JPH0269176A - Cell culture apparatus - Google Patents
Cell culture apparatusInfo
- Publication number
- JPH0269176A JPH0269176A JP22169588A JP22169588A JPH0269176A JP H0269176 A JPH0269176 A JP H0269176A JP 22169588 A JP22169588 A JP 22169588A JP 22169588 A JP22169588 A JP 22169588A JP H0269176 A JPH0269176 A JP H0269176A
- Authority
- JP
- Japan
- Prior art keywords
- culture
- stirring
- tank
- culture tank
- culture solution
- 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.)
- Granted
Links
- 238000004113 cell culture Methods 0.000 title claims abstract description 18
- 238000003756 stirring Methods 0.000 claims abstract description 58
- 239000007789 gas Substances 0.000 abstract description 13
- 239000001963 growth medium Substances 0.000 abstract description 13
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 10
- 239000001301 oxygen Substances 0.000 abstract description 10
- 229910052760 oxygen Inorganic materials 0.000 abstract description 10
- 238000012258 culturing Methods 0.000 abstract description 7
- 239000002699 waste material Substances 0.000 abstract description 6
- 239000007788 liquid Substances 0.000 abstract description 5
- 230000001174 ascending effect Effects 0.000 abstract 1
- 230000008878 coupling Effects 0.000 abstract 1
- 238000010168 coupling process Methods 0.000 abstract 1
- 238000005859 coupling reaction Methods 0.000 abstract 1
- 210000004027 cell Anatomy 0.000 description 34
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 10
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 7
- 229910001882 dioxygen Inorganic materials 0.000 description 7
- 235000015097 nutrients Nutrition 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 5
- 229910002092 carbon dioxide Inorganic materials 0.000 description 5
- 229910001873 dinitrogen Inorganic materials 0.000 description 5
- 239000001569 carbon dioxide Substances 0.000 description 4
- 239000003463 adsorbent Substances 0.000 description 3
- 210000004102 animal cell Anatomy 0.000 description 3
- 208000003251 Pruritus Diseases 0.000 description 2
- 239000000969 carrier Substances 0.000 description 2
- PQNFLJBBNBOBRQ-UHFFFAOYSA-N indane Chemical compound C1=CC=C2CCCC2=C1 PQNFLJBBNBOBRQ-UHFFFAOYSA-N 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000011859 microparticle Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 235000016623 Fragaria vesca Nutrition 0.000 description 1
- 240000009088 Fragaria x ananassa Species 0.000 description 1
- 235000011363 Fragaria x ananassa Nutrition 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 210000000170 cell membrane Anatomy 0.000 description 1
- 230000004663 cell proliferation Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000012531 culture fluid Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 230000007803 itching Effects 0.000 description 1
- 210000003126 m-cell Anatomy 0.000 description 1
- 239000002609 medium Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 229920002050 silicone resin Polymers 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、培養槽内の培養液(培地)を撹拌して細胞を
培養液内に分散させながら培養を行う細胞培養装置に関
し、特に動植物細胞の培養に適した細胞培養装置に関す
るものである。Detailed Description of the Invention [Industrial Application Field] The present invention relates to a cell culture device that performs culture while stirring a culture solution (medium) in a culture tank to disperse cells in the culture solution, and particularly relates to a cell culture device for culturing cells while dispersing them in the culture solution. The present invention relates to a cell culture device suitable for culturing cells.
細胞培養装置として、培養槽内の培養液中に細胞を分散
させて細胞の培養を行うものが知られている。この種の
細胞培養装置でm胞の増殖速度や培養効率を向上させる
ためには、細胞を培養液中に均一に分散させて栄養分や
酸素等を4−分に細胞へ供給する必要がある。そのため
には、培養液を適当に撹拌する必要があり、培養液の撹
拌手段とじC、プロペラ状やタービン状の撹拌翼あるい
はパドル状のF!を拝具を駆動軸や磁力により回転させ
るものが多く用いられていた。2. Description of the Related Art As a cell culture device, one is known that performs cell culture by dispersing cells in a culture solution in a culture tank. In order to improve the growth rate and culture efficiency of m-cells in this type of cell culture device, it is necessary to uniformly disperse the cells in the culture solution and supply nutrients, oxygen, etc. to the cells every 4 minutes. To do this, it is necessary to properly stir the culture solution, and the culture solution stirring means is C, a propeller-shaped or turbine-shaped stirring blade, or a paddle-shaped F! Many were used to rotate the worship tools using a drive shaft or magnetic force.
しかしながら、動物細胞は、他の微生物等に比べて大き
く、細胞を包むlll胞膜が脆く破壊されやすいため、
非常にゆっくりと撹拌することが要求されるが、上述の
撹拌翼等で、細胞を培養液中に均一に分散させるために
は、その回転数を高くしなければならず、細胞を傷付け
たり、また細胞を微粒子担体(マイクロキャリヤ)に担
持させて培養を行うものでは、担体からの脱落を生じる
虞があった。逆にm胞を傷付けない程度の回転数では、
撹拌力が不足して細胞を培養液中に均一に分散さUるこ
とができなかった。However, animal cells are larger than other microorganisms, and the cell membranes surrounding the cells are fragile and easily destroyed.
Very slow stirring is required, but in order to uniformly disperse the cells in the culture medium using the above-mentioned stirring blades, the rotation speed must be high, which may damage the cells or Furthermore, when cells are cultured by being supported on a microparticle carrier (microcarrier), there is a risk that the cells may fall off from the carrier. On the other hand, at a rotation speed that does not damage the m cell,
The cells could not be uniformly dispersed in the culture medium due to insufficient stirring power.
そこで、これを解決するため、従来より、撹IT苦を多
数設けたり、撹拌Wに複雑な動きをさぜたり、あるいは
特開昭60〜160 B 82号公報に示される撹拌器
のにうに特殊な形状の撹拌器を用いて培養液の撹拌を行
っていた。Therefore, in order to solve this problem, conventional methods have been to provide a large number of stirring IT devices, to add complex movements to the stirring W, or to create a special stirrer as shown in Japanese Patent Application Laid-open No. 160-160 B82. The culture solution was stirred using a stirrer with a different shape.
(発明が解決しようとする課題〕
しかしながら、これらのbのでは、装置が複雑になった
り、高価なものとなり、%J造や保守にし手間が11+
っていた。(Problems to be Solved by the Invention) However, with these methods, the device becomes complicated and expensive, and the construction and maintenance time is 11+.
It was.
そこで本発明は、筒中な構成で培養液の1Sl拌を十分
に行うことがでさ、製造や保守が容易で、しかも動植物
細胞のような弱い細胞の培養を行う際にも、細胞を傷付
けたりすることのない細胞培養装置を提供することを目
的とづる。Therefore, the present invention has a cylinder configuration that allows for sufficient stirring of 1 Sl of the culture solution, which is easy to manufacture and maintain, and which also prevents damage to cells even when culturing weak cells such as animal and plant cells. The purpose is to provide a cell culture device that does not require
〔課題を解決するための手段〕
上記した目的を達成する!こめに、本発明は、撹拌翼を
駆動軸により回転させて培慕液を撹拌し、Ill胞を培
養液中に分散させて組織培養を行う細胞培養装置におい
て、前記培養液を撹拌する撹拌翼を、萌記駆fJJ軸に
固着されるボス部材と、該ボス部材の下面外周部に、回
転の中心部を離間して設けられた複数の板状の撹拌器と
、該撹拌器の外縁下部を連結するリングとで形成すると
ともに、この撹ff黄を18養液内の上部に配設したこ
とを特徴としCいる。[Means to solve the problem] Achieve the above objectives! In particular, the present invention provides a cell culture device that performs tissue culture by rotating a stirring blade using a drive shaft to stir a culture medium and dispersing Ill cells in the culture medium. a boss member fixed to the Moeki drive fJJ shaft, a plurality of plate-shaped stirrers provided on the outer periphery of the lower surface of the boss member at a distance from the center of rotation, and a lower outer edge of the stirrer. It is characterized in that it is formed by a ring that connects the nutrient solution, and that the agitator is placed at the top of the nutrient solution.
〔作 用]
撹拌翼を上記のごとく形成して、培養液の上部に配置N
シて回転させると、撹拌器の回転による遠心力の作用に
より撹拌翼中心部の培養液が培養槽の壁面側に向かって
略水平に流動して壁面にfつ、壁面に沿って培養槽の底
部に向かって流下する。[Function] Form the stirring blades as described above and place them above the culture medium.
When the stirrer is rotated, the culture solution in the center of the stirring blade flows almost horizontally toward the wall of the culture tank due to the action of centrifugal force caused by the rotation of the stirrer. Flows down towards the bottom.
一方、培養槽中心部の培養液は、上記撹拌翼の回転に伴
いリング内を上界して撹拌翼の中心部に吸い上げられる
。これにより、培養槽内の培養液が、壁面近傍の下降流
と中心部の上昇流となって培養槽内を渦層なく流れるの
で、細胞が培養液中に均一に分散する。また上記形状の
撹拌翼によれば、撹拌翼の回転数が低くても、上記のよ
うな培養液の流れを発生させることができるので、非常
にゆっくりとした撹拌で、細胞を培養液内に均一に分散
させることができる。On the other hand, as the stirring blade rotates, the culture solution in the center of the culture tank rises inside the ring and is sucked up to the center of the stirring blade. As a result, the culture solution in the culture tank flows in the culture tank as a downward flow near the wall and an upward flow in the center without a whirlpool layer, so that cells are uniformly dispersed in the culture solution. In addition, according to the stirring blade of the above shape, even if the rotation speed of the stirring blade is low, it is possible to generate the flow of the culture medium as described above, so cells can be stirred into the culture medium with very slow stirring. Can be uniformly dispersed.
〔実施例) 以下、本発明の一実施例を図面に基づいて説明する。〔Example) Hereinafter, one embodiment of the present invention will be described based on the drawings.
第1図は細胞培養装dの全体構成を承りもので、細胞i
8苺装置1は、培養液を供給する液系統りと酸素等を供
給するガス系統Gとを有する供給部2と、細胞の培養を
行う培養部3、及び老廃物等を除去M゛るフィルタ一部
4により構成されている。Figure 1 shows the overall configuration of cell culture device d, with cells i
8. The strawberry device 1 includes a supply section 2 having a liquid system for supplying a culture solution and a gas system G for supplying oxygen, etc., a culture section 3 for culturing cells, and a filter for removing waste materials, etc. It is partly composed of 4 parts.
上記培養部3は、培養槽5と、該培養!!5内の上部に
配設された撹拌翼6からなるもので、培養槽5内には、
各種制御用としての溶存酸素センサ7、DI(センサ8
及びレベルセン+J9が設G″Jられるととしに、ガス
供給用のチューブ10が設けられている。The culture section 3 includes a culture tank 5 and the culture! ! It consists of stirring blades 6 placed on the top of the culture tank 5.
Dissolved oxygen sensor 7, DI (sensor 8) for various controls
A gas supply tube 10 is provided in addition to the level sensor +J9.
上、2撹拌W6は、第2図に示すように、駆動軸11に
固着されるボス部材12と、該ボス部材12の下面外周
部に設けられた4枚の板状の撹拌器13と、該撹拌器1
3の外縁下部を連結するリング14とで形成されており
、培養槽5の大きさ、叩ら培養液のm秀に応じて適宜の
大きさに形成される。As shown in FIG. 2, the upper 2 stirring W6 includes a boss member 12 fixed to the drive shaft 11, four plate-shaped stirrers 13 provided on the outer periphery of the lower surface of the boss member 12, The stirrer 1
3 and a ring 14 connecting the lower outer edges of the culture tank 5 and the ring 14, which is formed to an appropriate size depending on the size of the culture tank 5 and the strength of the beaten culture solution.
上記ボス部材12【よ、中心部に−F下方向の通孔12
aが形成されており、該通孔12aに駆動軸11を仲通
し、側壁に形成されたねじ孔12bにビスを螺合さVて
駆動軸11に固定される。また上記撹拌羽13は、前記
駆動軸11を中心とした円の法線方向に配設されており
、各撹拌器13の内方の撹拌翼6の回転中心部に空間部
を形成している。またリング14は、培養液Wt痒時に
整流板どして作用するもので、上記撹拌器13の外縁下
部を連結して撹拌′lJ6下部に適宜の高さで周設され
る。The boss member 12 [Yo, -F downward through hole 12 in the center]
A is formed, and the drive shaft 11 is inserted through the through hole 12a, and a screw is screwed into a screw hole 12b formed in the side wall to be fixed to the drive shaft 11. The stirring blades 13 are arranged in the normal direction of a circle centered on the drive shaft 11, and form a space at the center of rotation of the stirring blades 6 inside each stirrer 13. . Further, the ring 14 acts as a rectifying plate when the culture solution Wt is itchy, and connects the lower part of the outer edge of the stirrer 13 and is installed around the lower part of the stirrer 'lJ6 at an appropriate height.
上記のごとく形成された撹拌m6は、培養槽5の上部、
即ら培養液の上部に配置されて、館記駆!l!ll@1
1がモータ(図示せず)で回転駆動されることにより回
転する。The stirring m6 formed as described above is located at the top of the culture tank 5,
That is, it is placed on top of the culture solution, and it is used! l! ll@1
1 is rotated by being rotationally driven by a motor (not shown).
そして培養槽5内に培養液と細胞を入れて上記1党拌菌
6を回転させると、撹拌器13の回転に伴う遠心力の作
用により撹拌翼6中心部の培養液が培養槽5の壁面側に
向かって略水平に流動する。When the culture solution and cells are put into the culture tank 5 and the one-party stirring bacteria 6 is rotated, the culture solution in the center of the stirring blade 6 is spread onto the wall of the culture tank 5 due to the action of centrifugal force accompanying the rotation of the stirrer 13. It flows almost horizontally towards the side.
この18a液の流れは、培養槽5の壁面に至ると壁面に
治って培養槽5の底部に向かって流下し、培養槽5の底
部中心部に向かって流れていく。−万、リング14内方
の培養液は、上記培養液の壁面側への流れに伴い撹拌翼
6の中心部に上界し、上記のごとく順次撹拌16の外周
側に流れていく。即ち、培養槽5中心部の培養液は、上
記撹拌翼6の回転に伴いリング14内を上昇して撹拌翼
6の中心部に吸い上げられる。この時、撹拌翼6下部の
培養液は、撹拌羽13により撹拌されてもリング14で
1ft、痒翼6の外周側への流れ出しを止められるため
、叩らリング14の整流作用により、撹拌翼6下部の培
1に液がスムーズに撹拌翼6中心部に上界する。When this flow of liquid 18a reaches the wall surface of the culture tank 5, it settles on the wall surface, flows down toward the bottom of the culture tank 5, and flows toward the center of the bottom of the culture tank 5. - The culture solution inside the ring 14 rises to the center of the stirring blade 6 as the culture solution flows toward the wall, and sequentially flows to the outer circumferential side of the stirrer 16 as described above. That is, the culture solution in the center of the culture tank 5 rises within the ring 14 as the stirring blade 6 rotates and is sucked up to the center of the stirring blade 6. At this time, even if the culture solution at the bottom of the stirring blade 6 is stirred by the stirring blade 13, the ring 14 can stop it from flowing out to the outer circumferential side of the itching blade 6 by 1 ft. The liquid in the culture medium 1 at the bottom of the stirring blade 6 smoothly flows upward to the center of the stirring blade 6.
このように、撹拌m6を培養槽5の上部に配設して回転
させることにより、培!!115内の培養液に、培養槽
5壁面近傍の下降流と培養槽5中心部の上昇流を生じさ
せることができ、培養槽5内を溝肩なく流れる循環流と
することができる。従って、上記培養液の流れに伴いI
胞を培養液中に均一に分散することができ、細胞に十分
な栄養分や酸素を供給することができる。In this way, by placing the stirring m6 at the top of the culture tank 5 and rotating it, the culture! ! A downward flow near the wall surface of the culture tank 5 and an upward flow in the center of the culture tank 5 can be generated in the culture solution in the culture tank 115, and a circulating flow can be created that flows inside the culture tank 5 without any grooves. Therefore, with the flow of the above culture solution, I
Cells can be uniformly dispersed in the culture medium, and sufficient nutrients and oxygen can be supplied to the cells.
また撹拌翼6を上記のごとく形成して培養槽5のに部に
配設Jることにより、毎分10回回転度の非常にゆっく
りとした回転数でも、上記のような培養液の流れを生じ
させることができるので、細胞を傷付けることなく培養
液中に均一に分散させることができ、細胞の培養を効率
よく行うことができる。特に萌述のごとく傷付き易い動
物細胞や、細胞を微粒子担体(マイクロキャリA7)に
担持させて培養を行う際にも、細胞を傷付けたり、担体
から脱落させたりすることなく細胞を培養液中に均一に
分散させることができる。In addition, by forming the stirring blade 6 as described above and placing it in the corner of the culture tank 5, it is possible to maintain the flow of the culture solution as described above even at a very slow rotation speed of 10 rotations per minute. Therefore, the cells can be uniformly dispersed in the culture solution without damaging them, and the cells can be cultured efficiently. In particular, when culturing easily damaged animal cells such as Moe's, or cells supported on a microparticle carrier (Microcarrier A7), the cells can be placed in the culture solution without damaging the cells or causing them to fall off the carrier. can be uniformly dispersed.
一方上記培養部3に培養液や酸素等を供給する供給部2
は、新鮮な培N液を供給するための培養液タンク21と
培養液ポンプ22とからなる液系統りと、培養液内に酸
素ガス(0?)、窒素ガス(N2)、空気(air)及
びD H調整用の炭酸ガス(CO2)を供給するガス系
統Gを備えており、培養部3の状況に応じて培養液や各
種ガスを供給している。On the other hand, a supply section 2 that supplies culture solution, oxygen, etc. to the culture section 3
The liquid system consists of a culture solution tank 21 and a culture solution pump 22 for supplying fresh culture N solution, and oxygen gas (0?), nitrogen gas (N2), and air (air) in the culture solution. and a gas system G that supplies carbon dioxide gas (CO2) for DH adjustment, and supplies culture solution and various gases according to the conditions of the culture section 3.
上記ガス系統Gは、それぞれの回路に設けられた弁23
の開度を調節して各種ガスの供給量を調整しているが、
R索ガス回路Goと炭酸ガス回路GCには、それぞれコ
ントローラ24a、25aとタイマ24b、25bを備
えた補充回路24゜25が設けられている。酸素ガス回
路Goの補充回路24は、前記溶存酸素セン!す7によ
り検出された培養液中の溶存酸素lが所定量以下になる
と、コントローラ24aが作動し、タイマ24bに設定
された所定時間弁24Cを開いて酸素を補充り゛る。同
様に炭酸ガス回路Gcの補充回路25は、前記pHセン
サ8により検出された培甚液のpHが高くなった場合に
コントローラ25aが作動し、タイマ25bに設定され
た所定時間弁25cを聞いて炭酸ガスを補充する。The gas system G has valves 23 provided in each circuit.
The supply amount of various gases is adjusted by adjusting the opening degree of the
The R cable gas circuit Go and the carbon dioxide gas circuit GC are provided with replenishment circuits 24 and 25 each including controllers 24a and 25a and timers 24b and 25b. The replenishment circuit 24 of the oxygen gas circuit Go is the dissolved oxygen sensor! When the dissolved oxygen l in the culture solution detected by the cell 7 becomes less than a predetermined amount, the controller 24a is activated and opens the valve 24C for a predetermined time set in the timer 24b to replenish oxygen. Similarly, in the replenishment circuit 25 of the carbon dioxide circuit Gc, the controller 25a is activated when the pH of the culture solution detected by the pH sensor 8 becomes high, and the replenishment circuit 25 listens to the valve 25c for a predetermined time set in the timer 25b. Replenish carbon dioxide.
また酸素ガスと窒素ガスの供給源には、例えば窒素ガス
を選択的に吸着する吸着剤を充填した吸着器を用いた酸
素ガス供給装置1t26が用いられ、大気より濃厚な酸
素ガス(例えば、0290%〜93%、残部N2からな
るガス)を供給するように形成されている。窒素ガスも
、上記酸素ガス供給装置26と同様に酸素ガスの吸着剤
を用いた窒素ガス供給装置27を用いることで、窒素成
分の高いガス(例えば、N299%、021%からなる
ガス〉を供給することができる。Further, as a supply source of oxygen gas and nitrogen gas, for example, an oxygen gas supply device 1t26 using an adsorbent filled with an adsorbent that selectively adsorbs nitrogen gas is used, and oxygen gas that is richer than the atmosphere (for example, 0290 % to 93%, with the remainder being N2). Nitrogen gas can also be supplied by using a nitrogen gas supply device 27 that uses an oxygen gas adsorbent in the same way as the oxygen gas supply device 26 described above. can do.
前記各種のガスは、前記培!I槽5内に配設されたチュ
ーブ10を介して培養液中に供給される。The various gases mentioned above are the culture! It is supplied into the culture solution through a tube 10 disposed in the I tank 5.
このチューブ10は、ガス浸透性のシリコン樹脂により
形成されており、上記各種のガスを培養液中に発泡させ
ることなく溶解させることができる。The tube 10 is made of gas-permeable silicone resin, and can dissolve the various gases mentioned above into the culture solution without causing foaming.
またこのチューブ10は、培養槽5の中央部に螺旋状に
巻回して配設され、上下方向を開口したドラ71−チュ
ーブ状に設けられている。Further, this tube 10 is arranged in a spiral manner in the center of the culture tank 5, and is provided in the shape of a drum 71-tube that is open in the vertical direction.
このように、各種ガスを供給するチューブ10をドラ7
1へチューブ状に配設することで、#i記培養槽5内の
J8養液の上昇流と下降流とをチューブ10の内外周に
分離することができ、より円h゛+な循環流を形成づる
ことができ、培養液中の細胞の分散状態をさらに良好と
することができる。In this way, the tube 10 for supplying various gases is connected to the driver 7.
By arranging the tube 10 in a tube shape, the upward flow and downward flow of the J8 nutrient solution in the #i culture tank 5 can be separated into the inner and outer peripheries of the tube 10, resulting in a more circular circulation flow. can be formed, and the state of dispersion of cells in the culture solution can be further improved.
また前記フィルタ一部4は、員口胞の培養過程C・生じ
る産生物や老廃物を培養液の一部とともに除去し、培養
槽5内の培養液を所定の状態に保つbので、フィルター
31と培71R循環ポンプ32゜引扱きポンプ33及び
捕集タンク34により構成されており、前記培養槽5に
設置ノられたレベルヒンサ9に接続された:]ン1−ロ
ー″)35により引火きポンプ33の運転をLl制御し
℃ノイルター31の再生運転を自動的に行)ように形成
されている。Further, the filter part 4 removes products and wastes produced during the culture process C of the staff member along with a part of the culture solution, and maintains the culture solution in the culture tank 5 in a predetermined state. The culture tank 71R circulation pump 32 is composed of a handling pump 33 and a collection tank 34, and is connected to a level sensor 9 installed in the culture tank 5. 33 is under Ll control, and the regeneration operation of the Celsius noiler 31 is automatically carried out).
培N槽5内の培養液は、所定量が培養液循環ポンプ32
により吸入され、フィルター31の外部室31a下部に
導入されて産生物や老廃物を除去され、外部室31a上
部から培養槽5に戻る経路で循環している。前記引火き
ポンプ33は、通常はフィルタ−31内部室31E)の
培養液を産生物や老廃物と共に吸引して捕集タンク34
に送出しているが、培養槽5内の培養液の壜に応じ(−
前記コントローラ35が作動すると、この引抜きポンプ
:33が逆転しCフィルター31の内部室31bから外
部¥3121に向けC培養液を逆流さけ、フィルター3
1の+Tj生を行う。A predetermined amount of the culture solution in the culture N tank 5 is supplied to the culture solution circulation pump 32.
The water is sucked in, introduced into the lower part of the external chamber 31a of the filter 31, where products and wastes are removed, and circulated through the route returning to the culture tank 5 from the upper part of the external chamber 31a. The igniter pump 33 normally sucks the culture solution from the internal chamber 31E of the filter 31 together with products and wastes into the collection tank 34.
However, depending on the bottle of culture solution in culture tank 5 (-
When the controller 35 operates, this drawing pump 33 is reversed to avoid backflowing the C culture solution from the internal chamber 31b of the C filter 31 to the outside, and
Perform 1 +Tj raw.
このように細胞培養装置1を構成することにより、常に
新鮮な培養液と必要な酸素等を培養槽5内に供給づるこ
とができるどとbに、産生物ν)老廃物を含む培養液を
抜取ることができる。By configuring the cell culture device 1 in this way, it is possible to always supply fresh culture fluid and necessary oxygen etc. into the culture tank 5. It can be extracted.
従って、前記撹拌翼6の作用により、培養液中に均一に
分散した細胞に常に新鮮な培養液Al1等の持分4的え
ることができるとともに、産生物や老廃物を連続的に除
去でき、常に最適な培養環境を形成することができるの
で・、細胞の増殖速度や培養効率を向上させることがで
きる。Therefore, by the action of the agitating blades 6, it is possible to constantly supply the cells uniformly dispersed in the culture solution with a portion of fresh culture solution Al1, etc., and also to continuously remove products and wastes. Since an optimal culture environment can be created, cell proliferation rate and culture efficiency can be improved.
〔究明の効果]
本発明は、以上説明したよ−うに、特定の形状の撹拌翼
を培養槽の土1部に配設して培養液の撹拌を行うから、
ゆっくりどした回転で培養槽内の18養液を十分に撹拌
することができる。従って傷付き易い動物細胞を微粒子
担体に担持させて培養を行う場合でも、細胞を傷付(プ
たり、微粒子担体から1152落させること/、iく培
養液中に均一・に分散ざUることができるので、細胞に
十分な養分を与えることができ、細胞の培養効率を向上
ざぜることがでさ′る。また簡単な構造の撹拌刀を中線
に回転さぜるだ【プで十分な撹拌作用を(qられるため
、回転機構等を含めた培養槽の構造ら中細化でき、細胞
培養装置を安価に製作することができる。また撹拌翼の
製造組立く゛とともに、清掃、交換等の保守もn易とな
り、取扱・い性も向トする。[Effects of the Investigation] As explained above, the present invention stirs the culture solution by disposing stirring blades of a specific shape in one part of the soil of the culture tank.
The 18-nutrient solution in the culture tank can be sufficiently stirred by slow rotation. Therefore, even when culturing easily damaged animal cells supported on particulate carriers, it is important to avoid damaging the cells, dropping them from the particulate carriers, and ensuring that they are uniformly dispersed in the culture solution. As a result, sufficient nutrients can be given to the cells, and the cell culture efficiency can be improved.Additionally, a simple stirring knife can be rotated in the center line to provide sufficient agitation. Since the action is reduced, the structure of the culture tank, including the rotation mechanism, etc. can be downsized, and the cell culture device can be manufactured at low cost.In addition to manufacturing and assembling the stirring blades, maintenance such as cleaning and replacement can be done. It is also easier to handle and easier to handle.
第1図は細胞培養装置の全体構成を示す説明図、第2図
は撹拌翼の斜視図である。
1・・・細胞培養装置 3・・・培養部 5・・・
18養vI 6・・・撹拌翼 11・・・駆動軸
12・・・ボス部材 13・・・撹拌羽 14・
・・リング特 許 出 願 人 東京理化器械株式会社
代理人 弁理士 木 戸 傳一部間
木 戸 −愚問
小 川 眞
筋2因
旦攪拝翼FIG. 1 is an explanatory diagram showing the overall structure of the cell culture apparatus, and FIG. 2 is a perspective view of a stirring blade. 1...Cell culture device 3...Culture section 5...
18 Nutrient vI 6... Stirring blade 11... Drive shaft
12... Boss member 13... Stirring blade 14.
...Ring Patent Applicant Tokyo Rikakikai Co., Ltd. Agent Patent Attorney Denichi Kido
Kido - Stupid question
Ogawa Masuji 2 Indan stirring wing
Claims (1)
細胞を培養液中に分散させて組織培養を行う細胞培養装
置において、前記培養液を撹拌する撹拌翼を、前記駆動
軸に固着されるボス部材と、該ボス部材の下面外周部に
、回転の中心部を離間して設けられた複数の板状の撹拌
羽と、該撹拌羽の外縁下部を連結するリングとで形成す
るとともに、この撹拌翼を培養液内の上部に配設したこ
とを特徴とする細胞培養装置。1. Stir the culture solution by rotating the stirring blade with the drive shaft,
In a cell culture device that performs tissue culture by dispersing cells in a culture solution, a stirring blade for stirring the culture solution is attached to a boss member fixed to the drive shaft and a rotating part on the outer periphery of the lower surface of the boss member. It is characterized by being formed by a plurality of plate-shaped stirring blades spaced apart from the center and a ring connecting the lower outer edges of the stirring blades, and the stirring blades are arranged above the culture solution. A cell culture device for
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22169588A JP2742558B2 (en) | 1988-09-05 | 1988-09-05 | Cell culture device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22169588A JP2742558B2 (en) | 1988-09-05 | 1988-09-05 | Cell culture device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0269176A true JPH0269176A (en) | 1990-03-08 |
JP2742558B2 JP2742558B2 (en) | 1998-04-22 |
Family
ID=16770830
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22169588A Expired - Lifetime JP2742558B2 (en) | 1988-09-05 | 1988-09-05 | Cell culture device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2742558B2 (en) |
-
1988
- 1988-09-05 JP JP22169588A patent/JP2742558B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JP2742558B2 (en) | 1998-04-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AU2006340808B2 (en) | Pneumatic bioreactor | |
US20110003366A1 (en) | Methods of using pneumatic bioreactors | |
KR20160103135A (en) | Cell culture method and cell culture device | |
JPH01168272A (en) | Fermenter for cell culture | |
CN107438478B (en) | Biological treatment mixer | |
JP2005080662A5 (en) | ||
US20080261299A1 (en) | Pneumatic Bioreactor | |
KR900007935B1 (en) | Method and device for the treatment of a liquid mixture containing a biocatalyst or similar particles | |
JPH0269176A (en) | Cell culture apparatus | |
JPS6167476A (en) | Apparatus for vegetable cell culture | |
KR20120088900A (en) | Canister for receiving food waste | |
US5846817A (en) | Bioreactor, in particular for microgravity | |
JP2739066B2 (en) | Cell culture device | |
JPH01130722A (en) | Agitation device | |
JPH02119771A (en) | Cell culturing method and agitating fan for cell culture used in the same method | |
JPH0310676A (en) | Bag for cell culture | |
JPS61170383A (en) | Stirring culture apparatus | |
CN218465725U (en) | Protein dialysis device | |
JPS62269680A (en) | Cultivation apparatus | |
JP2547101B2 (en) | Underwater stirring device | |
JPH0659203B2 (en) | Incubator | |
RU2031113C1 (en) | Bioreactor | |
JPH0767625A (en) | Draft-tube-rotating air-lift culture and apparatus therefor | |
JPH0350715Y2 (en) | ||
CN207342320U (en) | Whirlpool and bubble avoiding device, magnetic agitation structure and tangential flow filtration system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080206 Year of fee payment: 10 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090206 Year of fee payment: 11 |
|
EXPY | Cancellation because of completion of term | ||
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090206 Year of fee payment: 11 |