JPS6212989B2 - - Google Patents
Info
- Publication number
- JPS6212989B2 JPS6212989B2 JP1095484A JP1095484A JPS6212989B2 JP S6212989 B2 JPS6212989 B2 JP S6212989B2 JP 1095484 A JP1095484 A JP 1095484A JP 1095484 A JP1095484 A JP 1095484A JP S6212989 B2 JPS6212989 B2 JP S6212989B2
- Authority
- JP
- Japan
- Prior art keywords
- cell culture
- culture
- cells
- unit
- suspension
- 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
Links
- 238000004113 cell culture Methods 0.000 claims description 27
- 239000012528 membrane Substances 0.000 claims description 14
- 235000015097 nutrients Nutrition 0.000 claims description 11
- 239000012510 hollow fiber Substances 0.000 claims description 10
- 239000006143 cell culture medium Substances 0.000 claims description 8
- 239000000126 substance Substances 0.000 claims description 6
- 239000012466 permeate Substances 0.000 claims description 5
- 230000002401 inhibitory effect Effects 0.000 claims description 4
- 210000004027 cell Anatomy 0.000 description 31
- 239000000243 solution Substances 0.000 description 17
- 239000000725 suspension Substances 0.000 description 13
- 239000000047 product Substances 0.000 description 9
- 239000002699 waste material Substances 0.000 description 6
- 238000012258 culturing Methods 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 230000002503 metabolic effect Effects 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- 238000004114 suspension culture Methods 0.000 description 5
- 239000001963 growth medium Substances 0.000 description 4
- 239000011148 porous material Substances 0.000 description 4
- 210000004102 animal cell Anatomy 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000003094 microcapsule Substances 0.000 description 3
- 210000002966 serum Anatomy 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
- 238000004115 adherent culture Methods 0.000 description 2
- 150000001413 amino acids Chemical class 0.000 description 2
- 239000003242 anti bacterial agent Substances 0.000 description 2
- 229940088710 antibiotic agent Drugs 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- UBAZGMLMVVQSCD-UHFFFAOYSA-N carbon dioxide;molecular oxygen Chemical compound O=O.O=C=O UBAZGMLMVVQSCD-UHFFFAOYSA-N 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000012531 culture fluid Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 229920000642 polymer Polymers 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- 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
- 210000000628 antibody-producing cell Anatomy 0.000 description 1
- 239000003443 antiviral agent Substances 0.000 description 1
- 239000012736 aqueous medium 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
- 230000001413 cellular effect Effects 0.000 description 1
- 229920002301 cellulose acetate Polymers 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000012364 cultivation method Methods 0.000 description 1
- 238000012136 culture method Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000001419 dependent 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
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 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
- 229940079322 interferon Drugs 0.000 description 1
- 238000012007 large scale cell culture Methods 0.000 description 1
- 239000002609 medium Substances 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
- 230000035515 penetration Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 229920002492 poly(sulfone) Polymers 0.000 description 1
- 229920002239 polyacrylonitrile Polymers 0.000 description 1
- 230000002062 proliferating effect Effects 0.000 description 1
- 230000035755 proliferation Effects 0.000 description 1
- 239000012679 serum free medium Substances 0.000 description 1
- 230000008685 targeting Effects 0.000 description 1
- 229960005486 vaccine Drugs 0.000 description 1
Landscapes
- 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器に
関するものである。さらに詳しくは、大規模に細
胞培養を行うに適した容器に関するものであり、
効率よく細胞に栄養分を与え、一方副生する物質
を除去する目的で作られたサスペンジヨン型細胞
培養システムにおける細胞培養器に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION (a) Industrial Application Field The present invention relates to an incubator for culturing and proliferating cells. More specifically, it relates to a container suitable for carrying out cell culture on a large scale,
This invention relates to a cell culture vessel in a suspension type cell culture system that is designed to efficiently supply nutrients to cells while removing by-product substances.
(b) 従来技術
大規模による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製造に必
須である。殊に近年特定タンパク質を標的とする
モノクローナル抗体の生産は抗体産生細胞とミエ
ローマによるハイブリドーマ大量培養によるもの
であり、その技術の解決は工業的に重要なテーマ
である。(b) Prior art For example, large-scale cell culture using viruses,
It is essential for the production of vaccines, antiviral agents such as interferon, and biological drugs such as hormones. Particularly in recent years, the production of monoclonal antibodies targeting specific proteins has been achieved by mass culturing hybridomas of antibody-producing cells and myeloma, and solving this technology is an industrially important theme.
従来細胞培養は一般にシヤーレ試験管、培養び
んなどを用いて実験室的規模で行なわれている。 Conventionally, cell culture is generally carried out on a laboratory scale using Schare test tubes, culture bottles, and the like.
一方近年細胞の大量培養法及びそのための装置
として、いくつかの提案がなされている。これら
の提案は、大きく分けて付着培養(anchorage
dependent culture)と浮遊培養、つまりサスペ
ンジヨン培養(suspension culture)との2つの
方式に分類される。しかし細胞の大量培養法とし
ては、そのほとんどが前者の付着培養による方式
である。この付着培養による方式は、細胞への栄
養分の補給、副生する老廃物の除去等に問題があ
り、細胞の培養に好適な環境条件を作り大量培養
に採用することは、未だ多くの克服すべき点を有
していた。殊に、動物細胞の培養に関しては、一
層不明の点を有していた。 On the other hand, in recent years, several proposals have been made regarding mass culture methods for cells and devices for the same. These proposals can be broadly divided into attached culture (anchorage culture).
It is classified into two types: dependent culture and suspension culture. However, most of the methods for mass culturing cells are the former method, which relies on adherent culture. This method of adherent culture has problems in supplying nutrients to cells and removing by-product waste, and there are still many hurdles to overcome before creating environmental conditions suitable for cell culture and adopting it for mass culture. It had the right points. In particular, the culture of animal cells has remained unclear.
一方サスペンジヨン培養によつて細胞を培養す
る方法に関して、最近いくつかの提案があり、例
えばマグネテイツクスターラーもしくは機械的に
駆動されるシヤフト上の羽根車によつて、スピナ
ーフラスコの中に調整された攪拌機能を設けた培
養方法などが提案されている(例えば特開昭57―
65180号公報参照)。 On the other hand, there have been several recent proposals regarding how to culture cells by suspension culture, for example by means of a magnetic stirrer or an impeller on a mechanically driven shaft, arranged in a spinner flask. Cultivation methods equipped with a stirring function have been proposed (for example, in Japanese Patent Laid-Open No. 1983-1989).
(See Publication No. 65180).
しかし上記の方法においては、一定量の栄養分
の中で培養器されるため細胞の生長増殖は比較的
低い密度で停止する。 However, in the above method, since the cells are incubated in a constant amount of nutrients, their growth and proliferation stop at a relatively low density.
(c) 発明の構成
そこで本発明者らは、前記した如き従来法にお
ける欠点を克服し、サスペンジヨン培養によつ
て、大量且つ高密度の培養が可能な培養器につい
て研究を進めた結果、本発明に到達した。(c) Structure of the Invention The present inventors have overcome the drawbacks of the conventional methods described above and conducted research on an incubator that can perform suspension culture in large quantities and at high density. invention has been achieved.
すなわち、本発明はサスペンジヨン型細胞培養
器であり、該培養器中には細胞培養に必要な栄養
分及び生育阻害物質を実質的に透過するが細胞は
実質的に透過しない壁膜を有する中空糸の多数よ
りなる毛管束及び該毛管束はそれを保護するため
の支持体によつて支持され、該支持体と該毛管束
の端末は固着層によつて固着されたユニツトの少
くとも1個が収納され、該ユニツトの一端には導
管に結合された細胞培養液流入口及び他端には導
管に結合された細胞培養液流出口が設けられてい
る細胞培養器である。 That is, the present invention is a suspension type cell culture device, and the culture device includes a hollow fiber having a wall membrane that substantially permeates nutrients and growth inhibitory substances necessary for cell culture, but does not substantially permeate cells. The capillary bundle is supported by a support for protecting the capillary bundle, and the support and the end of the capillary bundle have at least one unit fixed by a fixing layer. The cell culture vessel is housed in a cell culture vessel and is provided with a cell culture medium inlet connected to a conduit at one end of the unit and a cell culture medium outlet connected to a conduit at the other end.
さらに本発明の細胞培養器は、該ユニツトの少
くとも2個が直列又は並列に接続され、かくする
ことによつて膜透過面積を任意に増減せしめ得る
ようにし、且つその少くとも1個所のユニツトの
一端には導管に結合された細胞培養液流入口及び
他のユニツトの一端には細胞培養液流出口を設け
たものであつてもよい。 Furthermore, in the cell culture device of the present invention, at least two of the units are connected in series or in parallel, so that the membrane permeation area can be increased or decreased as desired, and at least one of the units is connected in series or in parallel. The unit may have a cell culture medium inlet connected to a conduit at one end and a cell culture medium outlet at one end of the other unit.
かくして本発明の培養器においては、サスペン
シヨン型の培養器の液中に、前記ユニツトが沈め
られており、そのユニツトにある毛管束の一端よ
り導管を経て新しい培養液が供給され、中空糸の
壁膜を介して新しい培養液がサスペンジヨン液へ
供給されると共に、細胞が産出した老廃物、代謝
生産物、その他生育阻害物質を含んだ古い培養液
が壁膜を通過してユニツトの他端にある毛管束を
経て培養器の外へ流出されるので、サスペンジヨ
ン液中において細胞の大量、高密度による培養が
容易に可能となる。特に本発明のユニツトは、2
個以上を別々にサスペンジヨン液中に浸入するこ
ともでき、また簡単に2個以上を直列又は並列に
連結して使用することもできるので、細胞の種類
と密度、培養条件、培養の規模の変化に応じて容
易に毛細管の壁膜の面積を適応させることが可能
である。 Thus, in the incubator of the present invention, the unit is submerged in the liquid of the suspension type incubator, and a new culture medium is supplied from one end of the capillary bundle in the unit through the conduit, and the hollow fibers are New culture fluid is supplied to the suspension fluid through the wall membrane, and old culture fluid containing waste products, metabolic products, and other growth-inhibiting substances produced by the cells passes through the wall membrane and is transferred to the other end of the unit. Since the cells flow out of the incubator through the capillary bundle in the suspension, it becomes possible to easily culture a large amount of cells at high density in the suspension liquid. In particular, the unit of the present invention has two
Two or more cells can be immersed separately into the suspension solution, or two or more cells can be easily connected in series or in parallel. It is possible to easily adapt the area of the capillary wall membrane in response to changes.
本発明の細胞培養器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、細
胞自体が或いはそれをマイクロキヤリアに担持し
て水性媒体中で浮遊しながら、懸濁状態で生育さ
れる培養方法を云い、細胞は植物細胞、動物細
胞、微生物細胞のいずれであつてもよく、さらに
人為的に或いは遺伝子操作により変性された細胞
であつてもよく、殊に本発明の培養器は動物細胞
の培養に適している。培養液中には無機塩、ブド
ウ糖、種々のアミノ酸、抗生物質などの細胞培養
に用いられる添加物を加えることができる。また
血清を加えることもできるし、血清を用いない所
謂無血清培地を培養液として用いることもでき
る。 The cell culture device of the present invention is applied to suspension-type cell culture, and suspension-type cell culture means that the cells themselves or supported on microcarriers are grown in a suspended state while floating in an aqueous medium. The cells may be plant cells, animal cells, or microbial cells, and may also be cells that have been modified artificially or by genetic manipulation. is suitable for culturing animal cells. Additives used in cell culture, such as inorganic salts, glucose, various amino acids, and antibiotics, can be added to the culture solution. Further, serum can be added, or a so-called serum-free medium without serum can also be used as the culture medium.
さらに細胞はそれ自体浮遊させてもよく、また
細胞を微小担体(マイクロキヤリアー)の表面上
に付着させて、その付着物を懸濁させて生育する
方法であつてもよくまたマイクロカプセルによる
方式であつてもよい。 Furthermore, the cells may be allowed to float themselves, or may be grown by attaching the cells to the surface of microcarriers and suspending the attached matter.Also, the cells may be grown by a method using microcapsules. It may be.
本発明のユニツトを構成している中空糸毛管
は、種々の重合体よりなるものであればよく、そ
の重合体としては例えばセルロースアセテート、
ポリスルホン、ポリアクリロニトリル、弗素系ポ
リマーなどが挙げられる。 The hollow fiber capillary constituting the unit of the present invention may be made of various polymers, such as cellulose acetate,
Examples include polysulfone, polyacrylonitrile, and fluorine-based polymers.
中空糸毛管の壁膜には多数の微細孔を有してお
り、その毛管の壁膜は、栄養分及び細胞の老廃
物、代謝生産物などを透過するが、細胞或いはそ
れが付着した微小担体又は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 wall of the hollow fiber capillary has many micropores, and the wall of the capillary is permeable to nutrients, cell waste products, metabolic products, etc. Microcapsules are provided with many pores that are sized to prevent penetration. When the cells themselves are cultured in suspension, the size of the pores depends on the size of the cells, but generally an average pore size of 10 μm or less, preferably 8 μm or less is suitable. On the other hand, when cells are cultured by adhering to the surface of microcarriers (microcarriers) or when cells are cultured using microcapsules, the pores need to be of a size that does not allow them to pass through.
また、該毛管の壁膜は、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、該壁膜
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 capillary wall membrane has the ability to permeate water to some extent. That is, it is advantageous for the wall membrane to have a water permeability coefficient (ml/m 2 ·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
10000 or less is desirable.
さらに該壁膜としては、栄養分や細胞の老廃
物、代謝生産物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。 Furthermore, the wall membrane is 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 (for example, 1000 or more, preferably 5000 or more) to pass through. It is also possible to use filter membranes.
以下添付図面により本発明の培養器を更に詳細
に説明する。 The incubator of the present invention will be explained in more detail below with reference to the accompanying drawings.
第3図は、本発明の細胞培養器の全体を示す該
略図の一例を示すものであり、第1は、本発明の
細胞培養器に使用されるユニツトの一例の側外観
図、第2図はそのユニツトの断面図を示すもの
で、また第4図は、本発明のユニツトの他の例の
側外観図及びユニツトを直列に連結した一例を示
すものである。 FIG. 3 shows an example of the schematic diagram showing the entire cell culture device of the present invention, the first is a side external view of an example of a unit used in the cell culture device of the present invention, and FIG. 4 shows a sectional view of the unit, and FIG. 4 shows a side external view of another example of the unit of the present invention and an example in which the units are connected in series.
第1図のユニツト及びその断面図を示した第2
図において、2は中空糸であり、支持体1中にそ
の中空糸が多数束を形成し、平行して充填されて
いる。第1図のユニツトの支持体1の側面には多
数の穴1′が設けられており、この穴1′より培養
液か流通し、中空糸毛管束の壁膜と接触するよう
になつている。この第1図のユニツトにおいて穴
1′は円形をしているが、この穴は培養液が流通
しさえすればよく、他の形状であつてもよい。例
えば第4図に示されているように四角形、長方
形、細長い矩形であつてもよく、その他の三角
形、楕円形等又はこれらの組合せであつてもよ
い。支持体1は中空糸毛管束を支持することが可
能であればよく、第1図の如く筒形である必要は
なく、中空糸の毛管壁膜と培養液を効果的に接触
させる機能を有していればよい。更に支持体1
は、これを直列又は並列に接続する場合の接続機
能をその端部に合せ有することも出来る。 The unit shown in Fig. 1 and its sectional view are shown in Fig. 2.
In the figure, reference numeral 2 indicates hollow fibers, and the hollow fibers form a large number of bundles in the support 1 and are packed in parallel. A large number of holes 1' are provided on the side surface of the support 1 of the unit shown in FIG. 1, and the culture solution flows through these holes 1' and comes into contact with the wall membrane of the hollow fiber capillary bundle. . In the unit shown in FIG. 1, the hole 1' is circular, but the hole may have any other shape as long as the culture solution can flow therethrough. For example, as shown in FIG. 4, it may be a square, a rectangle, or an elongated rectangle, or it may be a triangle, an ellipse, etc., or a combination thereof. The support 1 only needs to be capable of supporting the hollow fiber capillary bundle, and does not need to be cylindrical as shown in Fig. 1. It is enough if you have it. Furthermore, support 1
can also have a connection function at its end when connecting them in series or in parallel.
第3図において4は浮遊培養槽の本体であり、
栄養分を含む新しい培養液はその供給槽6からポ
ンプ7により培養液供給導管8を経て、培養槽中
の懸濁液へ設置されたユニツトの一端へ供給され
る。浮遊培養槽4には細胞がサスペンジヨン液内
を効果的に浮遊するように攪拌装置5が備えられ
ていてもよい。攪拌は5のように回転型攪拌翼に
限らずマグネツトスターラーでもよい。さらにサ
スペンジヨン液中の細胞を効果的に浮遊させるこ
とができる他の攪拌効果を有する手段であつても
よい。一方ユニツトの一端より導入された培養液
は中空糸毛管束を通過し、その壁膜を介してサス
ペンジヨン液中へ栄養分などを含む新しい培養液
が供給されると共に、細胞の老廃物、代謝生産物
などを含む古い培養液は毛管へ透過し、ユニツト
の他端を経て浮遊培養槽外へ導管8′により取出
される。 In Fig. 3, 4 is the main body of the floating culture tank;
Fresh culture medium containing nutrients is supplied from its supply tank 6 by means of a pump 7 via a medium supply conduit 8 to one end of the unit installed in the suspension in the culture tank. The suspension culture tank 4 may be equipped with a stirring device 5 so that the cells are effectively suspended in the suspension liquid. Stirring is not limited to the rotary stirring blade as in 5, but may also be a magnetic stirrer. Furthermore, other means having a stirring effect that can effectively suspend the cells in the suspension liquid may be used. On the other hand, the culture solution introduced from one end of the unit passes through the hollow fiber capillary bundle, and new culture solution containing nutrients is supplied to the suspension solution through the wall membrane, as well as cell waste products and metabolic production. The old culture solution, including substances, permeates into the capillary tube and is removed via the other end of the unit and out of the suspension culture tank by a conduit 8'.
本発明の培養器を用いて実際に培養を行う場合
には、前記ユニツトにおける新しい培養液の流入
口と、古い培養液の流出口とは、必要に応じて逆
にし、該流入口より古い培養液を取り出し、該流
出口より新しい培養液を導入することも可能であ
る。 When actually culturing using the incubator of the present invention, the inlet of the new culture solution and the outlet of the old culture solution in the unit are reversed as necessary, and the inlet of the inlet of the old culture solution is It is also possible to take out the liquid and introduce a new culture medium through the outlet.
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
細胞培養器にもこれらの装置が備えられてもよい
ことは云うまでもない。しかし第3図にはこれら
の付属装置は省略されている。 Furthermore, the culture tank is generally equipped with devices that measure the concentrations of oxygen, carbon dioxide, nutrients, and PH values and maintain them within a certain range, and the cell culture device of the present invention also incorporates these devices. Needless to say, it may be provided. However, these accessories are omitted from FIG.
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、タン白質の如き栄養源、種々
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。これら成分は必要な全てを培養
液としてユニツトを通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サスペンジヨン
液中へ導入することも可能である。一般に細胞培
養には、酸素、二酸化炭素なども必要であるが、
これらは新しい培養液に溶存させて供給してもよ
く、さらに直接サンペンジヨン液へ供給してもよ
い。 The new culture solution supplied to the culture tank of the present invention is
An aqueous solution containing nutrients such as glucose and protein, various amino acids, inorganic salts, antibiotics, and other components necessary for cell culture is used, but it may also contain serum. You don't have to be there. All of these components may be supplied through the unit as a culture solution, but some components may also be introduced into the suspension solution by other supply means. Generally, cell culture requires oxygen, carbon dioxide, etc.
These may be supplied dissolved in a fresh culture solution, or may be supplied directly to the sampendion solution.
第4図は、本発明におけるユニツトの4個を直
列に結いだ例を示したものであり、各ユニツトに
おける支持体には、それぞれ第4図に示す如き
種々の形状の穴がその側面に設けられ、各ユニツ
トはユニツト接続導管9によつて結合されてい
る。3は短管である。 Fig. 4 shows an example in which four units of the present invention are connected in series, and holes of various shapes as shown in Fig. 4 are provided on the sides of the support of each unit. and each unit is connected by a unit connecting conduit 9. 3 is a short tube.
以上説明した本発明の細胞培養器によれば、サ
スペンジヨン型の培養において、連続的に培養液
を供給でき、且つ連続的に老廃物、代謝生産物、
生育阻害物質などを除去できるので、高密度でし
かも大量の細胞を培養することが可能となる。さ
らに本発明のユニツトは単に2個以上或いはこれ
を直列又は並列、或いは独立して2本以上を適当
に組合せて装置の規模、細胞の種類、培養条件な
どに合せながら使用することが容易であるという
利点がある。 According to the cell culture device of the present invention described above, in suspension-type culture, a culture solution can be continuously supplied, and waste products, metabolic products,
Since growth-inhibiting substances can be removed, it becomes possible to culture a large number of cells at high density. Furthermore, the units of the present invention can be easily used by simply combining two or more units, in series or in parallel, or by combining two or more units independently to suit the scale of the device, cell type, culture conditions, etc. There is an advantage.
第1図は本発明の細胞培養器に使用されるユニ
ツトの一例の外観図であり、第2図はその断面図
を示すものである。第3図は、本発明の細胞培養
器の全体を示す該略図の一例を示すものである。
第4図は該ユニツトを直列に結合した一例を示し
たものである。
FIG. 1 is an external view of an example of a unit used in the cell culture device of the present invention, and FIG. 2 is a sectional view thereof. FIG. 3 shows an example of a schematic diagram showing the entire cell culture device of the present invention.
FIG. 4 shows an example in which the units are connected in series.
Claims (1)
器中には細胞培養に必要な栄養分及び生育阻害物
質を実質的に透過するが細胞は実質的に透過しな
い壁膜を有する中空糸の多数よりなる毛管束及び
該毛管束はそれを保護するための支持体によつて
支持され、該支持体と該毛管束の端末は固着層に
よつて固着されたユニツトの少くとも1個が収納
され、該ユニツトの一端には導管に結合された細
胞培養液流入口及び他端には導管に結合された細
胞培養液流出口が設けられている細胞培養器。 2 該ユニツトの少くとも2個が直列又は並列に
接続することによつて膜透過面積を増減せしめ得
るようにしたユニツト連結導管を形成し、且つそ
の少くとも1個所の筒の端末に細胞培養液流入口
及び他の端末に細胞培養液流出口を設けた第1項
記載の細胞培養器。[Scope of Claims] 1. A suspension-type cell culture vessel, which has a wall membrane that substantially permeates nutrients and growth-inhibiting substances necessary for cell culture, but substantially impermeable to cells. A capillary bundle consisting of a large number of hollow fibers, and the capillary bundle is supported by a support for protecting it, and the support and the end of the capillary bundle are connected to at least one of the units fixed by a fixing layer. A cell culture vessel in which a cell culture medium is housed, and the unit is provided with a cell culture medium inlet connected to a conduit at one end and a cell culture medium outlet connected to the conduit at the other end. 2 At least two of the units are connected in series or in parallel to form a unit connecting conduit that can increase or decrease the membrane permeation area, and at least one end of the tube is provided with a cell culture medium. 2. The cell culture device according to claim 1, wherein the inlet and the other terminal are provided with a cell culture solution outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1095484A JPS60156378A (en) | 1984-01-26 | 1984-01-26 | Culture medium of cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1095484A JPS60156378A (en) | 1984-01-26 | 1984-01-26 | Culture medium of cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60156378A JPS60156378A (en) | 1985-08-16 |
| JPS6212989B2 true JPS6212989B2 (en) | 1987-03-23 |
Family
ID=11764581
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1095484A Granted JPS60156378A (en) | 1984-01-26 | 1984-01-26 | Culture medium of cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60156378A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2507552B2 (en) * | 1988-08-29 | 1996-06-12 | 株式会社ニッショー | Method for removing cell culture product and changing medium |
| JPH0269179A (en) * | 1988-09-02 | 1990-03-08 | Nissho Corp | Method for gas-exchange of cell culture medium |
| JPH0272867A (en) * | 1988-09-07 | 1990-03-13 | Nissho Corp | Method for exchanging cell culture medium |
-
1984
- 1984-01-26 JP JP1095484A patent/JPS60156378A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60156378A (en) | 1985-08-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5079168A (en) | Cell culture apparatus | |
| US5416022A (en) | Cell culture apparatus | |
| US5270207A (en) | Circulatory culture equipment | |
| EP0531631B1 (en) | Cell culture apparatus | |
| US20160319234A1 (en) | Continuously controlled hollow fiber bioreactor | |
| CA1210352A (en) | Static cell culture maintenance system | |
| EP0416061B1 (en) | Cell culture unit with APPARATUS FOR OXYGENATING CULTURE MEDIUM | |
| US20030054544A1 (en) | Oxygen enriched bioreactor and method of culturing cells | |
| JPS62130683A (en) | Method and apparatus for culturing cell | |
| JPS6212989B2 (en) | ||
| JPH06102013B2 (en) | Bioreactor | |
| KR100575461B1 (en) | Biological culture apparatus and method | |
| Meng et al. | Hepatocyte culture in bioartificial livers with different membrane characteristics | |
| JPS6212990B2 (en) | ||
| JP3641123B2 (en) | Virus or cell culture method | |
| JPH0428352B2 (en) | ||
| Reiter et al. | High density microcarrier culture with a new device which allows oxygenation and perfusion of microcarrier cultures | |
| JPH0229310B2 (en) | ||
| JPS6233878B2 (en) | ||
| JPS6156075A (en) | Cultivation of human-human hybridoma | |
| JPH04117600U (en) | Hollow fiber membrane cell culture device | |
| JPH04252175A (en) | Tank of cell culture | |
| JPS63233776A (en) | Cell culture device and cell culture method | |
| Patkar et al. | Department of Chemical Engineering &* Biotechnology Laboratory | |
| JPS63233781A (en) | Cell culture method |