JPS6147184A - Cumulative suspension culture for somatic cell and culture medium useful for same - Google Patents

Cumulative suspension culture for somatic cell and culture medium useful for same

Info

Publication number
JPS6147184A
JPS6147184A JP16980184A JP16980184A JPS6147184A JP S6147184 A JPS6147184 A JP S6147184A JP 16980184 A JP16980184 A JP 16980184A JP 16980184 A JP16980184 A JP 16980184A JP S6147184 A JPS6147184 A JP S6147184A
Authority
JP
Japan
Prior art keywords
tank
medium
culture
cells
somatic
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
JP16980184A
Other languages
Japanese (ja)
Inventor
Yasuo Yonezawa
米澤 保雄
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.)
Nippon Zenyaku Kogyo Co Ltd
Original Assignee
Nippon Zenyaku Kogyo 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 Nippon Zenyaku Kogyo Co Ltd filed Critical Nippon Zenyaku Kogyo Co Ltd
Priority to JP16980184A priority Critical patent/JPS6147184A/en
Publication of JPS6147184A publication Critical patent/JPS6147184A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To make cumulative cells into a slow suspension state, and to cultivate them efficiently without damaging them, by dividing a culture meidum into a cell retaining tank and a medium tank by a porous member to pass a medium but not to pass the somatic cells, feeding continuously the medium and stirring the medium. CONSTITUTION:Somatic cells are collected and kept in one of the tank (somatic cell-retaining tank) 2 of a culture medium divided by the porous member (e.g., Teflon perforated plate ) 3, and a mediun in the other tank 1 is sitirred, so that cumulative cells in the cell-retaining tank 2 is made into a slow suspension state, a fresh medium is fed to the culture tank 1, the medium is transferred to the cell-retaining tank 2, and the consumed medium is discharged from the medium outlet 9. Part of the medium and a fresh medium are fed to the medium tank 1 and circulated. By using the culture medium of the construction, the cumulative cells are made into a slow suspension state, and high-density cell culture is carried out.

Description

【発明の詳細な説明】 [産業上の利用分野〕 本発明は体細胞集積浮遊培養法及びそれに使用する培養
器に関するもの゛である。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a somatic cell enrichment suspension culture method and a culture vessel used therein.

[従来の技術] 体細胞の大通培養法の原理は、浮遊細胞ではその培養体
積を、付着依存性細胞ではその培養表面積を拡大する事
にある。そして現在までの所、その方法を具体化するも
のとしては浮遊細胞、マイクロキャリヤーに接着させた
付着依存性細胞の低速攪拌培養器がある(例えば、スピ
ンナー培養フラスコ、低速のジャーファーメンタ−等)
[Prior Art] The principle of the Odori culture method for somatic cells is to expand the culture volume for floating cells and the culture surface area for adhesion-dependent cells. To date, the method has been implemented in low-speed agitated culture vessels for floating cells and attachment-dependent cells attached to microcarriers (e.g., spinner culture flasks, low-speed jar fermenters, etc.).
.

この低速攪拌培養器は、培養器中の培養液を低速(5〜
30回/分程度)で攪拌する事により、浮遊細胞及びマ
イクロキャリヤー付着細胞を円滑に懸濁浮遊し、培養体
積を増大させると同時に、培地と細胞との接触数の増大
による培養成分吸収率の向上を計っているものである。
This low-speed stirring incubator allows the culture solution in the incubator to be stirred at low speed (5~
By stirring at a speed of about 30 times/min), floating cells and cells attached to microcarriers are suspended and suspended, increasing the culture volume, and at the same time, increasing the number of contacts between the culture medium and cells, thereby reducing the absorption rate of culture components. This is something we are trying to improve.

[発明が解決しようとする問題点] しかしながら、浮遊細胞(非付着依存性細胞)及び付着
依存性細胞の両者共に、上述の従来培養法における攪拌
操作は、培養液と細胞との間に剪断力を生じさせ、細胞
に対し損傷を与え、その増殖性をある程度抑制させてし
まう。
[Problems to be Solved by the Invention] However, for both floating cells (non-adhesion-dependent cells) and attachment-dependent cells, the agitation operation in the conventional culture method described above creates a shear force between the culture medium and the cells. This causes damage to cells and inhibits their proliferation to some extent.

即ち、非付着依存性細胞の場合には攪拌によって生じる
剪断力により直接的損傷が起こり、付着依存性細胞の場
合には剪断力によりマイクロキャリヤ−11JI!複合
体の分離及び付着細胞への直接的損傷が起こるのである
That is, in the case of non-adhesion-dependent cells, direct damage occurs due to the shear force generated by agitation, and in the case of attachment-dependent cells, the shear force causes microcarrier-11JI! Dissociation of the complex and direct damage to adherent cells occurs.

[問題点を解決するための手段3 本発明者は、培養細胞の損傷を軽減出来る浮遊培養法及
びそれに使用する培養器を鋭意研究し、本発明を完成し
た。
[Means for solving the problem 3] The present inventor has completed the present invention by intensively researching a suspension culture method that can reduce damage to cultured cells and a culture vessel used therein.

即ち、本発明の第1の方法の発明は、多孔性部材で仕切
った培養器の一方の槽に体細胞を集積保持し、他方の槽
の培地を攪拌する事により、前記一方の槽中の集積細胞
を緩慢な浮遊状態として培養する事を特徴とする体細胞
集積浮遊培養法であり、第2の方法の発明は高酸密度培
養を検討した結果のものであり前記第1の、方法の発明
において、培地槽に新鮮培地を供給し一1細胞保持槽に
培地を移行させ、該細胞保持槽から消費され゛た培地を
排出して連続的に培養する。事を特徴とする体細胞集積
浮遊培養法である。第3の方法の発明は、前記第2の方
法の発明において、細胞保持槽から排出した培地の一部
を新鮮培地と共に培地槽に供給して培地を循環させつつ
培養する事を特徴とする体細胞集積浮遊培養法にかかる
ものである。
That is, in the first method of the present invention, somatic cells are accumulated and retained in one tank of a culture vessel partitioned with a porous member, and the culture medium in the other tank is stirred. This is a somatic cell enrichment suspension culture method characterized by culturing accumulated cells in a slow suspension state, and the invention of the second method is the result of studying high acid density culture, and is different from the first method. In the invention, a fresh medium is supplied to a culture medium tank, the medium is transferred to a cell holding tank, and the consumed medium is discharged from the cell holding tank for continuous cultivation. This is a somatic cell enrichment suspension culture method that is characterized by: The invention of a third method is the invention of the second method, characterized in that a part of the medium discharged from the cell holding tank is supplied to the medium tank together with a fresh medium, and the culture is carried out while circulating the medium. This involves a cell enrichment suspension culture method.

又、以上の方法の発明を実施するだめの本発明の装置の
発明は、培養器の内部を、培地は通過させるがm胞は通
過させない多孔性部材により細胞保持槽と培地槽とに仕
切り、該培地槽内の培地を攪拌可能に構成した事を特徴
とする体細胞集積浮遊培養器にかかるものである。
Further, the invention of the apparatus of the present invention for carrying out the invention of the method described above is such that the inside of the culture vessel is partitioned into a cell holding tank and a medium tank by a porous member that allows the medium to pass through but does not allow the cells to pass through. This invention relates to a suspension culture device for accumulating somatic cells, characterized in that the culture medium in the culture medium tank can be stirred.

以上において、培養器を仕切る多孔性部材は、培地は通
過させるが培養細胞は通過させない大ぎさの孔を多数有
するものであればよく、具体的にはナイロンメツシュ等
のメツシュ布が使用できる。
In the above, the porous member that partitions the culture vessel may be any member having a large number of pores that allow the culture medium to pass through but not the cultured cells. Specifically, mesh cloth such as nylon mesh can be used.

使用する培養器の大きさ、形状は培養の目的、量等に応
じて適宜のものを使用する事が出来、培養器を仕切る方
法は上下、左右或は斜めのいずれでもよいが、上下に仕
切るのが好ましい。
The size and shape of the culture vessel to be used can be appropriate depending on the purpose of culture, quantity, etc. The culture vessel can be partitioned vertically, horizontally, or diagonally, but it is best to partition it vertically. is preferable.

仕切った培養器のいずれの槽を細胞保持槽としても差し
支えないが、上下に仕切った場合には上槽を細胞保持槽
とし下槽を培地槽とするのがよい。
Any tank in a partitioned culture vessel may be used as a cell holding tank, but when partitioned into an upper and lower tank, it is preferable to use the upper tank as the cell holding tank and the lower tank as the culture medium tank.

培地槽の培地の攪拌手段は、スピンナー等を利用する事
ができる。
A spinner or the like can be used as a means for stirring the medium in the culture medium tank.

本発明の培養法に適用できる体III胞としては、非付
着依存性の浮遊m胞及び付着依存性細胞がある。具体的
には、浮遊細胞の例としてプラズマサイトーマ(S P
 210 ) 、S P 210.111胞とジステン
パーウィルスで免疫したBALD/Cマウスの牌細胞と
細胞融合法によって造成したハイブリドーマ等がある。
Body III cells that can be applied to the culture method of the present invention include non-adhesion-dependent floating cells and attachment-dependent cells. Specifically, plasmacytoma (SP) is an example of floating cells.
210), and hybridomas created by a cell fusion method with tile cells of BALD/C mice immunized with SP 210.111 cells and distemper virus.

付着依存性細胞の例としてはベロ(Vero)l胞、ジ
ステンパーウィルス等があり、この場合にはマイクロキ
ャリヤーを接着担体として使用する。
Examples of adhesion-dependent cells include Vero cells, distemper virus, etc., in which case microcarriers are used as adhesion carriers.

又使用する培地は培養すべき体細胞の種類に応じて適宜
のものを選択して使用し、その他の培養条件(培養温度
等)は通常の一般的条件で行なう。
The medium to be used is appropriately selected depending on the type of somatic cells to be cultured, and other culture conditions (culture temperature, etc.) are carried out under normal general conditions.

[作   用] 第1の方法はいわゆるバッチ培養法といわれるもので、
細胞保持槽と培地m<攪拌WJ)とを多孔性部材からな
るII飽保持膜により隔離したので、攪拌槽での攪拌力
により培地が強制的に流動され、前記多孔性部材を通っ
て細胞保持槽の浮遊細胞、マイクロキャリヤー・付着依
存性細胞複合体等の集積細胞が緩慢な浮遊状態に浮遊さ
れる。即ち、従来の培養槽の培地全体を攪拌する事を排
したので、この攪拌が細胞へ及ぼす1tA傷筈の悪影響
を低減する事ができる。
[Effect] The first method is the so-called batch culture method,
Since the cell holding tank and the medium m<stirring WJ) are isolated by the II saturation holding membrane made of a porous member, the medium is forcibly flowed by the stirring force in the stirring tank, and the cell holding tank is passed through the porous member. Accumulated cells such as floating cells in the tank and microcarrier/adhesion-dependent cell complexes are suspended in a slow floating state. That is, since it is not necessary to stir the entire culture medium in the conventional culture tank, it is possible to reduce the adverse effect of 1tA damage on the cells due to this stirring.

第2の方法は連続i8養法であり、攪拌槽から新鮮培地
を供給し、細胞培養槽へ新鮮培地を通過させ、消費した
培地を細胞保持槽から排出する事により、通常のバッチ
ワイズ(3atchvise)法に比べ約8〜10倍の
細胞を得る事ができる。
The second method is the continuous i8 cultivation method, in which fresh medium is supplied from a stirring tank, the fresh medium is passed through the cell culture tank, and the spent medium is discharged from the cell holding tank. ) It is possible to obtain about 8 to 10 times more cells than the method.

第3の方法は、連続培養法における培地の流通を連続と
した循環式連続培養法であり、ウィルスの培養を飛躍的
に向上する事ができる。
The third method is a circulating continuous culture method in which the medium is continuously circulated in the continuous culture method, which can dramatically improve virus culture.

更に本発明の培養器によれば、上記の各培養方法をきわ
めて容易に実施する事を可能とするものである。
Furthermore, according to the incubator of the present invention, each of the above-mentioned culture methods can be carried out extremely easily.

[実 施 例] 以下、本発明を実施例により更に具体的に説明する。[Example] EXAMPLES Hereinafter, the present invention will be explained in more detail with reference to Examples.

実施例1 第1図は本発明の培養器の一実施例であり、円筒状の培
地槽1の上方に円筒状の細胞保持槽2を位置させ、両槽
1,2間にデフロン製の目皿3で両側から挟持したフィ
ルター4を介在させ、オーリングパイトン5及びオーリ
ング6を介して両槽1,2を水密となる様固定用リング
7により固定しである。8は培地槽1の側部に設けた培
地入口、9は細胞保持層2の上部側面に設けた培地出口
、10はキャップ、11はパツキン、12は培地槽1の
底部においてマグネチツクスターラ−13により外部か
ら回転されるスクリュー型マグネットを示ず。
Example 1 FIG. 1 shows an example of the incubator of the present invention, in which a cylindrical cell holding tank 2 is positioned above a cylindrical culture medium tank 1, and a deflon eye is placed between both tanks 1 and 2. A filter 4 sandwiched from both sides by a plate 3 is interposed, and both tanks 1 and 2 are fixed by a fixing ring 7 through an O-ring piton 5 and an O-ring 6 so as to be watertight. 8 is a medium inlet provided on the side of the medium tank 1, 9 is a medium outlet provided on the upper side of the cell holding layer 2, 10 is a cap, 11 is a packing, 12 is a magnetic stirrer 13 at the bottom of the medium tank 1. The screw type magnet rotated from the outside is not shown.

非付着依存性細胞例えばプラズマサイトーマ(SP21
0)の培養を行なう場合には、60〜90賜のフィルタ
ー14を装置し、培地WJ1での攪拌速度を35〜50
0回/分とする事で、フィルター4上の細胞を緩慢な浮
遊状態に置く事が出来る。M1図に示した規模(全高3
50mm 、直径110mm )の本発明の培養器によ
れば、細胞の接pi ffjl ヲ10”5佃p 、/
 11e X 1(111トL jC’1合、10日間
培養で1o 6−3細胞/1!となり、従来のスピンナ
ー培養の105.5細胞/11に比して約10倍の増殖
性を得る事が出来る。
Non-adhesion dependent cells such as plasmacytoma (SP21
0), a filter 14 of 60 to 90 mm is installed, and the stirring speed of the medium WJ1 is set to 35 to 50 mm.
By setting the rate to 0 times/min, the cells on the filter 4 can be placed in a slow floating state. The scale shown in the M1 diagram (total height 3
According to the incubator of the present invention having a diameter of 50 mm and a diameter of 110 mm, the cell connection rate is
11e x 1 (111tLjC'1 combination, 10 6-3 cells/1! after 10 days of culture, approximately 10 times the proliferation rate compared to 105.5 cells/11 in conventional spinner culture) I can do it.

実施例2 更に効果的なのは、体細胞の生産物を得る場合である。Example 2 Even more effective is the case where products of somatic cells are obtained.

例えば、5P2101胞とジステンパーウィルスで免疫
したBAL8/cマウスの牌細胞と細胞融合法によって
造成したバイブリド、−マの培養を前記第1図に示した
本発明の培養器で行なう事によって、従来のスピンナー
フラスコの同容量培地を用いるよりも、モノクローナル
抗体の生産性を向上する事が出来る。
For example, by culturing BAL8/c mouse tile cells immunized with 5P2101 cells and distemper virus and hybridomas produced by the cell fusion method in the incubator of the present invention shown in FIG. Monoclonal antibody productivity can be improved compared to using the same volume of culture medium in a spinner flask.

即ち、1!のスピンナーフラスコ(3orpmの回転数
、培地としてD−MEM、牛胎児血清1,0%)の培養
7日間では、抗ジステンパーモノクローナル抗体が50
0単位/ν1 (S/N価)しか生産されないのに対し
、本発明の培養法では5200単位/W (S/N価)
を1qる事が出来、本発明が従来のスピンナー培養に比
べ、その細胞の生理状態を向上させている事を示してい
る。
That is, 1! During 7 days of culture in spinner flasks (rotation speed: 3 orpm, D-MEM as medium, 1.0% fetal bovine serum), anti-distemper monoclonal antibodies
Whereas only 0 unit/ν1 (S/N value) is produced, the culture method of the present invention produces 5200 units/W (S/N value).
1q, indicating that the present invention improves the physiological state of the cells compared to conventional spinner culture.

実施例3 第2図は本発明の培養器の他の実施例であり、前記実施
例と略同様の構成において、培地人口8に新鮮培地容器
15からの管16を接続し、菌フィルター17を通して
圧力ガスを該新鮮培地容器15に送入し、新鮮培地を培
地槽1に供給する様にしである。
Embodiment 3 FIG. 2 shows another embodiment of the incubator of the present invention, which has substantially the same configuration as the previous embodiment, in which a pipe 16 from a fresh culture medium container 15 is connected to a culture medium 8, and a tube 16 from a fresh culture medium container 15 is passed through a bacterial filter 17. Pressure gas is fed into the fresh culture medium container 15 to supply fresh culture medium to the culture medium tank 1.

重環11器により、効率の良い培養を行なうには、第2
図の様に培地槽1より新鮮培地を注入し、細胞を培養し
ている細胞保持槽2より排出する事により連続培養法を
取る事が出来る。連続培養法はバッチ法(回分法)に比
し、IIIVI&増殖阻害物質の希釈と共に新鮮な栄養
分の供給が出来るので、例えば3.5!の連続培養を行
なう事によって、ハイブリドーマ細胞の培養で総計7日
間で36480単位# (S/N価)を得る事が出来る
In order to perform efficient culture using 11 heavy ring vessels, the second
As shown in the figure, a continuous culture method can be used by injecting a fresh medium from the medium tank 1 and discharging it from the cell holding tank 2 in which the cells are being cultured. Compared to the batch method, the continuous culture method allows for the dilution of IIIVI and growth inhibitory substances as well as the supply of fresh nutrients, for example 3.5! By continuously culturing the hybridoma cells, 36,480 units # (S/N value) can be obtained in a total of 7 days.

実施例4 担体に接着させた付着依存性1細胞を培養する場合にも
、本発明の培養器は以下のように効果を示す。第1図の
培養器でサイトデツクス(CVt0deX) 21.:
付着したへa (Vero ) m胞(Ill胞・担体
複合体)の培養を行なった場合、マイクロキャリヤー上
のベロ細胞の増殖細胞は、通常のスピンナーフラスコ(
1))では5[胞/担体であるのに比べ、本発明の培i
法では81IIIli!/担体に向上させる事が出来る
Example 4 The incubator of the present invention also exhibits the following effects when culturing adhesion-dependent 1 cells adhered to a carrier. Cytodex (CVt0deX) in the incubator shown in Figure 1 21. :
When culturing the attached a (Vero) m cells (Ill cells/carrier complex), the proliferating Vero cells on the microcarriers are grown in a normal spinner flask (
1)), the culture medium of the present invention
81IIIli in law! / It can be improved into a carrier.

実施例5 実施例4と同様の培養系にてジステンパーウィルスを培
養した場合、スピンナー培養では107/yfであるが
、本発明の培養法では1o910y−を得る事が出来る
Example 5 When distemper virus is cultured in the same culture system as in Example 4, spinner culture yields 107/yf, but the culture method of the present invention yields 1o910yf.

実施例6 第3図は本発明の培養器の更に他の実施例であり、前記
他の実施例と略同様の構成において細胞保持槽2の培地
出口9に管路18を接続し、咳管路18の先端部を分岐
せしめ一方の分岐管19を排出用とし、他方の分岐管2
0を循環用とし、循環用ポンプ21により新鮮培地と共
に培地槽1に循環供給するようにしである。
Embodiment 6 FIG. 3 shows still another embodiment of the incubator of the present invention, in which the conduit 18 is connected to the medium outlet 9 of the cell holding tank 2, and the cough tube The tip of the channel 18 is branched, one branch pipe 19 is used for discharge, and the other branch pipe 2 is used for discharge.
0 is used for circulation, and a circulation pump 21 is used to circulate and supply the culture medium together with the fresh culture medium to the culture medium tank 1.

この培養器により循環式連続培養法が行なえ、ジステン
パーウィルスを高生産する事が出来る。
With this incubator, a circulating continuous culture method can be performed and distemper virus can be produced at a high level.

例えばサイトデックス2を25ma/yfの濃度でベロ
細胞を増殖させ、3.5!の循環式連続培養を行なう事
により総計1t3”x 3.s!のウィルス量を得る事
が出来る。
For example, when Vero cells are grown with Cytodex 2 at a concentration of 25 ma/yf, 3.5! A total amount of virus of 1 t3" x 3.s! can be obtained by carrying out continuous circulating culture.

[発明の効果コ 以上述べたように本発明の体細胞集積浮遊培養法及びそ
れに使用する培養器によれば、培養器内を多孔性部材で
仕切り、一方の槽を1oIll保持槽とし他方の槽を培
地槽として、培地槽を攪拌させる事により細胞保持槽に
ゆるやかな攪拌効果を波及させて培養するようにしたの
で、培!Ill胞の損傷を著しく軽減する事が出来、効
率のよい培養を行なえる。又、新鮮培地を補給しながら
a続的に培養する事により、高密度の細胞培養を行なう
事が出来、更に培地の一部を循環させつつ培養する事に
より、培養液中の細胞生産物の濃度を著しく高める事が
出来る。
[Effects of the Invention] As described above, according to the somatic cell enrichment suspension culture method of the present invention and the culture vessel used therein, the inside of the culture vessel is partitioned with a porous member, and one tank is a 1oIll holding tank and the other tank is By using the medium tank as a culture medium tank, by stirring the culture medium tank, the gentle stirring effect spreads to the cell holding tank for culture. Damage to Ill cells can be significantly reduced and efficient culture can be performed. In addition, by continuously culturing while supplementing fresh medium, high-density cell culture can be achieved, and by culturing while circulating a portion of the medium, cell products in the culture solution can be The concentration can be significantly increased.

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

第1図は本発明の培養器の一実施例の部分切断説明図、
第2図は本発明の培養器の他の実施例の説明図、第3図
は本発明の培IIlの更に他の実施例の説明図である。 1は培地槽、2はm胞保持槽、4はフィルター、8は培
地入口、9は培地出口、12はスクリュー型マグネット
、15°は新鮮培地容器を示す。 特  許  出  願  人 日本全薬工業株式会社 第1図 第2図
FIG. 1 is a partially cutaway explanatory diagram of an embodiment of the incubator of the present invention;
FIG. 2 is an explanatory diagram of another embodiment of the incubator of the present invention, and FIG. 3 is an explanatory diagram of still another embodiment of the culture medium III of the present invention. 1 is a medium tank, 2 is an m cell holding tank, 4 is a filter, 8 is a medium inlet, 9 is a medium outlet, 12 is a screw type magnet, and 15° is a fresh medium container. Patent application Nippon Zenyaku Kogyo Co., Ltd. Figure 1 Figure 2

Claims (1)

【特許請求の範囲】 1)多孔性部材で仕切つた培養器の一方の槽に体細胞を
集積保持し、他方の槽の培地を攪拌する事により、前記
一方の槽中の集積細胞を緩慢な浮遊状態として培養する
事を特徴とする体細胞集積浮遊培養法。 2)一方の槽に集積保持された細胞が、浮遊細胞である
特許請求の範囲第1)項記載の体細胞集積浮遊培養法。 3)一方の槽に集積保持された細胞が、キャリヤーに接
着させた付着依存性細胞である特許請求の範囲第1)項
記載の体細胞集積浮遊培養法。 4)多孔性部材で仕切つた培養器の一方の槽に体細胞を
集積保持し、他方の槽の培地を攪拌する事により、前記
一方の槽中の集積細胞を緩慢な浮遊状態とし、該他方の
槽に新鮮培地を供給し、前記一方の槽に新鮮培地を移行
させ、該一方の槽から消費された培地を排出して連続的
に培養する事を特徴とする体細胞集積浮遊培養法。 5)多孔性部材で仕切つた培養器の一方の槽に体細胞を
集積保持し、他方の槽の培地を攪拌する事により、前記
一方の槽中の集積細胞を緩慢な浮遊状態とし、該他方の
槽に新鮮培地を供給し、前記一方の槽に新鮮培地を移行
させ、該一方の槽から消費された培地を排出し、該排出
した培地の一部を新鮮培地と共に前記他方の槽に供給し
て培地を循環させつつ培養する事を特徴とする体細胞集
積浮遊培養法。 6)培養器の内部を、培地は通過させるが細胞は通過さ
せない多孔性部材により細胞保持槽と培地槽とに仕切り
、該培地槽内の培地を攪拌可能に構成した事を特徴とす
る体細胞集積浮遊培養器。 7)細胞保持槽が培地出口を備えた細胞保持槽であり、
培地槽が培地入口を備えた培地槽である特許請求の範囲
第6)項記載の体細胞集積浮遊培養器。
[Claims] 1) Somatic cells are accumulated and maintained in one tank of a culture vessel partitioned with a porous member, and the accumulated cells in said one tank are slowly removed by stirring the medium in the other tank. A somatic cell enrichment suspension culture method characterized by culturing in a suspended state. 2) The somatic cell enrichment suspension culture method according to claim 1), wherein the cells accumulated and maintained in one tank are floating cells. 3) The somatic cell enrichment suspension culture method according to claim 1), wherein the cells accumulated and retained in one tank are adhesion-dependent cells adhered to a carrier. 4) Somatic cells are accumulated and maintained in one tank of a culture vessel partitioned by a porous member, and the culture medium in the other tank is stirred to bring the accumulated cells in the one tank into a slow floating state, and the other tank is A somatic cell enrichment suspension culture method characterized by supplying a fresh medium to the tank, transferring the fresh medium to the one tank, discharging the consumed medium from the one tank, and culturing continuously. 5) Somatic cells are accumulated and maintained in one tank of a culture vessel partitioned by a porous member, and the culture medium in the other tank is stirred to bring the accumulated cells in the one tank into a slow floating state, supplying a fresh medium to the tank, transferring the fresh medium to the one tank, discharging the consumed medium from the one tank, and supplying a part of the discharged medium to the other tank together with the fresh medium. A somatic cell enrichment suspension culture method characterized by culturing while circulating a medium. 6) Somatic cells, characterized in that the inside of the culture vessel is partitioned into a cell holding tank and a medium tank by a porous member that allows the medium to pass through but not the cells, and the culture medium in the medium tank can be stirred. Integrated floating culture vessel. 7) The cell holding tank is a cell holding tank equipped with a medium outlet,
The somatic cell enrichment suspension culture device according to claim 6, wherein the culture medium tank is a culture medium tank equipped with a medium inlet.
JP16980184A 1984-08-14 1984-08-14 Cumulative suspension culture for somatic cell and culture medium useful for same Pending JPS6147184A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16980184A JPS6147184A (en) 1984-08-14 1984-08-14 Cumulative suspension culture for somatic cell and culture medium useful for same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16980184A JPS6147184A (en) 1984-08-14 1984-08-14 Cumulative suspension culture for somatic cell and culture medium useful for same

Publications (1)

Publication Number Publication Date
JPS6147184A true JPS6147184A (en) 1986-03-07

Family

ID=15893144

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16980184A Pending JPS6147184A (en) 1984-08-14 1984-08-14 Cumulative suspension culture for somatic cell and culture medium useful for same

Country Status (1)

Country Link
JP (1) JPS6147184A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102007036611A1 (en) * 2007-08-02 2009-02-05 Deutsche Diabetes-Forschungsgesellschaft E.V. Method and device for cultivating living cells

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102007036611A1 (en) * 2007-08-02 2009-02-05 Deutsche Diabetes-Forschungsgesellschaft E.V. Method and device for cultivating living cells
DE102007036611B4 (en) * 2007-08-02 2015-10-08 Deutsche Diabetes-Forschungsgesellschaft E.V. Method and device for cultivating living cells

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