JPH0576344A - Floating cell culture method and culture device - Google Patents
Floating cell culture method and culture deviceInfo
- Publication number
- JPH0576344A JPH0576344A JP24189691A JP24189691A JPH0576344A JP H0576344 A JPH0576344 A JP H0576344A JP 24189691 A JP24189691 A JP 24189691A JP 24189691 A JP24189691 A JP 24189691A JP H0576344 A JPH0576344 A JP H0576344A
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- culture
- culture tank
- cells
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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
- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/02—Stirrer or mobile mixing elements
-
- 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
-
- 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
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/06—Nozzles; Sprayers; Spargers; Diffusers
-
- 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
- C12M33/00—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus
- C12M33/10—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus by centrifugation ; Cyclones
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- Health & Medical Sciences (AREA)
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- Chemical & Material Sciences (AREA)
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- Sustainable Development (AREA)
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- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Biotechnology (AREA)
- Molecular Biology (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
(57)【要約】
【構成】培養室6の上部は蓋7でシールされ、中央部の
シール用キャップ21により、蓋7を貫通する上清抜き
出し配管11,酸素含有ガス供給配管14,酸素含有ガ
ス排気配管16,D0電極17及びpH電極19が固定
され、培養槽1中に位置している。上清抜き出し配管1
1の下端部分には撹拌翼22の一端を接続し、翼22の
先端を配管11の下端を支点にして垂直方向に自在に上
下して、翼の開閉可能にしている。
【効果】ロータを培養槽にすることにより、容積効率を
従来の大スケールに比べ大幅に向上できるため、小スケ
ールでの灌流培養が可能になる。
(57) [Summary] [Structure] The upper part of the culture chamber 6 is sealed by a lid 7, and a sealing cap 21 at the central portion allows a supernatant extraction pipe 11 penetrating the lid 7, an oxygen-containing gas supply pipe 14, an oxygen-containing pipe. The gas exhaust pipe 16, the D0 electrode 17, and the pH electrode 19 are fixed and located in the culture tank 1. Supernatant extraction pipe 1
One end of a stirring blade 22 is connected to the lower end portion of the blade 1, and the tip of the blade 22 is freely moved up and down in the vertical direction with the lower end of the pipe 11 as a fulcrum so that the blade can be opened and closed. [Effect] By using the rotor as a culture tank, the volumetric efficiency can be greatly improved compared to the conventional large scale, and thus perfusion culture can be performed on a small scale.
Description
【0001】[0001]
【産業上の利用分野】本発明は浮遊性生物細胞の培養方
法及び培養装置に係り、特に、浮遊性動物細胞の小規模
培養に適する灌流培養方法及び灌流培養装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and apparatus for culturing buoyant organism cells, and more particularly to a perfusion culture method and a perfusion culture apparatus suitable for small-scale culturing of buoyant animal cells.
【0002】[0002]
【従来の技術】浮遊性細胞、特に、浮遊性動物細胞の高
密度灌流培養は、蛋白性の生理活性物質を生産するため
の基幹技術となりつつある。中でも遠心分離式の灌流培
養方法は耐久性が高く長期間の培養に耐え、灌流速度を
高く取れるため有望視されている。公知の技術として
は、例えば、特願昭63−143466号,特願昭63−282544号
明細書があげられる。これら従来の方式及び培養装置は
培養槽内の培養液を槽外に抜き出して、動物細胞用に工
夫した遠心分離装置により培地交換を行うものである。
かつ、遠心分離の際、細胞を高速回転面と接触して損傷
しないようにするため、撹拌翼を軸管ごとロータ外に引
き出すか、ロータと同期回転する必要があるため、堅牢
かつ複雑な機構にならざる得なかった。2. Description of the Related Art High-density perfusion culture of free-floating cells, especially free-flowing animal cells, is becoming a key technology for producing proteinaceous physiologically active substances. Among them, the centrifugal type perfusion culture method is considered to be promising because it has high durability, can endure long-term culture, and can achieve high perfusion rate. Known techniques include, for example, Japanese Patent Application Nos. 63-143466 and 63-282544. In these conventional methods and culture devices, the culture solution in the culture tank is extracted to the outside of the tank, and the medium is replaced by a centrifugal separator devised for animal cells.
In addition, in order to prevent the cells from coming into contact with the high-speed rotating surface and being damaged during centrifugation, it is necessary to pull the stirring blade out of the rotor together with the shaft tube or rotate it in synchronization with the rotor, so a robust and complicated mechanism There was no choice but to become.
【0003】しかるに、本培養の前に行う種培養や生産
物検索の段階で行う培養でも1リットル前後での小スケ
ールでの灌流培養が必要となってきている。しかし、上
述の公知技術では、そのままスケールダウンすることは
極めて困難であり、1リットル以下のスケールで長期間
の灌流培養に耐える培養装置は知られていない。However, perfusion culture on a small scale of about 1 liter is also required for seed culture before main culture and culture at the stage of product search. However, it is extremely difficult to scale down as it is by the above-mentioned known technique, and a culture device that can withstand a long-term perfusion culture at a scale of 1 liter or less is not known.
【0004】[0004]
【発明が解決しようとする課題】本発明の目的は、1リ
ットル以下の小スケールでも数ケ月の長期にわたり灌流
培養を可能とする方法及びシステムを提供するにある。
そのためには、装置の機能をそこなわずコンパクト化す
るプロセス及び構造の工夫が必要となる。SUMMARY OF THE INVENTION It is an object of the present invention to provide a method and system that enables perfusion culture for a long period of several months even on a small scale of 1 liter or less.
For that purpose, it is necessary to devise a process and a structure that make the function of the device compact without detracting from it.
【0005】[0005]
【課題を解決するための手段】発明者らはコンパクト化
に必要な原理につき、鋭意検討した結果遠心分離機のロ
ータを培養槽とする発想の転換により本発明に到達し
た。Means for Solving the Problems The inventors of the present invention have earnestly studied the principle required for compactification, and as a result, arrived at the present invention by changing the way of thinking that the rotor of a centrifuge is a culture tank.
【0006】本発明の第一の特徴は下記工程からなるプ
ロセスにある。The first feature of the present invention is a process including the following steps.
【0007】すなわち、(1)水平に回転自在な培養槽
に培地と種細胞とを導入し、(2)回転中心軸線上に固
定した酸素供給手段と、翼基部が固定され、基部から翼
端にかけて液面を上下する翼を液面以下に位置した状態
で、培養槽を実質的に細胞が沈降しない低い回転速度で
回転することにより、液の撹拌と酸素の溶解を所定の期
間行い、(3)回転翼面を液面に引きあげて、細胞が遠
心沈降するに足る回転速度で培養槽を回転して細胞を培
養槽内側面に沈着するまで回転した後、回転を停止し、
(4)遠心分離で生じた上清を、培養槽底に開口部を近
接し、かつ回転軸線上に固定配置した液移送配管を経由
して系外に抜き出し、(5)翼端にさげた状態で低速回
転しつつ、培養槽内側壁の上方から培地を放射して沈着
している細胞を培地に分散させ、(6)前記(2)の工
程に戻り、以後(2)〜(6)のサイクルを繰り返す。That is, (1) the medium and seed cells are introduced into a horizontally rotatable culture tank, and (2) the oxygen supply means fixed on the central axis of rotation and the blade base are fixed, and the base to the blade tip is fixed. With the blades moving above and below the liquid surface positioned below the liquid surface, the culture tank is rotated at a low rotation speed at which cells do not substantially settle, thereby stirring the liquid and dissolving oxygen for a predetermined period of time. 3) Pulling the rotor surface to the liquid surface, rotating the culture tank at a rotation speed sufficient for the cells to be centrifugally sedimented, rotating until the cells are deposited on the inner surface of the culture tank, and then stopping the rotation,
(4) The supernatant generated by centrifugation was extracted to the outside of the system via a liquid transfer pipe having an opening close to the bottom of the culture tank and fixedly arranged on the rotation axis, and (5) provided at the blade tip. While rotating at a low speed in the state, the culture medium is radiated from above the inner wall of the culture tank to disperse the deposited cells in the culture medium, and (6) the process returns to the step (2), and thereafter (2) to (6). Repeat the cycle.
【0008】さらに、本プロセスの概略を図示した図1
によりさらに詳しく説明する。ロータの機能をもつ培養
槽1は、培養時に於いて、上清抜き出し配管10の下端
に基部をもち翼端を上下できる撹拌翼2を配置し、翼2
を開した状態で、培養槽1を回転することにより培養液
4が混合される。この間、酸素含有ガスを酸素供給配管
8から配管10に固定した酸素透過性中空糸膜12に導
入して、培養液4に酸素を溶解する。培地の交換が必要
となった時点で、撹拌翼2の翼端を上方にあげ、培養槽
1を遠心分離に足る回転数で回転し、細胞5を槽内壁に
沈降させる。次いで上清6は配管10から抜き出す。次
に培地供給配管11より培地を放射して、槽内壁に付着
した細胞を培地に懸濁分散する。このとき培養槽1は翼
2を開いた状態で低速で回転する。Further, FIG. 1 schematically shows the present process.
Will be described in more detail. In the culture tank 1 having the function of a rotor, a stirring blade 2 having a base portion and capable of moving the blade tip up and down is arranged at the lower end of the supernatant withdrawing pipe 10 at the time of culture.
The culture solution 4 is mixed by rotating the culture tank 1 in the state of opening. During this time, an oxygen-containing gas is introduced from the oxygen supply pipe 8 into the oxygen-permeable hollow fiber membrane 12 fixed to the pipe 10 to dissolve oxygen in the culture solution 4. When the medium needs to be exchanged, the blade tip of the stirring blade 2 is raised and the culture tank 1 is rotated at a rotation speed sufficient for centrifugation to settle the cells 5 on the inner wall of the tank. Then, the supernatant 6 is extracted from the pipe 10. Next, the medium is radiated from the medium supply pipe 11 to suspend and disperse the cells attached to the inner wall of the tank in the medium. At this time, the culture tank 1 rotates at a low speed with the wings 2 open.
【0009】本発明に適用できる細胞は浮遊性であれば
特に限定されないが、浮遊性動物細胞、例えば、各種の
ハイブリドーマ,癌細胞,リンパ球細胞等に好適であ
る。The cells applicable to the present invention are not particularly limited as long as they are buoyant, but are preferably buoyant animal cells such as various hybridomas, cancer cells, lymphocyte cells and the like.
【0010】[0010]
【作用】遠心分離機のロータを培養槽とすることによ
り、灌流培養が可能となり、容積効率を大幅に向上でき
る。By using the rotor of the centrifuge as a culture tank, perfusion culture becomes possible, and the volumetric efficiency can be greatly improved.
【0011】[0011]
【実施例】次に、本発明なる実施例を示し、さらに詳し
く説明する。EXAMPLES Next, examples of the present invention will be shown and described in more detail.
【0012】〈実施例1〉図2に、本発明なる培養装置
の中核部分の断面を示す。水平に自在回転可能な培養槽
1は低部に回転力伝達用のマグネット2をもち、上下と
もベアリング4及び支持アーム5で支持され耐圧性の培
養室6に収納されている。培養室6の底外にはマグネッ
ト2を付したモータ3を配置し、培養槽を回転させう
る。培養室6の上部は蓋7でシールされ、中央部のシー
ル用キャップ21により、蓋7を貫通する上清抜き出し
配管11,酸素含有ガス供給配管14,酸素含有ガス排
気配管16,D0電極17及びpH電極19が固定さ
れ、培養槽1中に位置している。上清抜き出し配管11
の下端部分には撹拌翼22の一端を接続し、翼22の先
端を配管11の下端を支点にして垂直方向に自在に上下
して、翼の開閉可能にしている。Example 1 FIG. 2 shows a cross section of the core portion of the culture apparatus according to the present invention. The culture tank 1 which can be freely rotated horizontally has a magnet 2 for transmitting a rotational force at its lower portion, and is supported by a bearing 4 and a support arm 5 at the top and bottom and is housed in a pressure-resistant culture chamber 6. A motor 3 provided with a magnet 2 may be arranged outside the bottom of the culture chamber 6 to rotate the culture tank. The upper part of the culture chamber 6 is sealed with a lid 7, and a supernatant removal pipe 11 penetrating the lid 7, an oxygen-containing gas supply pipe 14, an oxygen-containing gas exhaust pipe 16, a D0 electrode 17, and a sealing cap 21 at the central portion. The pH electrode 19 is fixed and located in the culture tank 1. Supernatant extraction pipe 11
One end of the stirring blade 22 is connected to the lower end of the blade, and the tip of the blade 22 is freely moved up and down in the vertical direction with the lower end of the pipe 11 as a fulcrum to open and close the blade.
【0013】翼の支点より若干翼端方向に索線を配線
し、ソレノイド23及び作動用伝達索24により、翼2
2を開閉する。また、上清抜き出し配管11には酸素透
過性中空系6aを固定し、酸素含有ガス13を導入する
ことにより、培養槽内の培養液中に酸素を供給する。培
養中は翼22を開いた状態で培養槽1を低速で回転して
培養槽内を撹拌し、D0及びpHを各電極で検出し、各
設定範囲にコントロール可能である。遠心分離時には、
翼22を上方にあげ、液面から遊離するようにし、培養
槽を800〜2000rpm (1000G以下)に回転す
る。細胞を培地に懸濁する際には、培地供給配管27よ
り槽内側面に放射される。符号25はドレイン排出配管
である。A cable line is laid slightly toward the tip of the wing from the fulcrum of the wing, and a wing 2 is formed by a solenoid 23 and an operation transmission line 24.
Open and close 2. In addition, the oxygen permeable hollow system 6a is fixed to the supernatant extraction pipe 11 and the oxygen-containing gas 13 is introduced to supply oxygen into the culture solution in the culture tank. During the culture, the culture tank 1 is rotated at a low speed with the blades 22 open to stir the inside of the culture tank, and D0 and pH are detected by the respective electrodes, and it is possible to control within each set range. During centrifugation,
Raise the blades 22 upward so that they are separated from the liquid surface, and rotate the culture tank at 800 to 2000 rpm (1000 G or less). When the cells are suspended in the medium, they are emitted from the medium supply pipe 27 to the inner surface of the tank. Reference numeral 25 is a drain discharge pipe.
【0014】〈実施例2〉図3に培養槽単槽時の培養シ
ステムの例を示す。Example 2 FIG. 3 shows an example of a culture system in a single culture tank.
【0015】培養槽1への培地18の供給はホンプ1
2,上清16の抜き出しはポンプ13により行われる。
酸素含有ガスは配管7により酸素透過性中空糸膜6に供
給される。ガス供給及びポンプ作動,撹拌翼5の開閉は
D0/pHコントローラ15並びにプロセスシーケンサ
14により行われる。The medium 18 is supplied to the culture tank 1 by the horn 1.
2. The pump 13 extracts the supernatant 16.
The oxygen-containing gas is supplied to the oxygen-permeable hollow fiber membrane 6 through the pipe 7. The gas supply, the pump operation, and the opening / closing of the stirring blade 5 are performed by the D0 / pH controller 15 and the process sequencer 14.
【0016】9は上清、10は上清抜き出し配管、11
は培地、12は培地供給配管、13は酸素含有ガス給
気、14は酸素含有ガス給気配管、15は酸素含有ガス
廃気、16は酸素含有ガス廃気配管、17はpH電極、
18はpH電極信号配線、19はD0電極、20はモー
タ配線、21は培養室である。9 is a supernatant, 10 is a pipe for extracting the supernatant, 11
Is a medium, 12 is a medium supply pipe, 13 is an oxygen-containing gas supply pipe, 14 is an oxygen-containing gas supply pipe, 15 is an oxygen-containing gas waste gas, 16 is an oxygen-containing gas waste gas pipe, 17 is a pH electrode,
Reference numeral 18 is a pH electrode signal wiring, 19 is a D0 electrode, 20 is a motor wiring, and 21 is a culture chamber.
【0017】〈実施例3〉図4に複数槽の時の培養シス
テムの例を示す。上清抜き出し配管11,培地供給配管
10,ガス供給配管7は各槽毎の開閉バルブを操作して
集合化できる。<Embodiment 3> FIG. 4 shows an example of a culture system having a plurality of tanks. The supernatant extraction pipe 11, the medium supply pipe 10, and the gas supply pipe 7 can be assembled by operating the opening / closing valve for each tank.
【0018】[0018]
【発明の効果】本発明によればロータ培養槽にすること
により、容積効率を従来の大スケールに比べ大幅に向上
できるため、小スケールでの灌流培養が可能になる。According to the present invention, since the rotor culture tank is used, the volumetric efficiency can be greatly improved as compared with the conventional large scale, so that the perfusion culture can be performed on the small scale.
【図1】本発明のプロセス原理の説明図。FIG. 1 is an explanatory diagram of a process principle of the present invention.
【図2】本発明の培養装置の要部の断面図。FIG. 2 is a sectional view of a main part of the culture device of the present invention.
【図3】本発明の培養槽が単槽である場合の培養システ
ムのフローチャート。FIG. 3 is a flowchart of a culture system in which the culture tank of the present invention is a single tank.
【図4】本発明の培養槽が複数である場合の培養システ
ムのフローチャート。FIG. 4 is a flowchart of a culture system of the present invention when there are a plurality of culture tanks.
1…培養槽、2…マグネット、3…モータ、4…ベアリ
ング、5…支持アーム、6…培養室、22…撹拌翼。1 ... Culture tank, 2 ... Magnet, 3 ... Motor, 4 ... Bearing, 5 ... Support arm, 6 ... Culture chamber, 22 ... Stirring blade.
Claims (2)
細胞の培養方法。 (1)水平に回転自在な培養槽に培地と種細胞とを導入
し、 (2)回転中心軸線上に固定した酸素供給手段と、翼基
部が固定され、基部から翼端にかけて液面を上下する翼
を液面以下に位置した状態で、前記培養槽を実質的に細
胞が遠心沈降しない低い回転速度で回転することによ
り、液の撹拌と酸素の溶解を所定の期間行い、 (3)前記回転翼を液面に引きあげて、細胞が遠心沈降
するに足る回転速度で前記培養槽を回転して細胞を前記
培養槽内の側面に沈着するまで回転した後、回転を停止
し、 (4)遠心分離で生じた上清を、該培養槽底に開口部を
近接し、かつ回転軸線上に固定配置した液移送配管を経
由して系外に抜き出し、 (5)該翼端をさげた状態で低速回転しつつ、該培養槽
内側壁の上方から培地を放射して沈着している細胞を培
地に分散させ、 (6)(2)の工程に戻り、以後(2)〜(6)のサイ
クルを繰り返す。1. A method for culturing floating cells, which comprises the following steps. (1) The medium and seed cells are introduced into a horizontally rotatable culture tank, (2) the oxygen supply means fixed on the central axis of rotation, and the blade base are fixed, and the liquid level is raised and lowered from the base to the blade tip. (3) The stirring of the liquid and the dissolution of oxygen are performed for a predetermined period of time by rotating the culture tank at a low rotation speed at which cells are not settled by centrifugal sedimentation with the impeller positioned below the liquid surface. The rotor is pulled up to the liquid surface, and the culture tank is rotated at a rotation speed sufficient for centrifugal sedimentation of the cells to rotate the cells until they are deposited on the side surface in the culture tank, and then the rotation is stopped, (4) The supernatant produced by centrifugation is withdrawn to the outside of the system via a liquid transfer pipe having an opening close to the bottom of the culture tank and fixedly arranged on the rotation axis, and (5) a state in which the blade tip is lowered. While rotating at low speed, the culture medium is radiated from above the inner wall of the culture tank and deposited. The cells are dispersed in the medium, the process returns to (6) and (2), and then the cycles (2) to (6) are repeated.
細胞の培養装置。 (1)水平に回転可能なボール型培養槽の回転軸線上
に、培養槽の中心底面に近接した開口部をもち、回転軸
線上に液移送配管をもつ。 (2)前記液移送配管に酸素供給手段をもち、 (3)前記液移送配管の上下に基部を固定し、前記基部
を基点にして端部の上下を可能とする撹拌翼をもつ。2. A culturing device for floating cells, which has the following structure. (1) A horizontally rotatable ball-type culture tank has an opening near the center bottom surface of the culture tank on the axis of rotation and a liquid transfer pipe on the axis of rotation. (2) An oxygen supply means is provided in the liquid transfer pipe, and (3) a base is fixed on the upper and lower sides of the liquid transfer pipe, and a stirring blade is provided which allows the end part to be moved up and down with the base as a base point.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24189691A JPH0576344A (en) | 1991-09-20 | 1991-09-20 | Floating cell culture method and culture device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24189691A JPH0576344A (en) | 1991-09-20 | 1991-09-20 | Floating cell culture method and culture device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0576344A true JPH0576344A (en) | 1993-03-30 |
Family
ID=17081169
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24189691A Pending JPH0576344A (en) | 1991-09-20 | 1991-09-20 | Floating cell culture method and culture device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0576344A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6451961B2 (en) | 2000-02-03 | 2002-09-17 | Nippon Shokubai Co Ltd | Ethylenimine polymer, aqueous solution of ethylenimine polymer, production process for the same and purifying process therefor |
| CN105713825A (en) * | 2016-03-31 | 2016-06-29 | 上海拜高乐生物技术有限公司 | Cell sedimentation type liquid extraction device for cell suspension culture |
| WO2017141394A1 (en) * | 2016-02-18 | 2017-08-24 | エイブル株式会社 | Reaction device capable of performing centrifugation |
| WO2020138506A1 (en) * | 2018-12-27 | 2020-07-02 | エイブル株式会社 | Perfusion culture apparatus and centrifugal separator |
-
1991
- 1991-09-20 JP JP24189691A patent/JPH0576344A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6451961B2 (en) | 2000-02-03 | 2002-09-17 | Nippon Shokubai Co Ltd | Ethylenimine polymer, aqueous solution of ethylenimine polymer, production process for the same and purifying process therefor |
| WO2017141394A1 (en) * | 2016-02-18 | 2017-08-24 | エイブル株式会社 | Reaction device capable of performing centrifugation |
| CN105713825A (en) * | 2016-03-31 | 2016-06-29 | 上海拜高乐生物技术有限公司 | Cell sedimentation type liquid extraction device for cell suspension culture |
| WO2020138506A1 (en) * | 2018-12-27 | 2020-07-02 | エイブル株式会社 | Perfusion culture apparatus and centrifugal separator |
| JP2020103262A (en) * | 2018-12-27 | 2020-07-09 | エイブル株式会社 | Perfusion culture device and centrifuge |
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