced every 24 hours. As a result, the cells on all carrier particles had grown to 7.2×10 7 cells. Example 2 Cells were cultured using the same cultured cells, liquid medium, and carrier particles as in Example 1 using a culture apparatus having a culture container with an internal volume of 1 as shown in FIG. . That is, using 3 g (approximately 1.0 x 10 7 cells) of carrier particles in dry weight per 1 liquid medium, seeding 1 x 10 4 cultured cells per 1 ml of liquid medium, and making sure that no air enters the culture container. Filled with a mixed system of cultured cells, liquid medium, and carrier particles, the culture vessel was rotated for 144 hours at a temperature of 37°C with the rotation axis of the culture vessel set at an angle of 45° with respect to the horizontal plane. While rotating the culture container at 12 rpm, a new liquid medium was supplied into the culture container at a rate of 80 ml/hr, and the same amount of old liquid medium was discharged. As a result, the average number of cells on the carrier particles was 2.5×10 6 per ml of liquid medium. Furthermore, during the exchange of the liquid medium, the liquid medium could be exchanged stably to the end without clogging the filter member provided in the culture container. Comparative Example 1 Using a spinner bin with an internal volume of 2, Example 1
Cells were cultured using the same cultured cells, liquid medium, and carrier particles as in . That is, 3 g of dry weight carrier particles were added to 1 ml of liquid medium in a spinner bottle, and then 1 x 10 4 cultured cells were seeded per 1 ml of liquid medium, and the rotation speed of the rotor was adjusted at a temperature of 37°C. Culture was carried out for 144 hours while rotating at 30 rpm. During this time, air containing 5% carbon dioxide gas was continuously supplied to the top of the spinner bottle so that the liquid medium was constantly in contact with the air. As a result, the average number of cells on the carrier particles was 5.1×10 5 cells per ml of liquid medium. Example 3 A cylindrical culture container with an internal volume of 100 ml was filled with Linsmeyer-Skoog's liquid medium (specific gravity 1.0), and 0.5 g of dry weight Lithospermum erythrorhizon Sieb.et, Zucc was added to this.
After putting in the wet callus and sealing it, with the rotation axis of the culture container set at an angle of 30° with respect to the horizontal plane,
Rotation speed over 14 days in an environment with a temperature of 25℃
Plant tissues were cultured while rotating the culture container at 15 rpm. During this period, the rotation of the culture container was stopped and the entire liquid medium was replaced every 24 hours. When the thus obtained plant tissue was dried and its weight was measured, it was 1.3 g. Example 4 Plant tissue was cultured using the same plant tissue and liquid medium as in Example 3 using a culture apparatus having a culture container with an internal volume of 120 ml as shown in FIG. i.e. 0.6 dry weight for 120ml of liquid medium
Lithospermum erythrorhizon
After placing wet callus (Sieb.et, Zucc) and sealing, adjust the angle of the rotation axis of the culture container with respect to the horizontal plane.
14 in an environment with a temperature of 25℃ at a temperature of 30℃.
The culture vessel was rotated at a rotation speed of 15 rpm for days, and while supplying new liquid medium into the culture vessel at a rate of 120 ml/24 hours and discharging the old liquid medium at the same rate, the plant tissue was grown. Culture was carried out. When the thus obtained plant tissue was dried and its weight was measured, it was 1.7 g. Comparative Example 2 Using a spinner bottle with an internal volume of 200 ml, 100 ml of the same liquid medium as in Example 3 and callus were added.
Plant tissues were cultured in the same manner as in Example 3 using 0.5 g and using a rotating blade of 15 rpm. The dry weight of the resulting plant tissue was 1.0 g. [Effects of the Invention] As explained in detail above, according to the present invention, the culture container is rotated while the culture container is filled with a mixed system of a liquid medium and cells or plant tissues so as to be substantially filled. , cells or plant tissues can be dispersed with a good degree of dispersion without applying substantial shearing force, and the culture vessel is rotated around an axis tilted at an angle of 5 to 55 degrees with respect to the horizontal plane. For example, by using cells or plant tissues that have a higher specific gravity than the liquid medium, the cells or plant tissues can be dispersed with a difference in the dispersion concentration between the upper and lower parts of the liquid medium in the culture container. Therefore, by discharging the old liquid medium from the part where the dispersion concentration is low, it is possible to stably discharge the liquid medium without clogging the filter member provided in the culture container, and By supplying new liquid medium to areas with high dispersed concentration, a large number of cells or plant tissues can be brought into contact with the new liquid medium efficiently, resulting in stable growth of cells or plant tissues over a long period of time. It is possible to provide a culture method and apparatus that can perform culture and achieve culture with high efficiency.
第1図は本発明の一例についての説明用斜視
図、第2図は本発明に係る培養装置の一例を示す
説明用断面図、第3図は本発明に係る培養装置を
用いて培養を行う場合のシステムチヤートの一例
を示す説明図である。
1……培養容器、2……細胞もしくは植物組
織、3……液体培地、30……底板、31……容
器本体、32……押え機構、33……Oリング、
35……回転スリーブ、36……ドライベアリン
グ、37…スタンド、38……外套部材、40…
…メツシユ、41……内導管、42……外導管、
43……内導管の一端開口、44……外導管の一
端開口、50……連結シール部、51……供給
管、52……排出管、60……被動歯車、61…
…駆動歯車、70……液体培地タンク、71……
培養容器、72……排出タンク、73……モニタ
ー機構、74,77……PHセンサー、75,78
……DOセンサー、80……アルカリタンク、8
1……送気管、82……制御弁。
FIG. 1 is an explanatory perspective view of an example of the present invention, FIG. 2 is an explanatory sectional view of an example of a culture device according to the present invention, and FIG. 3 is a culture performed using the culture device according to the present invention. FIG. 2 is an explanatory diagram showing an example of a system chart for the case. 1... Culture container, 2... Cell or plant tissue, 3... Liquid medium, 30... Bottom plate, 31... Container body, 32... Holding mechanism, 33... O ring,
35... Rotating sleeve, 36... Dry bearing, 37... Stand, 38... Mantle member, 40...
...Meshyu, 41...Inner conduit, 42...Outer conduit,
43... One end opening of the inner conduit, 44... One end opening of the outer conduit, 50... Connecting seal portion, 51... Supply pipe, 52... Discharge pipe, 60... Driven gear, 61...
...Drive gear, 70...Liquid medium tank, 71...
Culture container, 72... Discharge tank, 73... Monitor mechanism, 74, 77... PH sensor, 75, 78
...DO sensor, 80 ...Alkaline tank, 8
1... Air pipe, 82... Control valve.
Claims (1)
分散粒子、浮遊増殖性細胞もしくは植物組織との
混合系を実質的に充満するように充填した培養容
器を水平面に対し5〜55゜の範囲の角度に傾斜さ
せた軸の周りに自転するように回転させて当該混
合系を前記培養容器と共に定常的に回転させるこ
とを特徴とする培養方法。 2 水平面に対し5〜55゜の範囲の角度に傾斜す
るよう軸支された回転軸を有する培養容器と、こ
の培養容器を前記回転軸の周りに自転するよう回
転せしめる駆動機構とを有してなり、前記駆動機
構は前記培養容器内に実質的に充満するように充
填された液体培地と接着依存性細胞を付着してな
る被分散粒子、浮遊増殖性細胞もしくは植物組織
との混合系を前記培養容器と共に定常的に回転せ
しめる機能を有するものであることを特徴とする
培養装置。[Scope of Claims] 1. A culture vessel filled with a mixed system of a liquid medium and a mixed system of particles to be dispersed with adhesion-dependent cells, suspended proliferative cells, or plant tissues is held against a horizontal surface. A culture method characterized in that the mixing system is constantly rotated together with the culture container by rotating it so as to rotate around an axis inclined at an angle in the range of 5 to 55 degrees. 2. A culture container having a rotation shaft supported so as to be inclined at an angle of 5 to 55 degrees with respect to a horizontal plane, and a drive mechanism for rotating the culture container so as to rotate around the rotation shaft. The driving mechanism drives a mixed system of a liquid medium filled in the culture container so as to substantially fill the culture container, and dispersed particles formed by adhering adhesion-dependent cells, suspended proliferative cells, or plant tissues. A culture device characterized in that it has a function of constantly rotating together with a culture container.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60180983A JPS6244173A (en) | 1985-08-20 | 1985-08-20 | Method of culture and device therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60180983A JPS6244173A (en) | 1985-08-20 | 1985-08-20 | Method of culture and device therefor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6244173A JPS6244173A (en) | 1987-02-26 |
| JPH0534944B2 true JPH0534944B2 (en) | 1993-05-25 |
Family
ID=16092691
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60180983A Granted JPS6244173A (en) | 1985-08-20 | 1985-08-20 | Method of culture and device therefor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6244173A (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5443985A (en) * | 1993-07-22 | 1995-08-22 | Alberta Research Council | Cell culture bioreactor |
| KR100848938B1 (en) | 2007-04-20 | 2008-07-29 | 코아스템(주) | Cell culture tube and mass cell culture apparatus including the same |
| JP5151923B2 (en) * | 2008-11-18 | 2013-02-27 | 株式会社Ihi | Microorganism concentration device |
| JP5589478B2 (en) * | 2010-03-24 | 2014-09-17 | 株式会社Ihi | Microorganism concentration device |
| AU2020386085B2 (en) | 2019-11-20 | 2022-08-11 | Upside Foods, Inc. | Apparatuses and systems for preparing a meat product |
| US11981884B2 (en) | 2022-10-17 | 2024-05-14 | Upside Foods, Inc. | Pipe-based bioreactors for producing comestible meat products and methods of using the same |
-
1985
- 1985-08-20 JP JP60180983A patent/JPS6244173A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6244173A (en) | 1987-02-26 |
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