JP3036032B2 - Cell culturing method and device - Google Patents

Cell culturing method and device

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Publication number
JP3036032B2
JP3036032B2 JP2246638A JP24663890A JP3036032B2 JP 3036032 B2 JP3036032 B2 JP 3036032B2 JP 2246638 A JP2246638 A JP 2246638A JP 24663890 A JP24663890 A JP 24663890A JP 3036032 B2 JP3036032 B2 JP 3036032B2
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Japan
Prior art keywords
cells
perforated plate
hole
culture solution
closed container
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.)
Expired - Fee Related
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JP2246638A
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Japanese (ja)
Other versions
JPH04126068A (en
Inventor
正浩 昆
幸生 福島
茂美 鈴木
繁 山野
信之 前橋
Original Assignee
日立プラント建設株式会社
東陶機器株式会社
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Priority to JP2246638A priority Critical patent/JP3036032B2/en
Publication of JPH04126068A publication Critical patent/JPH04126068A/en
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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は接着性の細胞を高密度且つ大量に培養する方
法及び装置に係り、特に細胞が代謝した老廃物を取り出
す濾過設備を備えた細胞の培養方法及びその装置に関す
る。
Description: TECHNICAL FIELD The present invention relates to a method and an apparatus for culturing adherent cells in high density and in a large amount, and in particular, to a cell provided with a filtration facility for removing waste products metabolized by cells. The present invention relates to a culture method and a device therefor.

〔従来の技術〕[Conventional technology]

近年、生体外で細胞を大量に培養してインターフェロ
ン等の生物薬品を生産する技術はとみにその重要性を増
している。特に接着性の細胞は多くの生理活性物質を生
産するので、その大量且つ高密度培養技術の確立は生産
の効率向上や生産コスト低減のために必須である。
In recent years, the technology of producing biological drugs such as interferon by culturing a large amount of cells in vitro has become increasingly important. In particular, since adherent cells produce many physiologically active substances, the establishment of a large-scale and high-density culture technique is essential for improving production efficiency and reducing production costs.

ところで、一般に接着性の細胞を大量で高密度に培養
する方法として、マイクロキャリア法とホロファイバー
法が知られている。マイクロキャリア法は直径数百μm
のマイクロキャリア上に細胞を付着させ、通気撹拌槽内
で浮遊培養する方法であり、この方法はスケールアップ
が容易で大量培養に適する。
Incidentally, a microcarrier method and a holofiber method are generally known as methods for culturing a large amount of adherent cells at high density. Microcarrier method is several hundred μm in diameter
Is a method in which cells are attached to microcarriers and suspended and cultured in an aeration and stirring tank. This method is easy to scale up and is suitable for mass culture.

一方、ホロファイバー法はホロファイバー膜を束ねた
容器内で細胞を膜に付着させて培養するもので、膜を介
して栄養分と酸素を含む新鮮な培養液を細胞に供給で
き、部分的には108個/mlの高濃度まで細胞を培養するこ
とができる(例えば特開昭62−163687号公報参照)。こ
のホロファイバー法は培養液の供給及び取り出しを、ホ
ロファイバー内に培養液を流して供給口と液出口の圧損
を利用して行っている。
On the other hand, the holo-fiber method involves culturing cells by attaching them to a membrane in a container with a bundle of holo-fiber membranes.A fresh culture solution containing nutrients and oxygen can be supplied to the cells via the membrane, and partially the cells can be cultured to high concentrations of 10 8 / ml (see, for example, JP-a-62-163687). In the holo fiber method, the culture solution is supplied and taken out by flowing the culture solution into the holo fiber and utilizing the pressure loss between the supply port and the liquid outlet.

〔発明が解決しようとする課題〕[Problems to be solved by the invention]

しかしながら、マイクロキャリア法は撹拌槽内で培養
するため、撹拌翼によって物理的な損傷を受けることが
避けられず、高密度に培養することが困難であるという
問題がある。また、培養開始前にマイクロキャリア上に
種細胞を付着させるために、マイクロキャリアを約10時
間細胞懸濁液中に浸漬する必要があるので、マイクロキ
ャリアに付着せず懸濁液中に残留する細胞が多く、この
間に細胞が死滅するという問題がある。更に、細胞培養
中に酸素の供給をするときに、培養液が発泡したり、マ
イクロキャリアからの細胞の分離が困難であるという問
題がある。
However, since the microcarrier method is cultivated in a stirring tank, it is unavoidable that the microcarrier method is physically damaged by the stirring blade, and it is difficult to culture at high density. In addition, the microcarriers need to be immersed in the cell suspension for about 10 hours in order to attach the seed cells to the microcarriers before the start of culture, so they do not adhere to the microcarriers and remain in the suspension. There is a problem that many cells are killed during this time. Furthermore, when oxygen is supplied during cell culture, there are problems that the culture solution foams and that it is difficult to separate cells from microcarriers.

一方、ホロファイバー法はホロファイバー内の圧力が
高く液供給口付近では容器内との差圧が大きいので膜を
介して培養液を容器内に供給し、液出口付近ではホロフ
ァイバー内の圧力が容器内より低くなるので膜を介して
培養液を取り出している。このため、ホロファイバーの
中央付近では、ホロファイバー内と容器の差圧が少ない
ので膜を透過する培養液の量が少なくなる。従って、培
養液の供給が不均一になるため、部分的にしか高濃度の
培養を行えないという問題がある。また、束状のホロフ
ァイバー膜から細胞を剥離させることが困難なので、細
胞の収率が低くなると共にホロファイバーの再利用が不
可能になり、ランニングコストが高価になるという問題
がある。
On the other hand, in the holo-fiber method, the pressure inside the holo-fiber is high and the pressure difference between the inside of the container and the liquid supply port is large, so the culture solution is supplied into the container through the membrane. The culture solution is taken out through the membrane because it is lower than the inside of the container. For this reason, near the center of the hollow fiber, the pressure difference between the inside of the hollow fiber and the container is small, so that the amount of the culture solution permeating the membrane is reduced. Therefore, since the supply of the culture solution becomes uneven, there is a problem that the culture at a high concentration can be performed only partially. Further, since it is difficult to detach cells from the bundle of holofiber membranes, there is a problem that the yield of cells is low, the holofibers cannot be reused, and the running cost is high.

本発明はこのような事情に鑑みて成されたもので、細
胞に培養や酸素を均一に供給して、大量の細胞を高密度
に培養できる細胞の培養方法及びその装置を提供するこ
とを目的とする。
The present invention has been made in view of such circumstances, and it is an object of the present invention to provide a cell culturing method and a device capable of culturing a large number of cells at high density by uniformly culturing cells and supplying oxygen to the cells. And

〔課題を解決する為の手段〕[Means for solving the problem]

本発明は、前記目的を達成する為に、表面に細胞が付
着する複数枚の多孔板と、該複数板の多孔板が所定間隔
で並設されるとともに多孔板の表面と連通する貫通孔を
有する回転自在な支軸とから成る濾過体と、前記濾過体
を収納するとともに該濾過体の支軸を支持する密閉容器
と、培養液を含む1乃至複数の流体を前記密閉容器に加
圧状態で供給する手段と、を備えたことを特徴としてい
る。
The present invention, in order to achieve the above object, a plurality of perforated plates to which cells adhere to the surface, and a plurality of perforated plates are juxtaposed at predetermined intervals and a through hole communicating with the surface of the perforated plate. A filter body comprising a rotatable support shaft, a closed container for accommodating the filter body and supporting the support shaft of the filter body, and pressurizing one or more fluids including a culture solution in the closed container. And means for supplying by means of:

また、本発明は、前記目的を達成する為に、貫通孔を
有する支軸に細胞を付着させる複数の多孔板を、支軸内
の貫通孔に連通するように装着して成る濾過体を、密閉
容器内に設置した培養装置を用い、培養液を加圧状態に
して密閉容器に供給すると共に、支軸内の貫通孔を大気
圧又は減圧状態にし老廃物を含む培養液を多孔板及び貫
通孔を介して取り出すことを特徴としている。
Further, the present invention, in order to achieve the above object, a plurality of perforated plates for attaching cells to a spindle having a through-hole, a filter body attached so as to communicate with the through-hole in the spindle, Using a culture device installed in a closed container, the culture solution is supplied to the closed container in a pressurized state, and the through-hole in the support shaft is set to the atmospheric pressure or reduced pressure to pass the culture solution containing wastes through the perforated plate and through. It is characterized in that it is taken out through a hole.

〔作用〕[Action]

本発明によれば、貫通孔が形成されている支軸に、貫
通孔に連通するように濾過体の多孔板を複数板並設して
支軸を密閉容器内に設け、更に培養液等を供給する供給
手段を密閉容器に連通した。従って、この供給手段を操
作すると新鮮な培養液を密閉容器内に供給して濾過体の
多孔板に付着した細胞に栄養分と酸素とを与え、同時に
細胞に付着している老廃物を除去して培養液と共に多孔
板を透過して細胞から分離すことができる。
According to the present invention, a plurality of perforated plates of a filter are arranged side by side in a closed vessel so as to communicate with the through hole, and the support shaft is provided in the closed container, and the culture solution and the like are further provided on the support shaft having the through hole formed therein. The supply means for supplying was connected to the closed vessel. Therefore, when this supply means is operated, a fresh culture solution is supplied into the closed vessel to provide nutrients and oxygen to the cells attached to the perforated plate of the filter, and at the same time to remove waste products attached to the cells. It can be separated from cells by passing through the perforated plate together with the culture solution.

〔実施例〕〔Example〕

以下添付図面に従って本発明に係る細胞の培養方法及
びその装置の好ましい実施例を詳説する。
Hereinafter, preferred embodiments of the cell culture method and apparatus according to the present invention will be described in detail with reference to the accompanying drawings.

第1図は本発明による培養装置の一実施例を示す全体
図である。培養装置10は円筒型の密閉容器12を備え、密
閉容器12には多孔板ユニット13が設けられている。この
多孔板ユニット13の回転軸14は、第2図に示すように密
閉容器12の中心に回転自在に支持され、回転軸14には軸
線上に貫通孔16が形成されている。貫通孔16は第2図上
で回転軸14の左端部に開口して流入口16Aを形成してい
る。回転軸14にはドーナツ状の多孔板20、20…が装着さ
れ、この多孔板20は連通孔18を介して貫通孔16に連通し
ている。
FIG. 1 is an overall view showing an embodiment of the culture apparatus according to the present invention. The culture apparatus 10 includes a cylindrical closed container 12, and the closed container 12 is provided with a perforated plate unit 13. The rotating shaft 14 of the perforated plate unit 13 is rotatably supported at the center of the closed container 12 as shown in FIG. 2, and the rotating shaft 14 has a through hole 16 formed on the axis thereof. The through hole 16 is opened at the left end of the rotating shaft 14 in FIG. 2 to form an inlet 16A. .. Are attached to the rotating shaft 14, and the perforated plates 20 communicate with the through holes 16 through the communication holes 18.

また、密閉容器12には流入口22と流出口24とが設けら
れている。密閉容器12は内径330mm、長さ700mmの円筒状
に形成され、その中に多孔板20、20が設けられているの
で、密封容器12の有効容積は42である。また、密閉容
器12の外周面には温度調節のために外周面に沿って温水
を流すことができるようにジャケット25が取付けられて
いる。
Further, the closed container 12 is provided with an inlet 22 and an outlet 24. The sealed container 12 is formed in a cylindrical shape having an inner diameter of 330 mm and a length of 700 mm, and the perforated plates 20 and 20 are provided therein, so that the effective volume of the sealed container 12 is 42. A jacket 25 is attached to the outer peripheral surface of the sealed container 12 so that warm water can flow along the outer peripheral surface for temperature control.

第3図は多孔板20の詳細と、その回転軸14への取付け
状態とを示したもので多孔板20はセラミック製の円板
で、その内周面は回転軸14の貫通孔16と連通する連通孔
18に当接して設けられている。多孔板20は孔径10μm〜
100μmと粗く透過抵抗が小さい多孔質の支持体26A上に
孔径0.01μm〜5μmと細かく透過抵抗が大きい多孔質
の層26Bを設けた多層構造の多孔質層26で形成されてい
る。このため、液が透過するときには多孔板20の表面で
の圧損が律速となって、多孔板20上のいずれの個所にお
いても貫通孔16まで液が流れるときの圧損がほぼ等しく
なる。従って、貫通孔16に近い個所だけから液がショー
トパスすることがなく、いずれの場所からも均一に培養
液の供給及び取り出しが行なえるので、多孔板ユニット
13は培養液の供給用及び細胞の老廃物取り出し用の両方
に用いるとができる。また、多孔板20は細胞の付着を容
易にするために、表面の粗さを約20μmに研磨してい
る。この多孔板20は、その直径が300mm、厚さが5mmに形
成され、密閉容器12の回転軸14に8mm間隔で各々50枚配
設されている。
FIG. 3 shows the details of the perforated plate 20 and the state of its attachment to the rotating shaft 14. The perforated plate 20 is a disc made of ceramic, and its inner peripheral surface communicates with the through hole 16 of the rotating shaft 14. Communication hole
It is provided in contact with 18. The perforated plate 20 has a pore diameter of 10 μm
It is formed of a porous layer 26 having a multilayer structure in which a fine porous layer 26B having a pore size of 0.01 μm to 5 μm and a large transmission resistance is provided on a porous support 26A which is coarse and has a small transmission resistance of 100 μm. For this reason, when the liquid permeates, the pressure loss on the surface of the perforated plate 20 is rate-determining, and the pressure loss when the liquid flows to the through hole 16 at any point on the perforated plate 20 is substantially equal. Therefore, the liquid is not short-passed only from the portion close to the through-hole 16 and the culture solution can be uniformly supplied and removed from any location.
13 can be used both for supplying a culture solution and for removing waste products from cells. The surface of the perforated plate 20 is polished to about 20 μm in order to facilitate cell attachment. The perforated plates 20 have a diameter of 300 mm and a thickness of 5 mm, and 50 perforated plates are arranged on the rotating shaft 14 of the sealed container 12 at intervals of 8 mm.

多孔板ユニット13が収納されている密封容器12は第1
図に示すように培養液などを貯留する各槽(34、36、3
8、39、40、42、44、46)、及び送液のための圧力源と
なるコンプレッサ30、真空ポンプ32等に接続されてい
る。
The sealed container 12 containing the perforated plate unit 13 is the first container.
As shown in the figure, each tank (34, 36, 3
8, 39, 40, 42, 44, 46), and a compressor 30, a vacuum pump 32, and the like, which are pressure sources for liquid feeding.

以下第1図に基づいてこれらの関係を説明する。密封
容器12の流入口22には、種細胞貯槽34、洗浄などに使用
される緩衝液の貯槽36、多孔板20を洗浄するアルカリ液
の貯槽38、及び培養液貯槽39が連通されている。これら
の各貯槽34、36、38及び39はコンプレッサ30と接続され
ており、コンプレッサ30からの無菌圧縮空気で液を加圧
し、密閉容器12に送れるようになっている。また、流入
口22には減菌用の蒸気を発生するボイラ40も連通されて
いる。
Hereinafter, these relationships will be described with reference to FIG. The inflow port 22 of the sealed container 12 communicates with a seed cell storage tank 34, a storage tank 36 for a buffer solution used for washing and the like, a storage tank 38 for an alkaline solution for washing the porous plate 20, and a culture solution storage tank 39. Each of these storage tanks 34, 36, 38, and 39 is connected to the compressor 30, so that the liquid can be pressurized by aseptic compressed air from the compressor 30 and sent to the sealed container 12. Further, a boiler 40 for generating steam for sterilization is connected to the inflow port 22.

流出口24には、密閉容器12の液を排出する管33A、及
び培養完了後多孔板20から剥離された細胞を種細胞貯槽
34に送るための管33Bが接続されている。
The outlet 24 has a tube 33A for discharging the liquid in the closed container 12, and a seed cell storage tank for cells detached from the porous plate 20 after completion of the culture.
A pipe 33B for sending to 34 is connected.

多孔板ユニット13の回転軸14の流出入口16Aには、培
養完了後多孔板20から細胞を剥離させるためのトリプシ
ンを供給するためのトリプシン貯槽42が連通されてい
る。このトリプシン貯槽42もコンプレッサ30と接続され
ており、コンプレッサ30からの無菌圧縮空気で液を加圧
し、密閉容器12に送れるようになっている。また、この
流出入口16Aには、細胞の生産物を回収する生産物貯槽4
4、細胞の老廃物を回収する老廃物貯槽46が連通されて
いる。これらの貯槽44、46は真空ポンプ32と接続されて
おり、多孔板20を介して密閉容器12から液を回収できる
ようになっている。
A trypsin storage tank 42 for supplying trypsin for detaching cells from the perforated plate 20 after completion of the culture is connected to the outlet 16A of the rotating shaft 14 of the perforated plate unit 13. The trypsin storage tank 42 is also connected to the compressor 30 so that the liquid can be pressurized with sterile compressed air from the compressor 30 and sent to the sealed container 12. The outlet 16A has a product storage tank 4 for collecting cell products.
4. A waste storage tank 46 for collecting waste from cells is connected to the waste storage tank 46. These storage tanks 44 and 46 are connected to the vacuum pump 32 so that liquid can be collected from the sealed container 12 via the perforated plate 20.

尚、第1図上で48は無菌フィルタ、50は培養液供給用
及び細胞の老廃物取出し用の切換弁、第2図上で52はジ
ャケット25への温水供給口、54はジャケット25からの温
水排出口、56はモータ、58、60はプーリ、62はベルトで
ある。
In FIG. 1, reference numeral 48 denotes a sterile filter, reference numeral 50 denotes a switching valve for supplying a culture solution and removal of cell wastes, and reference numeral 52 denotes a hot water supply port to the jacket 25 in FIG. A hot water outlet, 56 is a motor, 58 and 60 are pulleys, and 62 is a belt.

次に、発明の細胞の培養装置による培養の一例とし
て、人繊維芽細胞によるインターフェロン(IFN)の生
産例を示す。
Next, an example of production of interferon (IFN) by human fibroblasts will be described as an example of culture of the cells of the present invention using a culture device.

まず、密閉容器12の流入口22から121℃以上の蒸気を
密閉容器12内に送り、密閉容器12内を20分間以上121℃
に保つことにより空減菌を行う。次に、操作は温水供給
口52から温水を供給して密閉容器12のジャケット25に温
水を循環させて密閉容器12を37℃に保存する。
First, steam of 121 ° C. or higher is sent from the inlet 22 of the closed container 12 into the closed container 12, and the inside of the closed container 12 is heated at 121 ° C. for 20 minutes or more.
Empty sterilization is performed by keeping at Next, the operation supplies warm water from the warm water supply port 52, circulates warm water through the jacket 25 of the closed container 12, and stores the closed container 12 at 37 ° C.

この状態で細胞を多孔板20、20…の表面に付着させ
る。表面への付着は、コンプレッサ30及び真空ポンプ32
を作動して細胞を種細胞槽34から密閉容器12内に満たす
と共に、濃度105個/mlに懸濁した培養液(仔ウシ血清5
%を加えたMES培地)を培養液貯留槽39から密閉容器12
内に満たした後、減菌し溶存酸素を飽和させた緩衝液
(PBS液)を0.5kgf/cm2に加圧して緩衝液貯留槽36から
流入口22を介して密閉容器12内に送り、多孔板20、20…
を介して培養液を回転軸14の貫通孔16から取り出すこと
によって行う。
In this state, the cells are attached to the surfaces of the perforated plates 20, 20,. The adhesion to the surface is achieved by the compressor 30 and the vacuum pump 32
Fulfills the sealed container 12 and the cells operated from seed cells tank 34, concentration 10 5 cells / ml were suspended in culture medium (fetal calf serum 5
% Of the MES medium) from the culture solution storage tank 39 to the closed container 12.
After filling the buffer, the sterilized and dissolved oxygen-saturated buffer solution (PBS solution) is pressurized to 0.5 kgf / cm 2 and sent from the buffer solution storage tank 36 to the closed container 12 via the inlet 22, Perforated plates 20, 20 ...
This is performed by taking out the culture solution from the through-hole 16 of the rotating shaft 14 through the above.

これにより、細胞は液とともに多孔板20、20…の方向
に流されるが、多孔板20、20…を透過することができな
いので、強制的に多孔板20、20…の表面に付着させられ
る。通常行われている浸漬のみによる細胞の付着時間が
4〜14時間を要するのに対し、本願発明のろ過を伴う方
法では約30分で付着が完了する。このため、雑菌汚染の
可能性を少なくすることができると共に細菌の付着率及
び生存率をほぼ100%にできる。
As a result, the cells flow in the direction of the perforated plates 20, 20,... Together with the liquid, but cannot permeate through the perforated plates 20, 20,. Whereas the time required for cell attachment by only immersion, which is normally performed, requires 4 to 14 hours, the method of the present invention involving filtration can be completed in about 30 minutes. For this reason, the possibility of bacterial contamination can be reduced, and the bacterial adhesion rate and survival rate can be made almost 100%.

次いで、栄養分と酸素を含む新鮮な培養液を供給し、
老廃物を含む培養液を取り出して多孔板20、20…に付着
した細胞を大量に増殖させる。この増殖は、密閉容器12
の流入口22から、0.01〜1.0kgf/cm2に加圧した新鮮な培
養液を圧入し、貫通孔16を大気圧または−0.05kgf/cm2
程度の減圧状態にして流出入口16Aを経て培養液を取り
出すことによって行う。この時、加圧された新鮮な培養
液は多孔板20の表面に付着した細胞に栄養分と酸素とを
与えると共に、細胞が代謝した老廃物を含んで多孔板20
の内面を通り貫通孔16から取り出される。このような老
廃物の除去を伴う培養方法で、数日後には多孔板20、20
…上に高密度の細胞が付着する。
Next, a fresh culture solution containing nutrients and oxygen is supplied,
The culture solution containing waste products is taken out, and the cells attached to the perforated plates 20, 20,. This growth occurs in closed containers 12
From the inlet 22, 0.01~1.0kgf / cm 2 pressurized fresh culture medium was pressed into the through hole 16 atmospheric pressure or -0.05kgf / cm 2
This is performed by taking out the culture solution through the outlet 16A under a reduced pressure. At this time, the pressurized fresh culture solution provides nutrients and oxygen to the cells adhering to the surface of the perforated plate 20 and contains waste products metabolized by the cells.
Is taken out of the through hole 16 through the inner surface of the hole. In a culture method involving the removal of such wastes, perforated plates 20, 20
… High-density cells adhere on top.

続いて、供給する培養液中にIFN誘導剤を加え、IFNの
生産を開始させる。IFNは、貫通孔16の流出入口16Aから
培養液とともに取り出される。
Subsequently, an IFN inducer is added to the culture solution to be supplied, and IFN production is started. IFN is taken out together with the culture solution from the outlet 16A of the through-hole 16.

次に、IFNの生産が完了した細胞を多孔板20、20…か
ら剥離して、多孔板20、20…を再使用する。これは、密
閉容器12内の培養液を緩衝液と交換した後、貫通孔16を
通じてトリプシン液を多孔板20、20…の内面から滲出さ
せて行うことができる。この方法によると、多孔板20、
20…に付着している細胞の付着面をトリプシンで直接処
理できるので、2分間で剥離が終了する。この時間はト
リプシン液中で攪拌するだけの従来の方法の約1/10に相
当する。
Next, the cells for which IFN production has been completed are detached from the perforated plates 20, 20,..., And the perforated plates 20, 20,. This can be performed by exchanging the culture solution in the sealed container 12 with a buffer solution, and then exuding the trypsin solution from the inner surfaces of the porous plates 20, 20,. According to this method, the perforated plate 20,
Since the attachment surface of the cells attached to 20 ... can be directly treated with trypsin, the detachment is completed in 2 minutes. This time corresponds to about 1/10 of the conventional method of only stirring in the trypsin solution.

また、この時モータ56を駆動して多孔板20、20…を回
転すると、さらに短時間で細胞を剥離することができ
る。剥離された細胞は、密閉容器12内を緩衝液で洗浄す
る時緩衝液とともに取り出し、一部は次回の培養の種細
胞として利用するため種細胞貯槽34に貯留する。
At this time, when the motor 56 is driven to rotate the perforated plates 20, 20,..., The cells can be detached in a shorter time. The detached cells are taken out together with the buffer when the inside of the closed container 12 is washed with the buffer, and a part thereof is stored in the seed cell storage tank for use as seed cells for the next culture.

細胞の排出後、多孔板20、20…を洗浄するために、密
閉容器12をアルカリ液(界面活性剤を含む0.5%の水酸
化ナトリウム溶液)で満たし、多孔板20、20…を100rpm
で約1時間回転させる。この操作によって、多孔板20、
20…は、その表面上の付着物や残留物を除去することが
できるので、繰り返し培養に使用できる。
After the cells have been discharged, in order to wash the perforated plates 20, 20,..., The closed container 12 is filled with an alkali solution (0.5% sodium hydroxide solution containing a surfactant), and the perforated plates 20, 20,.
And rotate for about 1 hour. By this operation, the perforated plate 20,
Since 20 ... can remove deposits and residues on the surface thereof, they can be used for repeated culture.

前記実施例では、培養中の酸素の供給方法として、酸
素を含む新鮮な培地を密閉容器12に供給したが、酸素を
大量に要求する細胞の場合には、次の方法で酸素を供給
することができる。まず、培養液の量を密閉容器12の約
1/2とし、多孔板20、20…の半分が液面からでるように
してから多孔板20、20…を30〜50rpmで回転させる。こ
の状態で流入口22から酸素を含む気体(5%炭酸ガスと
無菌空気など)を送ると、細胞への酸素の供給効率が大
幅に向上する。
In the above embodiment, as a method of supplying oxygen during the culture, a fresh medium containing oxygen was supplied to the closed container 12, but in the case of cells requiring a large amount of oxygen, oxygen is supplied by the following method. Can be. First, adjust the volume of the culture solution to approximately
The half-hole of the perforated plates 20, 20,... Is rotated from 30 to 50 rpm after the perforated plates 20, 20,. When a gas containing oxygen (such as 5% carbon dioxide and sterile air) is sent from the inflow port 22 in this state, the efficiency of supplying oxygen to the cells is greatly improved.

また、前記実施例では生産物の回収方法として、新鮮
な培養液を送って細胞が代謝した生産物を回収したが、
培養液に代えて安価な緩衝液を用いてもよい。
Further, in the above-described embodiment, as a method of recovering the product, a fresh culture solution was sent to recover the product in which the cells were metabolized.
An inexpensive buffer may be used instead of the culture solution.

更に、前記実施例では、多孔板ユニット13の回転軸14
が一軸の場合について説明したが、これに限らず、培養
容量を大きくする場合には、第4図に示すように回転軸
を二軸使用して多孔板ユニットを二セット使用してもよ
い。この場合の細胞の培養装置の全体図を第5図に示
す。尚、第5図上で60は密閉容器であり、第4図、第5
図において前記実施例と同一部材については同一符号を
付して説明を省略する。
Further, in the above embodiment, the rotating shaft 14 of the perforated plate unit 13
However, the present invention is not limited to this, and in the case of increasing the culture volume, two sets of perforated plate units may be used using two rotating shafts as shown in FIG. FIG. 5 shows an overall view of the cell culture apparatus in this case. In FIG. 5, reference numeral 60 denotes a closed container.
In the drawing, the same members as those in the above-described embodiment are denoted by the same reference numerals, and description thereof is omitted.

第4図に示す実施例では、二セットの多孔板ユニット
の多孔板を隣接していないで設けたが、二セットの多孔
板同士がかみ合うように設けてもよい。尚、多孔板ユニ
ットは二セットに限らず複数セット設けてもよい。
In the embodiment shown in FIG. 4, the perforated plates of the two sets of perforated plate units are provided so as not to be adjacent to each other, but may be provided so that the two sets of perforated plates are engaged with each other. Note that the number of perforated plate units is not limited to two, and a plurality of sets may be provided.

〔発明の効果〕〔The invention's effect〕

本発明に係る培養方法及びその装置によれば、の濾過
体の多孔板の全域で細胞と培養液を均一に分離できるの
で、多孔板に付着した細胞に培養液に含まれている栄養
分及び酸素を均一に供給することができる。従って、大
量の細胞を高密度に培養できるので効率のよい生産を行
うことができる。
According to the culture method and the apparatus according to the present invention, the cells and the culture solution can be uniformly separated over the entire area of the perforated plate of the filter, so that the nutrients and oxygen contained in the culture solution in the cells attached to the perforated plate Can be supplied uniformly. Therefore, a large amount of cells can be cultured at a high density, so that efficient production can be performed.

また、細胞懸濁液を濾過することによって、培養開始
前に濾過体の多孔板に細胞を短時間でかつ確実に付着さ
せられることができる。
Further, by filtering the cell suspension, the cells can be reliably and quickly attached to the porous plate of the filter before the start of the culture.

更に、培養終了後に容易に細胞を濾過体の多孔板から
剥離させることができるので多孔板の再生が可能であ
る。
Furthermore, since the cells can be easily detached from the perforated plate of the filter after completion of the culture, the perforated plate can be regenerated.

また、濾過体の多孔板を孔径の大きな多孔質の支持体
の外周上に孔径の小さな多孔質の層を設けた多層構造に
することによって、多孔板の表面のいずれの場所からも
均一に培養液の供給及び取り出して行うことができ、更
に、細胞を容易に付着することができる。
In addition, by forming the porous plate of the filter into a multilayer structure in which a porous layer having a small pore size is provided on the outer periphery of a porous support having a large pore size, culture can be performed uniformly from any location on the surface of the porous plate. The solution can be supplied and taken out, and the cells can be easily attached.

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

第1図は本発明に係る細胞の培養装置を示す全体図、第
2図は多孔板ユニットの構造を示す断面図、第3図は多
孔板の拡大図、第4図は本発明に係る細胞の培養装置の
他の実施例に使用される多孔板ユニットの断面図、第5
図は第4図の多孔板ユニットが使用された細胞の培養装
置。 10……細胞の培養装置、12、60……密閉容器、 14……回転軸、16……貫通孔、 22……流入口、30……圧縮器、 32……真空ポンプ、34……種細胞貯送、 39……培養液貯槽。
1 is an overall view showing a cell culture apparatus according to the present invention, FIG. 2 is a cross-sectional view showing the structure of a perforated plate unit, FIG. 3 is an enlarged view of a perforated plate, and FIG. Sectional view of a perforated plate unit used in another embodiment of the culture apparatus of FIG.
The figure shows a cell culture device using the perforated plate unit of FIG. 10 …………………………………………………………………………………………………………………………………………………. Cell storage, 39 …… Culture storage tank.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 鈴木 茂美 神奈川県茅ケ崎市本村2丁目8番1号 東陶機器株式会社茅ヶ崎工場内 (72)発明者 山野 繁 神奈川県茅ケ崎市本村2丁目8番1号 東陶機器株式会社茅ヶ崎工場内 (72)発明者 前橋 信之 神奈川県茅ケ崎市本村2丁目8番1号 東陶機器株式会社茅ヶ崎工場内 (56)参考文献 特開 昭60−98981(JP,A) 特開 平2−200176(JP,A) (58)調査した分野(Int.Cl.7,DB名) C12M 1/00 - 3/08 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Shigemi Suzuki 2-81-1, Honmura, Chigasaki-shi, Kanagawa Prefecture Tochiki Kiki Co., Ltd. Chigasaki Plant (72) Inventor Shigeru Yamano 2-81-1, Honmura, Chigasaki-shi, Kanagawa Prefecture No. 72 in Toga Equipment Co., Ltd. Chigasaki Factory (72) Inventor Nobuyuki Maebashi 2-8-1, Honmura Chigasaki-shi, Kanagawa Prefecture Totoki Equipment Co., Ltd. Chigasaki Factory (56) References JP-A-60-99881 (JP, A JP, 2-200176 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) C12M 1/00-3/08

Claims (8)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】表面に細胞が付着する複数枚の多孔板と、
該複数枚の多孔板が所定間隔で並設されるとともに多孔
板の表面と連通する貫通孔を有する回転自在な支軸とか
ら成る濾過体と、 前記濾過体を収納するとともに該濾過体の支軸を支持す
る密閉容器と、 培養液を含む1乃至複数の流体を前記密閉容器に加圧状
態で供給する手段と、 を備えたことを特徴とする細胞の培養装置。
1. A plurality of perforated plates to which cells adhere to the surface,
A filter body comprising a plurality of perforated plates arranged side by side at predetermined intervals and a rotatable support shaft having a through hole communicating with the surface of the perforated plate; and a filter housing for accommodating the filter body and supporting the filter body. An apparatus for culturing cells, comprising: a sealed container that supports a shaft; and a unit that supplies one or more fluids including a culture solution to the sealed container in a pressurized state.
【請求項2】前記濾過体の支軸の貫通孔に、前記多孔板
から細胞を剥離させるための流体を加圧状態で供給する
手段を備えたことを特徴とする請求項(1)記載の細胞
の培養装置。
2. The method according to claim 1, further comprising: a means for supplying a fluid for separating cells from the perforated plate in a pressurized state in a through hole of a support shaft of the filter. Cell culture equipment.
【請求項3】濾過体の多孔板を、孔径10μm〜100μm
の多孔質の支持体の外周上に、孔径0.01μm〜5μmの
多孔質の層を設けて多層構造としたことを特徴とする請
求項(1)又は(2)記載の細胞の培養装置。
3. The porous plate of the filter has a pore size of 10 μm to 100 μm.
The cell culture device according to claim 1 or 2, wherein a porous layer having a pore size of 0.01 µm to 5 µm is provided on the outer periphery of the porous support to form a multilayer structure.
【請求項4】貫通孔を有する支軸に細胞を付着させる複
数の多孔板を、支軸内の貫通孔に連通するように装着し
て成る濾過体を、密閉容器内に設置した培養装置を用
い、培養液を加圧状態にして密閉容器に供給すると共
に、支軸内の貫通孔を大気圧又は減圧状態にし老廃物を
含む培養液を多孔板及び貫通孔を介して取り出すことを
特徴とする細胞の培養方法。
4. A culturing apparatus in which a filter provided by mounting a plurality of perforated plates for attaching cells to a spindle having a through hole so as to communicate with the through hole in the spindle is provided in a closed container. Using, while supplying the culture solution to the closed container in a pressurized state, the through-hole in the support shaft is set to atmospheric pressure or reduced pressure, and the culture solution containing waste products is taken out through the perforated plate and the through-hole. Cell culture method.
【請求項5】密閉容器内に種細胞懸濁液を供給して多孔
板の半分又は全体を種細胞懸濁液中に浸漬した後、密閉
容器内を加圧して種細胞懸濁液を多孔板で濾過して多孔
板に細胞を付着させることを特徴とする請求項(4)記
載の細胞の培養方法。
5. A seed cell suspension is supplied into a closed container, and half or all of the perforated plate is immersed in the seed cell suspension. 5. The method for culturing cells according to claim 4, wherein the cells are filtered and the cells are attached to a perforated plate.
【請求項6】密閉容器内に培養液を供給して多孔板の一
部を培養液に浸漬し、密閉容器内に圧縮空気を供給して
多孔板を酸素を含む無菌の気体に接触させ、多孔板を回
転させて細胞に酸素を供給することを特徴とする請求項
(4)又は(5)記載の細胞の培養方法。
6. A culture solution is supplied into a closed container, a part of the perforated plate is immersed in the culture solution, and compressed air is supplied into the closed container to contact the perforated plate with a sterile gas containing oxygen. The method for culturing cells according to claim 4 or 5, wherein oxygen is supplied to the cells by rotating the perforated plate.
【請求項7】新鮮な培養液又は緩衝液を加圧して密閉容
器内に供給した後、誘導剤を加圧して密閉容器内に供給
し、生産された生産物を含む培養液を多孔板及び貫通孔
を介して取り出すことを特徴とする請求項(4)、
(5)又は(6)記載の細胞の培養方法。
7. A fresh culture solution or buffer solution is pressurized and supplied into the closed container, and then the inducer is pressurized and supplied into the closed container, and the culture solution containing the produced product is supplied to the perforated plate and (4) The liquid is taken out through the through hole.
The method for culturing cells according to (5) or (6).
【請求項8】貫通孔を介して多孔板から剥離用の液体を
滲出させて多孔板に付着した細胞を多孔板から剥離する
ことを特徴とする請求項(4)、(5)、(6)又は
(7)記載の細胞の培養方法。
8. The cell according to claim 4, wherein the liquid for exfoliation is leached from the perforated plate through the through-hole, and the cells attached to the perforated plate are separated from the perforated plate. ) Or (7).
JP2246638A 1990-09-17 1990-09-17 Cell culturing method and device Expired - Fee Related JP3036032B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2246638A JP3036032B2 (en) 1990-09-17 1990-09-17 Cell culturing method and device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2246638A JP3036032B2 (en) 1990-09-17 1990-09-17 Cell culturing method and device

Publications (2)

Publication Number Publication Date
JPH04126068A JPH04126068A (en) 1992-04-27
JP3036032B2 true JP3036032B2 (en) 2000-04-24

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Publication number Priority date Publication date Assignee Title
WO2001021760A2 (en) * 1999-09-24 2001-03-29 Cell Science Therapeutics, Inc. Cell culture spinner flasks
DE10016554A1 (en) * 2000-04-03 2001-10-18 Rootec Ges Fuer Bioaktive Wirk Plant or animal tissue cultivation unit, comprises fermenter container, supply for liquid nutrients and gases, discharger for used nutrients, and carrier plates
JP4230176B2 (en) * 2002-06-28 2009-02-25 独立行政法人科学技術振興機構 Embryo culture apparatus and method for controlling embryo asymmetry
WO2005052136A1 (en) * 2003-11-28 2005-06-09 Ares Trading S.A. Process for recycling solid supports for cultivation of anchorage-dependent cells
JP5666131B2 (en) * 2008-02-22 2015-02-12 コバレントマテリアル株式会社 Cell culture module
JP2010081823A (en) * 2008-09-30 2010-04-15 Covalent Materials Corp Apparatus for cell culture
US9657266B2 (en) 2011-04-15 2017-05-23 Pluristem Ltd. Methods and systems for harvesting cells
DK3430119T3 (en) * 2016-03-14 2023-09-18 Omnibrx Biotechnologies Private Ltd A BIOREACTOR SYSTEM AND ITS OPERATION

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