JPH0229310B2 - - Google Patents
Info
- Publication number
- JPH0229310B2 JPH0229310B2 JP59080293A JP8029384A JPH0229310B2 JP H0229310 B2 JPH0229310 B2 JP H0229310B2 JP 59080293 A JP59080293 A JP 59080293A JP 8029384 A JP8029384 A JP 8029384A JP H0229310 B2 JPH0229310 B2 JP H0229310B2
- Authority
- JP
- Japan
- Prior art keywords
- cells
- culture tank
- cell culture
- filter
- culture
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000004113 cell culture Methods 0.000 claims description 25
- 239000001963 growth medium Substances 0.000 claims description 5
- 239000012466 permeate Substances 0.000 claims description 2
- 210000004027 cell Anatomy 0.000 description 24
- 239000000243 solution Substances 0.000 description 12
- 238000012258 culturing Methods 0.000 description 7
- 239000000725 suspension Substances 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 235000015097 nutrients Nutrition 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- 239000003094 microcapsule Substances 0.000 description 4
- 239000011148 porous material Substances 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 239000012736 aqueous medium Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 210000002966 serum Anatomy 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 2
- 150000001413 amino acids Chemical class 0.000 description 2
- 210000004102 animal cell Anatomy 0.000 description 2
- 239000003242 anti bacterial agent Substances 0.000 description 2
- 229940088710 antibiotic agent Drugs 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 230000002503 metabolic effect Effects 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 102000014150 Interferons Human genes 0.000 description 1
- 108010050904 Interferons Proteins 0.000 description 1
- 206010035226 Plasma cell myeloma Diseases 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 210000000628 antibody-producing cell Anatomy 0.000 description 1
- 239000003443 antiviral agent Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 1
- UBAZGMLMVVQSCD-UHFFFAOYSA-N carbon dioxide;molecular oxygen Chemical compound O=O.O=C=O UBAZGMLMVVQSCD-UHFFFAOYSA-N 0.000 description 1
- 230000001413 cellular effect Effects 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000005515 coenzyme Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010353 genetic engineering Methods 0.000 description 1
- 239000005556 hormone Substances 0.000 description 1
- 229940088597 hormone Drugs 0.000 description 1
- 210000004408 hybridoma Anatomy 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 229940079322 interferon Drugs 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 201000000050 myeloid neoplasm Diseases 0.000 description 1
- -1 nutrients Chemical class 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 230000035755 proliferation Effects 0.000 description 1
- 230000001902 propagating effect Effects 0.000 description 1
- 238000013341 scale-up Methods 0.000 description 1
- 239000012679 serum free medium Substances 0.000 description 1
- 238000004114 suspension culture Methods 0.000 description 1
- 230000008685 targeting Effects 0.000 description 1
- 229960005486 vaccine Drugs 0.000 description 1
- 239000011782 vitamin Substances 0.000 description 1
- 235000013343 vitamin Nutrition 0.000 description 1
- 229940088594 vitamin Drugs 0.000 description 1
- 229930003231 vitamin Natural products 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
- 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)
Description
【発明の詳細な説明】
(a) 産業上の利用分野
本発明は細胞を培養増殖させるための培養槽に
関するものである。さらに詳しくは、大規模にか
つ高密度に細胞培養を行なう目的で作られたサス
ペンジヨン型細胞培養槽に関するものである。DETAILED DESCRIPTION OF THE INVENTION (a) Industrial Application Field The present invention relates to a culture tank for culturing and propagating cells. More specifically, the present invention relates to a suspension-type cell culture tank manufactured for the purpose of culturing cells on a large scale and at high density.
(b) 従来技術
細胞大量培養は例えばウイルス、ワクチン、イ
ンターフエロンなどの抗ウイルス剤、あるいはホ
ルモンなどの生物薬品の工業的製造に重要な技術
である。殊に近年特定タンパク質などの標的とす
るモノクローナル抗体の生産は抗体産生細胞とミ
エローマ細胞の配合によるハイブリドーマ細胞の
大量培養によるものであり、その技術の解決は工
業的に不可欠な問題である。(b) Prior Art Mass cell culture is an important technology for the industrial production of viruses, vaccines, antiviral agents such as interferon, or biological drugs such as hormones. Particularly in recent years, the production of monoclonal antibodies targeting specific proteins has been achieved by mass culturing hybridoma cells by combining antibody-producing cells and myeloma cells, and solving this technology is an industrially essential problem.
また、大規模であり、かつ高密度に細胞を培養
することは上記有用物質を低コストで生産するた
めに必須の技術であり、その技術の急速な解決が
望まれている。 In addition, culturing cells on a large scale and at high density is an essential technology for producing the above-mentioned useful substances at low cost, and a rapid solution to this technology is desired.
従来、サスペンジヨン型の細胞培養は一般に培
養びんやスピンナ―フラスコを用いて実験室的規
模で行なわれている。 Conventionally, suspension-type cell culture has generally been carried out on a laboratory scale using culture bottles or spinner flasks.
しかしながら、上記の方法では一定量の栄養分
の中で培養されるため細胞の生長増殖は比較的低
い濃度で停止する。 However, in the above method, since the cells are cultured in a fixed amount of nutrients, the growth and proliferation of cells stops at a relatively low concentration.
近年、サスペンジヨン型の高密度細胞培養方法
およびそのための装置としていくつかの提案がな
されている。たとえば、マグネチツクスターラー
もしくはモーターで駆動される回転軸に平行な面
にフイルターを有する筒形回転体を回転させてフ
イルターのつまりを遠心力で防ぎながら培養液を
入れかえる高密度培養装置が提案されている(米
国特許第3647632号明細書参照)。 In recent years, several proposals have been made for suspension-type high-density cell culture methods and devices for the same. For example, a high-density culture device has been proposed that rotates a cylindrical rotating body that has a filter on a plane parallel to a rotating shaft driven by a magnetic stirrer or motor, and replaces the culture solution while preventing the filter from clogging using centrifugal force. (See US Pat. No. 3,647,632).
しかしながら上記の方法では、単位細胞当たり
または培養液あたりの濾過面積を或る一定以上大
きくすることに制約があるため、スケールアツプ
が非常に困難である。 However, in the above method, there are restrictions on increasing the filtration area per unit cell or per culture solution beyond a certain level, making it extremely difficult to scale up.
(c) 発明の構成
そこで本発明者らは前記のような従来法におけ
る欠点を克服し、サスペンジヨン型の細胞培養法
によつて大規模かつ高密度の培養が可能な培養槽
について研究を進めた結果、本発明に到達した。(c) Structure of the Invention Therefore, the present inventors overcame the drawbacks of the conventional methods as described above and proceeded with research on a culture tank that is capable of large-scale and high-density culture using a suspension type cell culture method. As a result, the present invention was achieved.
すなわち本発明はサスペンジヨン型細胞培養槽
であつて、該培養槽中には、培養液は透過するが
細胞は透過しないフイルターの領域を少なくとも
部分的に有する盤状体の少なくとも1個が培養液
を装置外へ取り出す導管に該導管と同軸で回転す
るように取り付けられた回転型フイルターを培養
槽中に装着したサスペンジヨン型細胞培養槽であ
る。 That is, the present invention is a suspension-type cell culture tank, in which at least one plate-like body having at least partially a filter region through which the culture solution permeates but not cells is provided. This is a suspension-type cell culture tank in which a rotary filter is installed in the culture tank and is attached to a conduit that takes out the cellulose to the outside of the apparatus so as to rotate coaxially with the conduit.
本発明の細胞培養槽はサスペンジヨン型の細胞
培養に適用されるが、サスペンジヨン型とは、水
性媒体中で細胞それ自体が浮遊しながら或いは細
胞を微小担体(マイクロキヤリアー)に担持して
浮遊しながら、またマイクロカプセル中で細胞が
生育されるような種々の浮遊培養をいう。殊に本
発明は細胞自体を浮遊させながら培養する方法に
有利に用いられる。 The cell culture tank of the present invention is applied to suspension type cell culture, which means that the cells themselves are suspended in an aqueous medium or that the cells are supported on microcarriers. Refers to various suspension cultures in which cells are grown in suspension or in microcapsules. In particular, the present invention can be advantageously used in a method of culturing cells in suspension.
本発明の細胞培養槽を用いて培養される細胞
は、植物細胞、動物細胞、微生物細胞などであつ
てもよく、また人為的或いは遺伝子操作により変
性された細胞であつてもよい。殊に本発明の培養
槽は動物細胞の培養に適している。 The cells cultured using the cell culture tank of the present invention may be plant cells, animal cells, microbial cells, etc., or may be cells that have been modified artificially or by genetic manipulation. In particular, the culture tank of the present invention is suitable for culturing animal cells.
本発明におけるサスペンジヨン型の細胞培養槽
中においては、培養しようとする細胞培が培養液
中に浮遊した状態で培養される。培養液は実質的
に水よりなる水性媒体に、種々の無機塩、ビタミ
ン類、補酵素、ブドウ糖、アミノ酸、抗生物質な
どの通常細胞培養に使用される添加成分が加えら
れている。また培養液には血清を加えることもで
きるし、血清を用いない所謂無血清倍地を培養液
として使用することも出来る。 In the suspension-type cell culture tank of the present invention, the cell culture to be cultured is cultured in a suspended state in a culture solution. The culture solution is an aqueous medium consisting essentially of water, to which additive components commonly used in cell culture, such as various inorganic salts, vitamins, coenzymes, glucose, amino acids, and antibiotics, are added. Further, serum can be added to the culture solution, or a so-called serum-free medium that does not use serum can also be used as the culture solution.
本発明における盤状体のフイルター領域には培
養液は透過するが、細胞あるいはそれが付着した
微小担体又はそれが中に入つたマイクロカプセル
は透過しない大きさの細孔が多数設けられてい
る。細胞自体を浮遊させて培養させる場合、細孔
の大きさは細胞の大きさによつて左右されるが一
般に平均孔径が10μ以下、好ましくは8μ以下が適
当である。一方微小担体(マイクロキヤリアー)
の表面に細胞を付着させて培養させる場合又はマ
イクロカプセルを使用して培養させる場合にはそ
れらが透過しない大きさの細孔である必要があ
る。 The filter region of the disc-shaped body in the present invention is provided with a large number of pores of a size that allows the culture solution to pass through, but not the cells, the microcarriers to which they are attached, or the microcapsules in which they are contained. When cells are cultured in suspension, the size of the pores depends on the size of the cells, but in general, an average pore size of 10 μm or less, preferably 8 μm or less is suitable. On the other hand, microcarriers
When cells are cultured by adhering to the surface of the microcapsule or when cells are cultured using microcapsules, the pores need to be large enough to prevent them from passing through.
また、該フイルターは、水を或る程度透過する
能力を有することが望ましい。すなわち該フイル
ターは水の透過係数(ml/m2・hr・mmHg)が10
以上、好ましくは100以上であるのが有利である。
一方上限は特にないが、20000以下、好ましくは
10000以下が望ましい。 It is also desirable that the filter has the ability to transmit water to some extent. In other words, the filter has a water permeability coefficient (ml/ m2・hr・mmHg) of 10.
or more, preferably 100 or more.
On the other hand, there is no particular upper limit, but 20,000 or less, preferably
Desirably 10000 or less.
さらに該フイルター領域には栄養分や細胞の老
廃物、代謝生産物などの如き分子量の小さい化合
物は透過するが分子量の大きい化合物(例えば分
子量1000以上、好ましくは5000以上)は透過しな
い膜、例えば限外濾過膜を使用することも可能で
ある。 In addition, the filter region includes a membrane that allows small molecular weight compounds such as nutrients, cellular waste products, and metabolic products to pass through, but does not allow large molecular weight compounds (e.g., molecular weight of 1000 or more, preferably 5000 or more) to pass through. It is also possible to use filter membranes.
本発明でいう盤状体とは、回転軸に垂直な面の
径をa、回転軸方向の長さをbとしたとき、a/
bの比が2以上100以下のものが適当であり、と
くに2以上30以下のものがよい。 In the present invention, the disk-shaped body means a/
A ratio of b of 2 or more and 100 or less is suitable, and a ratio of 2 or more and 30 or less is particularly preferred.
また、培養槽における回転軸に垂直な培養槽の
断面積あたり盤状体の面積比は10%以上95%以下
が好ましく、特に20%以上80%以下のものがよ
い。 Further, the area ratio of the plate-shaped bodies per cross-sectional area of the culture tank perpendicular to the rotation axis of the culture tank is preferably 10% or more and 95% or less, particularly preferably 20% or more and 80% or less.
盤状体の断面の形状は薄い矩形、菱形、三角
形、楕円、半楕円などが適当である。 Appropriate cross-sectional shapes of the plate-shaped body include thin rectangles, rhombuses, triangles, ellipses, and semi-ellipses.
かかる盤状体には前記フイルター領域が少くと
も部分的に設けられており、そのフイルター領域
は盤状体のほぼ全面に設けられてもよく、一部で
あつてもよい。一部である場合には、上面或いは
下面、又はそれら面の一部であつてもよい。 The filter area is provided at least partially on such a disk-like body, and the filter area may be provided on almost the entire surface of the disk-like body, or may be provided on only a part of the disk-like body. If it is a part, it may be the upper surface, the lower surface, or a part of these surfaces.
以下、添付図面により本発明の細胞培養槽を更
に詳細に説明する。 Hereinafter, the cell culture tank of the present invention will be explained in more detail with reference to the accompanying drawings.
添付第1図は、本発明の細胞培養槽を用いて培
養を行なうための該略図の一例を示すものであ
り、第2―A図は本発明の細胞培養槽に使用され
る盤状体の一例の外観図で、第2―B図はその盤
状体の断面構造を示すもので、また第3―A図は
他の例の盤状体の外観図であり、第3―B図はそ
の断面構造を示すものである。また第4図は第1
図とは別個の細胞培養槽の該略図を示したもので
ある。 Attached Figure 1 shows an example of the schematic diagram for carrying out culture using the cell culture tank of the present invention, and Figure 2-A shows a diagram of the disc-shaped body used in the cell culture tank of the present invention. Fig. 2-B is an external view of one example, and Fig. 2-B shows the cross-sectional structure of the plate-like body, and Fig. 3-A is an external view of another example of the plate-like body. It shows its cross-sectional structure. Also, Figure 4 shows the first
The figure shows a schematic diagram of a separate cell culture tank.
第1図は盤状体5を回転作動させて培養する場
合を示したものであり、第1図において、1はサ
スペンジヨン型培養槽における培養槽本体であ
り、栄養物などを含む水性媒体はその供給槽2か
らポンプ3により供給導管4を通り、培養槽中へ
送られる。培養槽1にはフイルター部分を有する
盤状体5がそのフイルター領域がサスペンジヨン
液につかるように備えられており、この盤状体は
駆動部6により回転し、細胞を培養液中に効果的
に浮遊させる。撹拌は特に必要はないが、盤状体
の上部又は下部又は中間にとりつけられた撹拌翼
によつて撹拌をさらに効果的に行なうことも可能
である。また別途に設けられたマグネチツクスタ
ーラーでもよい。さらに培養液中の細胞を効果的
に浮遊させることのできる他の撹拌効果を有する
手段であつてもよい。 Fig. 1 shows the case of culturing by rotating the disk-shaped body 5. In Fig. 1, 1 is the main body of a suspension-type culture tank, and the aqueous medium containing nutrients, etc. From the supply tank 2, it is sent by a pump 3 through a supply conduit 4 into the culture tank. The culture tank 1 is equipped with a disk-like body 5 having a filter portion so that the filter area is submerged in the suspension liquid, and this disk-like body is rotated by a drive unit 6 to effectively transfer the cells into the culture medium. to float. Stirring is not particularly necessary, but stirring can be made more effective by using a stirring blade attached to the top, bottom, or middle of the disc. Alternatively, a separately provided magnetic stirrer may be used. Furthermore, other means having a stirring effect that can effectively suspend cells in the culture solution may be used.
一方、古い培養液はポンプ3′によつて盤状体
5の下面に設けられたフイルター領域を透過し、
回転軸の中を経て導管4′を通つて培養槽外へ取
り出される。 On the other hand, the old culture solution is passed through a filter area provided on the lower surface of the plate-like body 5 by the pump 3'.
It passes through the rotating shaft and is taken out of the culture tank through a conduit 4'.
第2―A図の盤状体およびその断面を示した第
2―B図において、7はフイルター領域であり、
回転軸と同軸の導管8にとりつけられている。2
―B図においてフイルターは平面の同型で下面に
ついているが、これは他の形状であつてもよい。
例えば第3―A図およびその断面を示す第3―B
図に示されているようにドーナツ型で上下両面に
フイルター領域(斜線部分)があつてもよい。 In FIG. 2-B showing the disk-shaped body in FIG. 2-A and its cross section, 7 is a filter area;
It is attached to a conduit 8 coaxial with the rotation axis. 2
- In Figure B, the filter is of the same planar shape and is attached to the bottom surface, but it may have other shapes.
For example, Figure 3-A and Figure 3-B showing its cross section.
As shown in the figure, it may be donut-shaped with filter areas (hatched areas) on both the top and bottom sides.
このように回転軸の方向とフイルター領域の面
を垂直にすることにより、フイルターのめづまり
を遠心力によつて防ぐことができると同時に、培
養槽の形状、培養液の量、細胞密度などに応じて
フイルターの面積を容易に増減することが可能で
ある。さらに培養槽には、酸素、二酸化炭素や栄
養素の濃度、PHの値を測定し、それらを或る範囲
に維持する装置が一般に設置されているが、本発
明の細胞培養槽にもこれらの装置が備えられてい
てもよいことはいうまでもない。しかし第1図及
び第4図にはこれらの付属装置は省略されてい
る。 By making the direction of the rotation axis perpendicular to the plane of the filter area, centrifugal force can prevent the filter from clogging. It is possible to easily increase or decrease the area of the filter. Furthermore, culture tanks are generally equipped with devices that measure oxygen, carbon dioxide, nutrient concentrations, and PH values and maintain them within certain ranges, and the cell culture tank of the present invention also includes these devices. Needless to say, it may be provided. However, these accessories are omitted from FIGS. 1 and 4.
本発明の培養槽に供給される新しい培養液は、
この中にブドウ糖、タンパク質の如き栄養源、
種々のアミノ酸、無機塩、抗生物質などの細胞培
養に必要な成分を水溶液として含むものが使用さ
れるが、さらに血清を含んでいてもよく、また含
んでいなくてもよい。これらの成分は必要なすべ
てを培養源として供給してもよいが、一部の成分
は、他の供給手段によつて培養液中へ導入するこ
とも可能である。 The new culture solution supplied to the culture tank of the present invention is
This includes nutrients such as glucose and protein,
An aqueous solution containing components necessary for cell culture such as various amino acids, inorganic salts, and antibiotics is used, and may or may not further contain serum. All of the necessary components may be supplied as a culture source, but some of the components may also be introduced into the culture medium by other supply means.
第4図は本発明における盤状体の4個の9のよ
うに多段に直列につないだ列を示したものであ
り、盤状体の数およびフイルター部分の面積を増
減することにより培養槽に応じた撹拌と濾過面積
を容易に得ることが可能である。第4図におい
て、1,2,3,4,3′及び4′は第1図と同様
のものを意味する。 Figure 4 shows a row of four disc-shaped bodies connected in series in multiple stages like 9 in the present invention, and the number of disc-shaped bodies and the area of the filter part can be increased or decreased to accommodate the culture tank. It is possible to easily obtain suitable stirring and filtration areas. In FIG. 4, 1, 2, 3, 4, 3' and 4' have the same meanings as in FIG.
以上説明した本発明の細胞培養槽によれば、サ
スペンジヨン型の細胞培養において連続的に培養
液を供給できかつ連続的に老廃物、代謝生産物、
生育阻害物質などを除去でき、またフイルターの
めづまりもおこらないため、高密度でしかも大量
の細胞を長期間にわたつて培養することが可能と
なる。 According to the cell culture tank of the present invention as described above, it is possible to continuously supply a culture medium in suspension-type cell culture, and to continuously remove waste products, metabolic products, etc.
Since growth-inhibiting substances can be removed and the filter does not become clogged, it is possible to culture a large number of cells at high density over a long period of time.
第1図は本発明の細胞培養槽の全体を示す該略
図の一例を示すものである。第2―A図は本発明
の細胞培養槽に使用される盤状体の一例の外観図
であり、第2―B図はその断面を示すものであ
る。第3―A図は本発明に使用される盤状体の他
の一例の外観図であり、第3―B図はその断面を
示すものである。第4図は、該盤状体を多段に直
列につないだ培養槽の一例の概略図を示したもの
である。
FIG. 1 shows an example of a schematic diagram showing the entire cell culture tank of the present invention. FIG. 2-A is an external view of an example of a disk-shaped body used in the cell culture tank of the present invention, and FIG. 2-B is a cross-sectional view thereof. FIG. 3-A is an external view of another example of the disk-shaped body used in the present invention, and FIG. 3-B is a cross-sectional view thereof. FIG. 4 shows a schematic diagram of an example of a culture tank in which the plate-shaped bodies are connected in series in multiple stages.
Claims (1)
液は透過するが細胞は透過しないフイルター領域
を少なくとも部分的に有する盤状体の少なくとも
1個が培養液を装置外へ取り出す導管に該導管と
同軸で回転し得るように取り付けられた回転型フ
イルターを培養槽中に装着したサスペンジヨン型
細胞培養槽。1. A sun pendillion type cell culture tank, in which at least one disk-like body having at least partially a filter region through which the culture medium permeates but not cells is coaxially connected to the conduit for taking out the culture medium out of the apparatus. A suspension-type cell culture tank in which a rotatable filter is installed in the culture tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59080293A JPS60224486A (en) | 1984-04-23 | 1984-04-23 | Cell culture tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59080293A JPS60224486A (en) | 1984-04-23 | 1984-04-23 | Cell culture tank |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60224486A JPS60224486A (en) | 1985-11-08 |
| JPH0229310B2 true JPH0229310B2 (en) | 1990-06-28 |
Family
ID=13714220
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59080293A Granted JPS60224486A (en) | 1984-04-23 | 1984-04-23 | Cell culture tank |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60224486A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH074234B2 (en) * | 1986-01-30 | 1995-01-25 | 三井石油化学工業株式会社 | Plant tissue culture method and culture device |
| JP2509630B2 (en) * | 1987-07-29 | 1996-06-26 | 三井石油化学工業株式会社 | Culture method and culture device |
| EP3109314A4 (en) | 2014-02-17 | 2017-03-08 | Asahi Kasei Kabushiki Kaisha | Cell culturing device |
-
1984
- 1984-04-23 JP JP59080293A patent/JPS60224486A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60224486A (en) | 1985-11-08 |
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