JPH0775549A - Living cell culture device - Google Patents
Living cell culture deviceInfo
- Publication number
- JPH0775549A JPH0775549A JP22418993A JP22418993A JPH0775549A JP H0775549 A JPH0775549 A JP H0775549A JP 22418993 A JP22418993 A JP 22418993A JP 22418993 A JP22418993 A JP 22418993A JP H0775549 A JPH0775549 A JP H0775549A
- Authority
- JP
- Japan
- Prior art keywords
- culture
- screen
- stirring
- aeration
- 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.)
- Pending
Links
- 238000004113 cell culture Methods 0.000 title claims description 9
- 238000005273 aeration Methods 0.000 claims abstract description 54
- 238000003756 stirring Methods 0.000 claims abstract description 53
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 25
- 239000001301 oxygen Substances 0.000 claims abstract description 25
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 25
- 239000007787 solid Substances 0.000 claims abstract description 9
- 239000002245 particle Substances 0.000 claims abstract description 7
- 239000007788 liquid Substances 0.000 claims description 27
- 239000011148 porous material Substances 0.000 claims description 5
- 239000007789 gas Substances 0.000 abstract description 28
- 238000013019 agitation Methods 0.000 abstract description 12
- 230000000694 effects Effects 0.000 abstract description 6
- 230000007774 longterm Effects 0.000 abstract description 4
- 210000004027 cell Anatomy 0.000 description 33
- 238000000034 method Methods 0.000 description 18
- 239000001963 growth medium Substances 0.000 description 10
- 238000012258 culturing Methods 0.000 description 7
- 239000002609 medium Substances 0.000 description 7
- 230000001954 sterilising effect Effects 0.000 description 5
- 238000004659 sterilization and disinfection Methods 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 238000007796 conventional method Methods 0.000 description 4
- 239000006260 foam Substances 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 3
- 239000012737 fresh medium Substances 0.000 description 3
- 235000015097 nutrients Nutrition 0.000 description 3
- 230000010412 perfusion Effects 0.000 description 3
- 238000009423 ventilation Methods 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 230000021164 cell adhesion Effects 0.000 description 2
- 230000010261 cell growth Effects 0.000 description 2
- 230000003013 cytotoxicity Effects 0.000 description 2
- 231100000135 cytotoxicity Toxicity 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 238000011282 treatment Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000001464 adherent effect Effects 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 210000004102 animal cell Anatomy 0.000 description 1
- 244000309466 calf Species 0.000 description 1
- 238000012136 culture method Methods 0.000 description 1
- 238000013480 data collection Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000012010 growth Effects 0.000 description 1
- 239000000696 magnetic material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000035755 proliferation Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 210000002966 serum Anatomy 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Classifications
-
- 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
- C12M27/16—Vibrating; Shaking; Tilting
-
- 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
- C12M29/02—Percolation
-
- 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
- C12M29/04—Filters; Permeable or porous membranes or plates, e.g. dialysis
Landscapes
- Wood Science & Technology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Health & Medical Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical & Material Sciences (AREA)
- Zoology (AREA)
- Biomedical Technology (AREA)
- Sustainable Development (AREA)
- Microbiology (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Biotechnology (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
(57)【要約】
【構成】培養槽1にはスクリーン7が設置され、通気ス
パージャ14が設置された液中通気用配管2および循環
用配管3と閉鎖循環系を形成し、加振器4,振動軸5,撹
拌翼8が取付けられた撹拌軸6が装備されている。通気
スパージャ14から酸素含有ガスを通気して培養槽内の
培養液をエアリフト撹拌する。加振器4を稼働させて、
振動軸5および撹拌軸6を振動させ、スクリーン7およ
び撹拌翼8近傍の培養液を撹拌し、よりきめの細かい均
一な撹拌を行う。
【効果】マイクロキャリア等の固形粒子を含んだ培養液
でも、液中通気による効率的な酸素供給とエアリフト撹
拌を実施し、振動による撹拌によりきめ細かく均一に培
養液を撹拌でき、生体の細胞の長期高密度培養ができ
る。
(57) [Summary] [Structure] A screen 7 is installed in the culture tank 1, a submerged aeration pipe 2 and a circulation pipe 3 in which an aeration sparger 14 is installed form a closed circulation system, and a shaker 4 is provided. A stirring shaft 6 to which a vibrating shaft 5 and a stirring blade 8 are attached is provided. An oxygen-containing gas is aerated from the aeration sparger 14 to agitate the culture solution in the culture tank by air lift. Activate the shaker 4,
The vibrating shaft 5 and the stirring shaft 6 are vibrated to stir the culture solution in the vicinity of the screen 7 and the stirring blade 8 to perform finer and uniform stirring. [Effect] Even for a culture solution containing solid particles such as microcarriers, efficient oxygen supply and air lift agitation by submerged aeration can be performed, and the agitation by vibration can be used to finely and uniformly agitate the culture solution for long-term living cells. High density culture is possible.
Description
【0001】[0001]
【産業上の利用分野】本発明は、生体の細胞の培養装
置、特に、マイクロキャリア等の培養担体を用いる培養
装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a culture device for living cells, and more particularly to a culture device using a culture carrier such as a microcarrier.
【0002】[0002]
【従来の技術】マイクロキャリア培養に用いられる撹拌
方法に関しては、マイクロキャリアセル カルチャー
“ザ・プリンシプルズ アンド メンズ”(Microcarrie
r Cell Culture −the principles & methods−)(P3
5〜P37,マイクロキャリア培養法技術資料集,発
行:ファルマシアファインケミカル社)に記載されてい
る。また、細胞培養におけるその他の撹拌方法及びエア
リフト撹拌に関しては、「バイオリアクターの世界」
(P167〜P200,1992年,発行:株式会社柴
田ハリオ研究所)に記載されている。2. Description of the Related Art The stirring method used for microcarrier culture is described in Microcarrier Cell Culture.
“The Principles and Mens” (Microcarrie
r Cell Culture-the principles & methods-) (P3
5 to P37, technical data collection for microcarrier culture method, published by Pharmacia Fine Chemical Co., Ltd.). For other agitation methods and airlift agitation in cell culture, refer to "World of bioreactors".
(P167 to P200, 1992, published by Hario Research Institute Shibata Co., Ltd.).
【0003】[0003]
【発明が解決しようとする課題】エアリフト法は、ガス
通気の気泡のドライビングフォースで培養液を流動/撹
拌する方法で、培養槽内で直接ガスを通気する内部循環
エアリフト法と培養槽外において、ガスを通気し液を循
環させる外部循環式とに大別される。エアリフト法は、
所要動力が少なく、また、大型の装置にも適応可能な優
れた撹拌方法である。しかし、エアリフト法では培養槽
内の培養液の流動状態は大まかにしか制御できず、部分
的に滞流や偏流等が生じて培養液の混合状態にむらが生
じる場合がある。この現象は、特に、マイクロキャリア
(直径100〜1000μm)等の細胞よりもかなり大
きな固体粒子を含む培養液の場合に問題となる。The air lift method is a method of flowing / stirring a culture solution with a driving force of gas-permeable bubbles, and an internal circulation air lift method in which a gas is directly aerated in the culture tank and outside the culture tank. It is roughly classified into an external circulation type in which gas is aerated and liquid is circulated. The air lift method is
It is an excellent stirring method that requires less power and can be applied to large equipment. However, in the air lift method, the flow state of the culture solution in the culture tank can only be roughly controlled, and there is a case where a stagnant flow or a partial flow occurs and the mixed state of the culture solution becomes uneven. This phenomenon becomes a problem especially in the case of a culture medium containing solid particles much larger than cells such as microcarriers (diameter 100 to 1000 μm).
【0004】本発明の目的は、エアリフト法の長所を活
かしつつ、均一な培養液の混合を行い、マイクロキャリ
ア等の培養担体を用いた高密度培養を実施する生体の細
胞培養装置を提供することにある。An object of the present invention is to provide a cell culture device for a living body, which utilizes the advantages of the air-lift method, uniformly mixes culture solutions, and carries out high-density culture using a culture carrier such as a microcarrier. It is in.
【0005】[0005]
【課題を解決するための手段】上記目的を達成するため
に用いた手段について、図1を例に詳細に説明する。本
発明になる生体の細胞の培養装置では、まず、培養槽1
内にマイクロキャリアは通過させないが液成分は通過さ
せる細孔径をもったスクリーン7を設置する。スクリー
ン7によりマイクロキャリアの液中通気用配管2への漏
出を防止し、培養槽1内の培養液のエアリフト撹拌を可
能にする。図1に示したように培養槽1内にスクリーン
7を上下に二枚設置し、マイクロキャリアを二枚のスク
リーン7ではさまれた空間内に完全に閉じ込めるのがよ
り望ましい。液中通気用配管2の下部に設置されたスパ
ージャ14からガスを通気して配管内の液の密度を低下
させることにより、液が配管内を上昇し、次いで循環用
配管3を下降し、さらに培養槽1下部から上部に向かっ
て流れ、また液中通気配管2に戻る循環流を生じさせ
る。このように通気によって生じた液の循環流、すなわ
ち、通気によるエアリフト作用で生じる液の流動によ
り、培養槽1内の培養液が混合/撹拌される。このよう
なエアリフト撹拌を行い、生体の細胞の高密度培養を実
現することのできる生体の細胞の培養装置を、特願平5
−60581号明細書として既に出願している。ところで、
培養密度を高めるためにマイクロキャリア濃度を高めた
場合、マイクロキャリアの培養液中での分散状態にむら
を生じることがわかった。そこで、我々は更なる実験に
より、この問題を解決する方法として、上下振動する撹
拌器を取り付ける方法を見出した。撹拌器は撹拌軸6と
撹拌軸に取り付けられた撹拌翼8とから構成され、スク
リーン7の振動軸5と接続されている。さらに、振動軸
5は培養槽外に設置した加振器4に接続される。加振器
4を稼働させると、スクリーン7と撹拌翼8の近傍に図
2に示した混合流が生じて、マイクロキャリアが均一に
浮遊し、撹拌される。エアリフト作用による液の流れが
弱い部分に混合流が起こるように撹拌翼を設置するのが
より望ましい。本発明の撹拌器を装備した培養装置によ
れば、より均一なマイクロキャリア等の固体粒子を含有
する培養液の混合/撹拌と、液中通気配管内へのガス通
気量の低減化がはかれ、よりマイルドな撹拌を行うこと
ができる。Means used for achieving the above object will be described in detail with reference to FIG. 1 as an example. In the apparatus for culturing living cells according to the present invention, first, the culture tank 1
A screen 7 having a pore size that allows microcarriers to pass but liquid components to pass therethrough is installed therein. The screen 7 prevents the microcarriers from leaking into the submerged aeration pipe 2 and enables air lift stirring of the culture liquid in the culture tank 1. As shown in FIG. 1, it is more desirable that two screens 7 are installed in the culture tank 1 one above the other, and the microcarriers are completely confined in the space between the two screens 7. By injecting gas from the sparger 14 installed in the lower part of the submerged aeration pipe 2 to reduce the density of the liquid in the pipe, the liquid rises in the pipe, and then the circulation pipe 3 descends. A circulation flow is generated which flows from the lower part of the culture tank 1 toward the upper part and returns to the submerged aeration pipe 2. In this way, the circulating flow of the liquid generated by aeration, that is, the flow of the liquid generated by the air lift action by aeration mixes / stirs the culture liquid in the culture tank 1. Japanese Patent Application No. Hei 5 (1999) -9698 discloses a device for culturing living cells capable of achieving high-density culturing of living cells by performing such air-lift stirring.
-60581 has already been filed. by the way,
It was found that when the concentration of microcarriers was increased to increase the culture density, the microcarriers were unevenly dispersed in the culture solution. Then, we found a method of attaching a stirrer that vibrates up and down as a method of solving this problem by further experiments. The stirrer includes a stirring shaft 6 and a stirring blade 8 attached to the stirring shaft, and is connected to the vibration shaft 5 of the screen 7. Further, the vibrating shaft 5 is connected to the vibrator 4 installed outside the culture tank. When the shaker 4 is operated, the mixed flow shown in FIG. 2 is generated in the vicinity of the screen 7 and the stirring blade 8, and the microcarriers are uniformly suspended and stirred. It is more desirable to install a stirring blade so that a mixed flow occurs in a portion where the liquid flow due to the air lift action is weak. According to the culture device equipped with the stirrer of the present invention, it is possible to achieve more uniform mixing / stirring of the culture solution containing solid particles such as microcarriers and reduction of the gas aeration amount in the submerged aeration pipe. , A milder agitation can be performed.
【0006】[0006]
【作用】本発明の生体の細胞の培養装置は、培養液中の
液成分は通過させるがマイクロキャリアは通過させない
スクリーン7を装備した培養槽1と、下端に少なくとも
一つのガス通気スパージャを具備した液中通気用配管2
と、液中通気配管2内部での通気のエアリフト作用によ
り培養槽1内の培養液が撹拌されるように接続された閉
鎖循環系配管とを有し、さらにスクリーン7および/ま
たは撹拌軸6を振動させることにより培養液を均一に撹
拌する手段を有することを特徴とする。The apparatus for culturing living cells of the present invention comprises a culture tank 1 equipped with a screen 7 that allows liquid components in a culture medium to pass but not microcarriers, and at least one gas aeration sparger at the lower end. Liquid aeration pipe 2
And a closed circulation system pipe connected so that the culture liquid in the culture tank 1 is agitated by the air lift action of aeration in the submerged aeration pipe 2, and further comprises a screen 7 and / or a stirring shaft 6. It is characterized by having means for uniformly stirring the culture solution by vibrating.
【0007】培養槽内に設置されたスクリーン7は、マ
イクロキャリアが、ガス通気のエアリフト作用により液
の流動を生じさせる液中通気用配管内部に漏出するのを
防止する。マイクロキャリアが液中通気用配管に漏出し
た場合、マイクロキャリアは通気によるガスの気泡に同
伴されて、培養液上面の気相部に形成される泡沫層に取
り込まれてしまい培養が継続できなくなる。よって、エ
アリフト撹拌を可能にするにはマイクロキャリアを培養
槽内に閉じ込める必要がある。本発明の培養装置では、
スクリーン7の設定場所は、培養槽内の液に浸漬される
位置なら特に限定するものではない。しかし、マイクロ
キャリアの閉じ込められる空間が、実際に生体の細胞が
生存/増殖する培養ゾーンとなるので、培養ゾーンがで
きるだけ大きくとれる位置にスクリーン7を設置するの
が望ましい。さらに、培養液上部と培養槽の底部に二枚
スクリーン7を設置してマイクロキャリアを二枚のスク
リーン7内に閉じ込めるのがより望ましいスリーン7の
設置方法である。さらに、本発明では、培養槽内の培養
ゾーン以外の部分、すなわち、スクリーン7の外側か
ら、マイクロキャリア等の固形分を含まない培地を他の
分離手段を用いることなく抜き出すことができるので、
容易に灌流培養を行うことができる。The screen 7 installed in the culture tank prevents the microcarriers from leaking into the submerged aeration pipe which causes the liquid to flow due to the air-lifting action of gas aeration. When the microcarriers leak into the submerged aeration pipe, the microcarriers are entrained in gas bubbles due to aeration and taken into the foam layer formed in the gas phase portion on the upper surface of the culture solution, so that the culture cannot be continued. Therefore, it is necessary to confine the microcarriers in the culture tank to enable air lift stirring. In the culture device of the present invention,
The setting place of the screen 7 is not particularly limited as long as it is a position where it is immersed in the liquid in the culture tank. However, since the space in which the microcarriers are confined becomes a culture zone in which living cells actually survive / proliferate, it is desirable to install the screen 7 at a position where the culture zone can be as large as possible. Further, it is more desirable to install the two screens 7 on the upper part of the culture solution and the bottom part of the culture tank so as to confine the microcarriers in the two screens 7. Further, in the present invention, since the portion other than the culture zone in the culture tank, that is, the outside of the screen 7, the medium containing no solid content such as microcarriers can be extracted without using other separation means,
Perfusion culture can be easily performed.
【0008】スクリーン7は培養液のろ過効率を高める
ために培養液の循環流路に面しかつ循環方向に対して垂
直な向きとなるように設置されるのが望ましい。また、
スクリーン7を構成する部材の細孔径は、使用するマイ
クロキャリアの大きさにあわせて、マイクロキャリアが
培養ゾーンから漏出して酸素溶解溶液中に混入すること
のない大きさが選択される。スクリーン7の部材は、特
に限定するものではないが、培養開始時にオートクレー
ブ滅菌やスチーム滅菌を行うことから、これらの滅菌処
理に耐えうる材料であり、かつ、腐食性のないこと、細
胞毒性を示さないことが必須条件である。In order to enhance the filtration efficiency of the culture solution, the screen 7 is preferably installed so as to face the circulation channel of the culture solution and be oriented perpendicular to the circulation direction. Also,
The pore diameter of the member forming the screen 7 is selected in accordance with the size of the microcarrier used, so that the microcarrier does not leak from the culture zone and mix into the oxygen-dissolved solution. Although the member of the screen 7 is not particularly limited, it is a material that can withstand these sterilization treatments because it undergoes autoclave sterilization and steam sterilization at the start of culture, and it is not corrosive and exhibits cytotoxicity. The absence is a prerequisite.
【0009】液中通気用配管2は、ガス通気のエアリフ
ト作用により液の流動を生じさせると同時に、ガス通気
により効率的に酸素を溶解させることができる。よっ
て、本発明の培養装置の液中通気用配管でのガス通気
は、エアリフト作用による液の流動/撹拌の他に、培養
槽内の生体の細胞への効率的な酸素供給手段となってい
る。ガス通気によるエアリフト作用および酸素供給は、
ガスの通気量と通気ガスの組成によって制御できる。通
常は、空気,酸素,窒素,二酸化炭素ガスを適時混合し
て通気ガスとして用いる。さらに、本発明の一実施例を
示している図1により詳細に説明する。液中通気用配管
2の下部に設置したガス通気スパージャから酸素を含有
する通気ガスを通気する。通気のエアリフト作用により
液の流動が起こり、配管2を上昇し、次に、接続管3を
下降して培養槽1下部に設置されたスクリーン7の外側
まで達する。液はスクリーン7を通過して培養槽1内を
上昇し、スクリーン7を通過し、接続管3に流入して下
降し、配管2に戻る。酸素含有ガス通気による液中通気
で液中通気用配管内の液には酸素が富化される。酸素が
富化された液は、培養槽内を上昇していく過程で、培養
槽内の細胞に酸素および栄養分を供給し、代わりに老廃
物を受けとる。液中通気用配管内で通気する場所は、少
量の通気でより強い循環力を得ることができるよう、液
中通気用配管内部の下部にガス通気スパージャを設置す
るのがよい。The submerged aeration pipe 2 allows the liquid to flow by the air-lifting action of the gas aeration, and at the same time, can efficiently dissolve oxygen by the aeration of the gas. Therefore, the gas aeration in the submerged aeration pipe of the culture device of the present invention serves as an efficient oxygen supply means to the cells of the living body in the culture tank, in addition to the flow / agitation of the liquid by the air lift action. . The air lift function and oxygen supply by gas ventilation are
It can be controlled by the gas flow rate and the composition of the gas. Usually, air, oxygen, nitrogen, and carbon dioxide gas are appropriately mixed and used as an aeration gas. Further, a detailed description will be given with reference to FIG. 1 showing an embodiment of the present invention. An aeration gas containing oxygen is aerated from a gas aeration sparger installed at the bottom of the submerged aeration pipe 2. The liquid is caused to flow by the air-lifting action of aeration, and rises in the pipe 2 and then descends the connecting pipe 3 to reach the outside of the screen 7 installed under the culture tank 1. The liquid passes through the screen 7 and rises in the culture tank 1, passes through the screen 7, flows into the connecting pipe 3, descends, and returns to the pipe 2. Oxygen is enriched in the liquid in the pipe for submerged aeration by submerged aeration by aeration of oxygen-containing gas. The oxygen-enriched liquid supplies oxygen and nutrients to the cells in the culture tank in the process of rising in the culture tank, and receives waste products instead. A place to ventilate in the submerged aeration pipe is preferably provided with a gas aeration sparger under the inside of the submerged aeration pipe so that a stronger circulation force can be obtained with a small amount of aeration.
【0010】次に、本発明の特徴である、スクリーンの
振動と撹拌器の振動による培養液の撹拌について図1に
より詳細に説明する。スクリーン7には振動軸5と撹拌
軸6が接続されている。撹拌軸6には撹拌翼8が取りつ
けられている。振動軸5は加振器4に接続されている。
加振器4を稼働させると、振動軸5,スクリーン7,撹
拌軸5は一体となって、上下振動する。振動によりスク
リーン7近傍の培養液と撹拌翼8近傍の溶液が撹拌され
る。撹拌翼8は通気のエアリフト作用による液の流動が
弱い領域に設置するのがよい。撹拌翼の形状は特に限定
するものではないが、撹拌翼上にマイクロキャリア等の
固形物が堆積しない形状であることが望ましい。例を挙
げると、図3のような(a)円盤に円形の孔をあけたも
の、(b)円錐形のものなどがある。撹拌翼,撹拌軸およ
び振動軸の部材は、特に限定するものではないが、培養
開始時にオートクレーブ滅菌やスチーム滅菌を行うこと
から、これらの滅菌処理に耐えうる材料であり、かつ、
腐食性のないこと、細胞毒性を示さないことが必須条件
である。振動の大きさ、すなわち、上下の振れ幅と振動
回数によって培養液の撹拌状態は変化する。本発明によ
れば、エアリフト作用による液の流動と撹拌軸およびス
クリーンの振動により培養槽内の撹拌状態の適正化を図
ることできる。Next, the agitation of the culture solution by the vibration of the screen and the vibration of the agitator, which is a feature of the present invention, will be described in detail with reference to FIG. A vibration shaft 5 and a stirring shaft 6 are connected to the screen 7. A stirring blade 8 is attached to the stirring shaft 6. The vibration shaft 5 is connected to the vibrator 4.
When the vibration exciter 4 is operated, the vibrating shaft 5, the screen 7, and the stirring shaft 5 integrally vibrate vertically. Due to the vibration, the culture solution near the screen 7 and the solution near the stirring blade 8 are stirred. The stirring blade 8 is preferably installed in a region where the liquid flow due to the air lift effect of ventilation is weak. The shape of the stirring blade is not particularly limited, but it is preferably a shape in which solid matter such as microcarriers does not deposit on the stirring blade. For example, as shown in FIG. 3, (a) a disc with a circular hole, and (b) a conical disc are available. The members of the stirring blade, stirring shaft, and vibration shaft are not particularly limited, but since they are autoclave sterilized or steam sterilized at the start of culture, they are materials that can withstand these sterilization treatments, and
It is essential that it is not corrosive and does not show cytotoxicity. The stirring state of the culture solution changes depending on the magnitude of vibration, that is, the vertical swing range and the number of vibrations. ADVANTAGE OF THE INVENTION According to this invention, the stirring state in a culture tank can be optimized by the flow of the liquid by an air lift action, and the vibration of a stirring shaft and a screen.
【0011】加振器は、培養槽へ設置および/または取
外しが容易で、その加振操作により培養装置内の無菌状
態に影響を与えることなく、更に、培養装置の滅菌操作
に耐えうる部材で構成されているのが必須条件である。
具体的には、振動軸5に1)伸縮可能な蛇腹状の部材を
取付け、空気圧変化により該伸縮部材を伸縮させてスク
リーンに上下振動を与える方法、2)ソレノイドを取付
け、磁性体の吸引/排斥力によりスクリーンに上下振動
を与える方法、また、3)別途設けた回転軸に扁芯部材
を設置し、該扁芯部材と振動軸5としゅう動部材を間に
かませて接続し、扁芯部材の回転によりスクリーンに上
下振動を与える等の方法がある。加振器4による振動
は、培養液の撹拌と同時にスクリーン7の目詰りを抑制
する作用も持ち合わせている。振動により、スクリーン
7には培養液中の固形分が付着せず、目詰りが抑制され
るので、長期の培養を可能にする。The shaker is a member that can be easily installed in and / or removed from the culture tank, does not affect the aseptic condition in the culture apparatus by its vibration operation, and can withstand the sterilization operation of the culture apparatus. It is essential that it is configured.
Specifically, 1) a method of attaching an expandable and contractible bellows-shaped member to the vibration shaft 5 and expanding and contracting the expandable and contractible member by changing the air pressure to vertically vibrate the screen, 2) install a solenoid, and attract the magnetic material. A method in which the screen is vertically vibrated by the repulsive force, and 3) a eccentric member is installed on a separately provided rotating shaft, and the eccentric member and the vibration shaft 5 are connected by interposing a sliding member therebetween, There is a method of applying vertical vibration to the screen by rotating the core member. The vibration by the shaker 4 has the effect of suppressing clogging of the screen 7 at the same time as stirring the culture solution. Due to the vibration, the solid content in the culture solution does not adhere to the screen 7 and clogging is suppressed, which enables long-term culture.
【0012】[0012]
【実施例】以下、実施例により本発明を詳細に説明す
る。The present invention will be described in detail below with reference to examples.
【0013】(実施例1)図1は、本発明の培養装置の
一実施例である。(Embodiment 1) FIG. 1 shows an embodiment of the culture apparatus of the present invention.
【0014】本培養装置は、ステンレス鋼性の内容積8
リットル,培養容積6リットルの培養槽1,液中通気用
配管2,接続管3,加振器4,振動軸5,撹拌軸6,撹
拌翼8、図示していないが、新鮮培地貯槽,培地貯槽,
ガス供給系として空気源,酸素源,炭酸ガス源,窒素
源、および培養状況を監視し制御を行うための制御部か
ら構成されている。The main culturing apparatus has a stainless steel internal volume of 8
Liter, culture tank of 6 liters of culture volume 1, submerged aeration pipe 2, connection pipe 3, vibrator 4, vibrating shaft 5, stirring shaft 6, stirring blade 8, although not shown, fresh culture medium storage tank, culture medium Storage tank,
The gas supply system is composed of an air source, an oxygen source, a carbon dioxide gas source, a nitrogen source, and a control unit for monitoring and controlling the culture condition.
【0015】培養槽1には、培養液とマイクロキャリア
の懸濁液が貯留され、細孔径75μmのステンス製金網
で構成されたスクリーン7が、マイクロキャリアが液中
通気配管へ混入しないように設置されている。培養槽1
の培養液面上部の気相部には、通気によって発生する泡
沫を破泡するための消泡層13が設けられている。さら
に、培養槽1内にはレベルセンサ11,温度センサ1
2,pHセンサ9,DOセンサ10が設置されている。In the culture tank 1, a suspension of a culture solution and a microcarrier is stored, and a screen 7 composed of a stainless steel mesh with a pore diameter of 75 μm is installed so that the microcarrier does not enter the submerged aeration pipe. Has been done. Culture tank 1
A defoaming layer 13 for breaking bubbles generated by aeration is provided in the gas phase portion above the culture liquid surface. Furthermore, in the culture tank 1, a level sensor 11 and a temperature sensor 1
2, pH sensor 9 and DO sensor 10 are installed.
【0016】本培養装置により培養され得る生体の細胞
は、動物の細胞,微生物,植物細胞等がある。特に生体
の細胞が100μm以上の粒子状にて培養液中に浮遊し
ている培養液およびマイクロキャリア等の培養担体を用
いた培養に適している。Living cells that can be cultured by the present culture apparatus include animal cells, microorganisms, plant cells and the like. In particular, it is suitable for culturing using a culture medium in which living cells are suspended in the culture medium in the form of particles of 100 μm or more and a culture carrier such as a microcarrier.
【0017】まず、あらかじめ、培養槽1,新鮮培地貯
槽,培地貯槽およびこれらを接続する配管を高圧蒸気滅
菌する。First, the culture tank 1, the fresh medium storage tank, the medium storage tank, and the pipes connecting them are sterilized by high-pressure steam in advance.
【0018】なお、培養しようとする生体の細胞が付着
性の細胞である場合には、細胞が付着するための細胞付
着用マイクロキャリアを、あらかじめ常法により調製し
た後、培養槽内のスクリーン7で仕切られた培養ゾーン
内に注入して滅菌する。別途、細胞付着用マイクロキャ
リア調製槽を設置して、細胞付着用マイクロキャリアの
調製,滅菌,平衡化を行った後、培養槽1に無菌的に供
給する手段をとっても良い。When the cells of the living organism to be cultivated are adherent cells, a cell-adhering microcarrier for adhering cells is prepared in advance by a conventional method, and then the screen 7 in the culture tank is used. Sterilize by injecting into the culture zone partitioned by. Separately, a cell adhesion microcarrier preparation tank may be installed to prepare, sterilize and equilibrate the cell adhesion microcarrier, and then aseptically supply to the culture tank 1.
【0019】次いで、培養する生体細胞の生育に必要な
栄養分を溶かし込んだ培地を調製し、滅菌処理して新鮮
培地貯留槽に保管する。保管した新鮮培地のうち必要量
を培養槽1に移送する。培養槽内の液量はレベルセンサ
11の情報により調節する。次に、培養槽1外部に設け
たウォータジャケットに温水を通じて、培養槽内を培養
する生体の細胞の生育に適した温度に調節する。培養槽
内の温度状況は温度センサ12によって制御部におくら
れ、その情報をもとに制御部は培養槽内の温度を一定に
保つ。Next, a medium in which the nutrients necessary for the growth of the living biological cells to be cultured are dissolved is prepared, sterilized, and stored in a fresh medium storage tank. A required amount of the stored fresh medium is transferred to the culture tank 1. The amount of liquid in the culture tank is adjusted by the information from the level sensor 11. Next, warm water is passed through a water jacket provided outside the culture tank 1 to adjust the temperature in the culture tank to a temperature suitable for the growth of cells of the living body to be cultured. The temperature condition in the culture tank is sent to the control unit by the temperature sensor 12, and the control unit keeps the temperature in the culture tank constant based on the information.
【0020】細胞の増殖により、培養液中のpH,溶存
酸素濃度(DO)の変化や、栄養成分の枯渇,老廃物の
蓄積が起こる。このため、培養槽1には、温度センサ1
2,pHセンサ9,DOセンサ10が設置され、温度,
pH,DOを計測する。これらの計測情報は制御部に伝
送され培養状況の判定が行われる。The cell growth causes changes in pH and dissolved oxygen concentration (DO) in the culture solution, depletion of nutrients, and accumulation of waste products. Therefore, the temperature sensor 1 is installed in the culture tank 1.
2, pH sensor 9, DO sensor 10 is installed, temperature,
Measure pH and DO. These pieces of measurement information are transmitted to the control unit to determine the culture status.
【0021】生体細胞への酸素の供給および培養液のエ
アリフト撹拌は以下の方法によって行われる。すなわ
ち、生体の細胞により培養液中の酸素が消費されて溶存
酸素濃度が低下したことをDOセンサ10からの情報に
より制御部が判断する。この判断により制御部は、適当
な通気量で通気スパージャ14から酸素含有ガスを通気
する。通気により酸素は培地に溶解し、通気のエアリフ
ト作用により酸素が溶解した培地が流動,循環し、スク
リーン7を介して培養ゾーン内の培養液と接触し、酸素
が拡散して細胞に供給される。培養液中への酸素供給量
の調節は、通気ガス中の酸素濃度を調製して調節する方
法,通気量の増減により調節する方法、および培養槽1
の内圧を変化させて培養液中への酸素の溶解量を増加す
る方法の三手法を併用して行う。通気により培養槽液面
および液中通気用配管内気相部に生じる泡沫層は、消泡
層13により破泡する。消泡層13は表面をポリシロキ
酸で疎水化したステンレス製金網で構成されており、該
表面に泡沫が接触すると破泡する。さらに、エアリフト
撹拌と同時に加振器4を稼働させて、スクリーン7およ
び撹拌軸7を振動させ、ガス通気量を調節する。Supply of oxygen to living cells and airlift stirring of the culture solution are performed by the following methods. That is, the control unit determines from the information from the DO sensor 10 that oxygen in the culture solution has been consumed by the cells of the living body and the dissolved oxygen concentration has decreased. Based on this determination, the control unit vents the oxygen-containing gas from the vent sparger 14 at an appropriate ventilation rate. Oxygen is dissolved in the medium by aeration, and the medium in which oxygen is dissolved flows and circulates due to the airlift effect of aeration, contacts the culture solution in the culture zone through the screen 7, and oxygen is diffused and supplied to the cells. . The amount of oxygen supplied to the culture solution is adjusted by adjusting and adjusting the oxygen concentration in the aeration gas, by increasing or decreasing the aeration amount, and the culture tank 1.
This is carried out in combination with the three methods of changing the internal pressure of the solution to increase the amount of oxygen dissolved in the culture solution. The defoaming layer 13 breaks the foam layer generated on the liquid surface of the culture tank and on the gas phase inside the submerged aeration pipe by aeration. The defoaming layer 13 is composed of a stainless wire mesh whose surface is hydrophobized with polysiloxy acid, and when the foam comes into contact with the surface, the foam breaks. Further, the vibrator 4 is operated at the same time as the air lift agitation to vibrate the screen 7 and the agitation shaft 7 to adjust the gas aeration amount.
【0022】図4は、本実施例と従来法との実際の灌流
培養結果の一例を示した図である。旭化成マイクロキャ
リア(旭化成工業製)を6g/リットルの濃度で用い、
培地は新生子牛血清(大日本製薬より購入)を5%(V
/V)添加したERDF培地(極東製薬製)を使用して
CHO−K1細胞を培養した。グラフの縦軸は細胞濃度
を、横軸は培養日数を示す。細胞濃度は、培養液を適時
にサンプリングし、常法による核放出法によりマイクロ
キャリアに付着していた細胞数を生細胞数として計測
し、培養液1mリットルあたりの細胞数に換算して細胞
濃度とした。本実施例による培養結果をグラフ中にAと
して示し、従来法による培養結果をBに示した。従来法
とは本実施例で撹拌軸を取付けていない場合である。A
の培養では、撹拌軸およびスクリーンを振れ幅5〜10
mmで、5秒ごとに1回振動させた。A,Bともに細胞は
順調に増殖し、細胞の増殖に対応させて灌流率を1〜1
0まで増加し、培養日数30日の長期培養を達成した。
到達細胞濃度を比較すると、AではBでの到達細胞濃度
の約2倍の約4×107 個/mリットルとなった。これ
は、本発明の撹拌軸により培養液の混合状態の適正化が
はかれた効果の表れであるといえる。FIG. 4 is a diagram showing an example of an actual perfusion culture result of this example and the conventional method. Asahi Kasei Microcarriers (manufactured by Asahi Kasei Corporation) was used at a concentration of 6 g / liter,
The medium was 5% newborn calf serum (purchased from Dainippon Pharmaceutical) (V
/ V) ERDF medium (manufactured by Kyokuto Pharmaceutical Co., Ltd.) was used to culture CHO-K1 cells. The vertical axis of the graph represents the cell concentration and the horizontal axis represents the number of culture days. The cell concentration is determined by sampling the culture medium at a suitable time, measuring the number of cells attached to the microcarriers as the number of viable cells by the conventional nuclear release method, and converting it to the number of cells per 1 ml of the culture medium. And The culture result according to this example is shown as A in the graph, and the culture result according to the conventional method is shown as B. The conventional method is the case where the stirring shaft is not attached in this embodiment. A
In culturing, the agitation shaft and screen were shaken with a width of 5-10.
It was vibrated once every 5 seconds in mm. In both A and B, cells proliferate smoothly, and the perfusion rate is adjusted to 1 to 1 according to the proliferation of cells.
It was increased to 0 and a long-term culture of 30 days was achieved.
Comparing the reaching cell concentrations, the reaching cell concentration in A was about twice the reaching cell concentration in B and was about 4 × 10 7 cells / ml. It can be said that this is a manifestation of the effect that the mixing state of the culture solution was optimized by the stirring shaft of the present invention.
【0023】[0023]
【発明の効果】本発明によれば、マイクロキャリア等の
固形粒子を含んだ培養液でも、液中通気による効率的な
酸素供給とエアリフト撹拌を実施し、さらに振動による
撹拌によりきめ細かく均一に培養液を撹拌できるので、
生体の細胞の長期高密度培養が実現できる。EFFECTS OF THE INVENTION According to the present invention, even in a culture medium containing solid particles such as microcarriers, efficient oxygen supply and air lift agitation are carried out by submerged aeration, and further, the culture medium is finely and uniformly mixed by agitation by vibration. Can be stirred,
A long-term high-density culture of living cells can be realized.
【図1】本発明の培養装置の一実施例を示す説明図。FIG. 1 is an explanatory view showing an embodiment of a culture device of the present invention.
【図2】本発明の培養装置の培養槽内の液の混合状態を
示す説明図。FIG. 2 is an explanatory view showing a mixed state of the liquid in the culture tank of the culture device of the present invention.
【図3】本発明の撹拌器の撹拌翼の二つの実施例を示す
説明図。FIG. 3 is an explanatory view showing two examples of stirring blades of the stirrer of the present invention.
【図4】本発明の培養装置での培養結果の一例を示す特
性図。FIG. 4 is a characteristic diagram showing an example of a culture result in the culture device of the present invention.
1…培養槽、2…液中通気配管、3…循環用配管、4…
加振器、5…振動軸、6…撹拌軸、7…スクリーン、8
…撹拌翼、9…pHセンサ、10…DOセンサ、11…
レベルセンサ、12…温度センサ、13…消泡層、14
…通気スパージャ。1 ... Culture tank, 2 ... Submerged aeration pipe, 3 ... Circulation pipe, 4 ...
Exciter, 5 ... Vibration axis, 6 ... Stirring axis, 7 ... Screen, 8
... stirring blade, 9 ... pH sensor, 10 ... DO sensor, 11 ...
Level sensor, 12 ... Temperature sensor, 13 ... Defoaming layer, 14
… Ventilated spargers.
Claims (4)
せる細孔を有するスクリーンを装備した培養装置におい
て、前記スクリーンを振動させる手段及び前記スクリー
ン近傍の培養液を撹拌する手段を装備したことを特徴と
する生体の細胞培養装置。1. A culture device equipped with a screen having pores for preventing the passage of solid particles and for allowing the culture solution to pass, equipped with means for vibrating the screen and means for stirring the culture solution near the screen. A biological cell culture device characterized by the above.
手段が、前記スクリーンを振動させるための振動軸に接
続された撹拌軸及び前記撹拌軸に取り付けた撹拌翼であ
る生体の細胞培養装置。2. The biological cell culture apparatus according to claim 1, wherein the means for stirring the culture solution is a stirring shaft connected to a vibration shaft for vibrating the screen, and a stirring blade attached to the stirring shaft. .
複数の撹拌翼を取付けて培養液を撹拌する生体の細胞培
養装置。3. The biological cell culture device according to claim 1, wherein a plurality of stirring blades are attached to the stirring shaft to stir the culture solution.
せる細孔を有するスクリーンを装備した培養槽と、培養
液に酸素を供給するための液中通気用配管と、前記液中
通気用配管に通気してエアリフトを生じさせる手段を有
し、前記培養槽と前記液中通気用配管とは、前記液中通
気用配管内部でのエアリフト作用により前記培養槽内の
培養液に上向流が生じるように相互に接続された閉鎖循
環系を形成している生体の細胞培養装置において、前記
スクリーンを振動させるための振動軸と、前記振動軸に
接続された少なくとも一つの撹拌翼をもつ撹拌軸と、前
記スクリーンを振動させる手段を有することを特徴とす
る生体の細胞培養装置。4. A culture tank equipped with a screen having pores for preventing the passage of solid particles and allowing passage of the culture solution, a submerged aeration pipe for supplying oxygen to the culture solution, and the submerged aeration. The culture tank and the submerged aeration pipe have a means for aeration to generate air lift in the submerged pipe, and the culture tank and the submerged aeration pipe are directed upward to the culture liquid in the subculture tank by an airlift action inside the submerged aeration pipe. A living cell culture device forming a closed circulation system interconnected to generate a flow, comprising a vibrating shaft for vibrating the screen, and at least one stirring blade connected to the vibrating shaft. A living body cell culture device comprising a stirring shaft and means for vibrating the screen.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22418993A JPH0775549A (en) | 1993-09-09 | 1993-09-09 | Living cell culture device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22418993A JPH0775549A (en) | 1993-09-09 | 1993-09-09 | Living cell culture device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0775549A true JPH0775549A (en) | 1995-03-20 |
Family
ID=16809922
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22418993A Pending JPH0775549A (en) | 1993-09-09 | 1993-09-09 | Living cell culture device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0775549A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7419819B2 (en) | 2004-02-09 | 2008-09-02 | Mitsutech Co., Ltd. | Apparatus for cell culture |
CN103194382A (en) * | 2013-04-01 | 2013-07-10 | 南京工业大学 | Stirring type and air-lift type combined bioreactor and application thereof in preparation of rhamnose gum |
CN108522247A (en) * | 2018-04-28 | 2018-09-14 | 刘汉石 | A bioreactor for cultivating adventitious roots of ginseng |
CN111004713A (en) * | 2019-12-27 | 2020-04-14 | 华中科技大学鄂州工业技术研究院 | A culturing device for the dynamic growth environment of microorganisms |
KR20210095400A (en) * | 2020-01-23 | 2021-08-02 | (주)이셀 | Bio reactor for Cell Culture |
CN113403201A (en) * | 2021-08-10 | 2021-09-17 | 王思远 | Cell damage repairing culture device and application thereof |
-
1993
- 1993-09-09 JP JP22418993A patent/JPH0775549A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7419819B2 (en) | 2004-02-09 | 2008-09-02 | Mitsutech Co., Ltd. | Apparatus for cell culture |
CN103194382A (en) * | 2013-04-01 | 2013-07-10 | 南京工业大学 | Stirring type and air-lift type combined bioreactor and application thereof in preparation of rhamnose gum |
CN108522247A (en) * | 2018-04-28 | 2018-09-14 | 刘汉石 | A bioreactor for cultivating adventitious roots of ginseng |
CN111004713A (en) * | 2019-12-27 | 2020-04-14 | 华中科技大学鄂州工业技术研究院 | A culturing device for the dynamic growth environment of microorganisms |
KR20210095400A (en) * | 2020-01-23 | 2021-08-02 | (주)이셀 | Bio reactor for Cell Culture |
CN113403201A (en) * | 2021-08-10 | 2021-09-17 | 王思远 | Cell damage repairing culture device and application thereof |
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