JPH0644857B2 - Cell culture device - Google Patents
Cell culture deviceInfo
- Publication number
- JPH0644857B2 JPH0644857B2 JP22748386A JP22748386A JPH0644857B2 JP H0644857 B2 JPH0644857 B2 JP H0644857B2 JP 22748386 A JP22748386 A JP 22748386A JP 22748386 A JP22748386 A JP 22748386A JP H0644857 B2 JPH0644857 B2 JP H0644857B2
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- Japan
- Prior art keywords
- porous
- cells
- porous body
- cell culture
- 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.)
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Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は、微生物、特にカビや放線菌などの糸状菌、ま
たは動物細胞、植物細胞などを増殖させ、各種抗生物
質、各種酵素、蛋白質、多糖類、生理活性物質、動・植
物ホルモンなどの有用物質を生産させる細胞の培養方法
に適する細胞培養装置に関する。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention is intended to grow microorganisms, particularly filamentous fungi such as molds and actinomycetes, or animal cells, plant cells, etc., to produce various antibiotics, various enzymes, proteins, The present invention relates to a cell culture device suitable for a cell culture method for producing useful substances such as polysaccharides, physiologically active substances, animal and plant hormones.
(従来技術) 従来、糸状菌などの培養には、液体培養法と固体培養某
が用いられており、菌の種類や目的生産物の種類によ
り、液体もしくは固体培養法が選択されている。(Prior Art) Conventionally, a liquid culture method and a solid culture method have been used for culturing filamentous fungi, etc., and a liquid or solid culture method is selected depending on the type of bacteria and the type of target product.
固体培養法の場合、米、ふすまなどの天然物が培地とし
て使用され、主に静置培養で行なわれている。近年、天
然物を培地として用いる固体培養法に代わるものとし
て、スポンジ状物質に培養液を含浸させて静置培養する
方法も報告されている。In the case of the solid culture method, natural products such as rice and bran are used as a medium, and the culture is mainly performed by static culture. In recent years, as an alternative to the solid culture method using a natural product as a medium, a method of impregnating a sponge-like substance with a culture solution and performing static culture has also been reported.
本出願人は特願昭61−106393号において新規な
細胞培養法を提案した。この細胞培養法は、ウレタンフ
ォームをはじめとする合成高分子材料、複合高分子材料
を発泡させたもの、あるいは海綿をはじめとする天然ス
ポンジなどの多孔質物体、さらにホリエステルをはじめ
とする合成繊維、綿をはじめとする天然繊維などの糸
状、レース状、布状、立毛状に加工したものなどの高分
子多孔質物体に、培養液を含浸させ、細胞を接種し、し
かる後、この高分子多孔質物体を振盪、振動、混合など
の操作によって動かすことによって、細胞と培養液およ
び空気(酸素)との接触を高め、細胞を多孔質物体表層
内に一様な生物膜として形成させることによって、細胞
の増殖率を高め、諸酵素の細胞内活性を高め、かつ細胞
外への分泌作用の促進や、また、目的生産物の生産性を
高めること可能とした方法として微生物、生化学分野か
ら注目をあびている。The present applicant has proposed a novel cell culture method in Japanese Patent Application No. 61-106393. This cell culture method is used for synthetic polymeric materials such as urethane foam, foamed composite polymeric materials, or porous materials such as natural sponge such as sponge, and synthetic fibers such as holyester. , Macromolecules such as cotton, natural fibers and other thread-like, lace-like, cloth-like, napped, etc., are impregnated with the culture solution, cells are inoculated, and then the polymer By moving the porous object by shaking, shaking, mixing, etc., to enhance the contact between the cells and the culture solution and air (oxygen), and to form the cells as a uniform biofilm in the surface layer of the porous object. , A method of increasing the growth rate of cells, increasing intracellular activities of various enzymes, promoting extracellular secretory action, and increasing productivity of a target product. It is attracting attention from the academic field.
(発明が解決しようとする問題点) 固体培養法の場合には、固体天然培地のロットによって
培地成分組成が異なるため、増殖菌体量や目的性産物の
収量が大きく変動したり、また、目的生産物が固体培地
中に蓄積されるため、その分離・精製が煩雑となるなど
の欠点を有している。スポンジ状物体に培養液を含浸さ
て静置培養する方法では液体培地中に目的生産物が蓄積
されるためその分離・精製は容易であるが、菌体と培地
および空気との接触が不十分であり、また、物質の移動
が主に拡散によるためその効率が悪く、かつ菌体の生育
が不均一となるため増殖率が低下し、目的生産物の生産
性が押さえられるという問題がある。(Problems to be Solved by the Invention) In the case of the solid culture method, since the composition of the medium components varies depending on the lot of the solid natural medium, the amount of cells to be propagated or the yield of the desired product may vary greatly, or Since the product is accumulated in the solid medium, it has a drawback that the separation / purification becomes complicated. In the method of impregnating the sponge-like object with the culture solution and statically culturing, the target product accumulates in the liquid medium, so separation and purification is easy, but contact between the bacterial cells and the medium and air is insufficient. In addition, there is a problem in that the efficiency of the movement of the substance is poor because it is mainly due to diffusion, and the growth of the cells is non-uniform, so that the proliferation rate is reduced and the productivity of the target product is suppressed.
上記特願昭記載の発明は新規な細胞培養方法であり、上
記従来法と異なり高分子多孔質物体に液体培地を均一に
含浸させ、細胞を接種し、この高分子多孔質物体を振
盪、振動、混合などの操作によって動かすことによっ
て、細胞と培養液および空気(酸素)との接触を高め、
高分子多孔質物体表層内で細胞の増殖率を高め、目的生
産物の生産を高めることを可能とする特徴を有するがこ
れに適する装置が存在しないという問題点がある。即
ち、本発明の目的は、上記特願昭記載の発明のこの特徴
をさらに生かすものとして細胞と培養液を含む高分子多
孔質物体を連続して混練培養し、かつ、連続して細胞と
目的生産物を含む培養液を分離し、それぞれ細胞を含む
高分子多孔質物体と培養液を回収する培養装置を提供す
ることにある。The invention described in the above-mentioned Japanese Patent Application is a novel cell culturing method, which is different from the above-mentioned conventional method, in which a polymeric porous material is uniformly impregnated with a liquid medium, cells are inoculated, and the polymeric porous material is shaken and shaken. By increasing the contact between the cells and the culture solution and air (oxygen)
Although it has a feature that it is possible to increase the growth rate of cells in the surface layer of the porous polymer object and increase the production of the target product, there is a problem that there is no apparatus suitable for this. That is, the object of the present invention is to further utilize the characteristics of the invention described in the above-mentioned Japanese Patent Application No. 1 to 5, by continuously kneading and culturing a polymeric porous body containing cells and a culture solution, and continuously producing cells and objects. It is an object of the present invention to provide a culture device that separates a culture solution containing a product, and collects a polymer porous body containing cells and the culture solution, respectively.
(問題点を解決するための手段) 上述した問題点は本発明の細胞培養装置即ち、圧搾され
ることによつて容積だけが縮小し細かく破砕されない強
度を有する高分子多孔質物体を投入する投入口を一端に
有し、他端に前記高分子多孔質物体を排出する排出口を
有する多孔質物体収容部と、この多孔質物体収容部内に
位置して増殖させようとする細胞と培養液とを含む前記
高分子多孔質物体の混練混合しつつ前記投入口から前記
排出口まで移動させるスクリュー混練翼とを有する細胞
培養装置本体、および 前記排出口から排出された前記高分子多孔質物体を圧搾
してこの高分子多孔質物体に含浸する液体を絞り出す圧
搾装置を備えてなる細胞培養装置によって解決される。(Means for Solving the Problems) The above-mentioned problems are caused by the cell culture apparatus of the present invention, that is, the introduction of a polymeric porous body having a strength that does not shatter into small pieces only by being compressed to reduce the volume. A porous body containing portion having a mouth at one end and an outlet for discharging the polymer porous body at the other end, and cells and a culture solution which are located in the porous body containing portion and are to be proliferated. A cell culture device body having a screw kneading blade that moves from the input port to the discharge port while kneading and mixing the polymer porous object, and squeezing the polymer porous object discharged from the discharge port. This is solved by a cell culture device provided with a squeezing device for squeezing out the liquid impregnated into the polymer porous body.
(作 用) 従来の、細胞培養法、とりわけ、固体培養法にみられる
固体培地に増殖させようとする細胞を接種し、固体培地
を静置させて培養する培養装置と、本発明である高分子
多孔質物体に培養液を含浸させ、増殖させようとする細
胞を接種し、かつ、動かしながら連続して培養する培養
装置との違いは、高分子多孔質物体を動かすことによ
り、含浸培養液を多孔質物体内に均一に分散させると同
時に、高分子多孔質物体表層を空気酸素)と常に接触さ
せることを可能にし、細胞への酸素と培養液の物質移動
を積極的に促進させることによって、連続して細胞を多
孔質物体の表層内に一様な生物膜として増殖させるため
の手段が設けられていることである。すなわち、培養液
と増殖させようとする細胞とを含んだ高分子多孔質物体
を多孔質物体収容部の一端から連続してあるいは回分的
に投入し、この多孔質物体収容部内に設けられたスクリ
ュー混練翼で高分子多孔質物体個々を適度に混練混合さ
せ、温度、湿度が調整された注入気体と常に接触させ細
胞への酸素移動を促進するとともに、培養過程で生じる
発酵熱や炭酸ガスなどを排除し、適切な培養温度維持さ
せ細胞の増殖を促進させることができる。多孔質物体収
容部での細胞の培養期間の設定はスクリュー混練翼のピ
ッチ、ピッチ数およびスクリュー混練軸の回転数を適切
に配置し、制御することにより、多孔質物体収容部の長
さに対する高分子多孔質物体の移動速度を規定すること
により所定の培養期間を与えることができ、高分子多孔
質物体の移動量に合わせて細胞と培養液を含む新しい高
分子多孔質物体を連続して投入することによって連続培
養を行うことができる。(Operation) A culture apparatus for inoculating cells to be proliferated in a conventional solid culture method, in particular, a solid culture method, which is found in a conventional solid culture method, and allowing the solid medium to stand for culturing, and the present invention. The difference from a culture device that impregnates a molecular porous material with a culture solution, inoculates cells to be proliferated, and continuously cultivates while moving is that the polymer porous material is moved to impregnate the culture solution. Is uniformly dispersed in the porous body, and at the same time, the surface layer of the polymer porous body can be constantly brought into contact with air oxygen, and by positively promoting the mass transfer of oxygen and culture medium to cells, Means are provided for continuously growing cells as a uniform biofilm within the surface of the porous body. That is, a polymeric porous body containing a culture solution and cells to be proliferated is continuously or batchwise charged from one end of the porous body storage part, and a screw provided in the porous body storage part The kneading blades appropriately knead and mix the individual polymeric porous objects to promote oxygen transfer to the cells by keeping them in contact with the injected gas whose temperature and humidity are adjusted, as well as the fermentation heat and carbon dioxide gas generated during the culture process. It can be eliminated and the appropriate culture temperature is maintained to promote cell growth. The setting of the cell culture period in the porous object housing part is performed by setting the pitch of the screw kneading blade, the number of pitches and the rotation speed of the screw kneading shaft appropriately, and controlling it to achieve a high value for the length of the porous object housing part. A predetermined culture period can be given by defining the moving speed of the molecular porous object, and new polymeric porous objects containing cells and culture solution are continuously added according to the moving amount of the polymeric porous object. By doing so, continuous culture can be performed.
目的生産物収穫の際には増殖した細胞と目的生産物を含
む培養液を保持した高分子多孔質物体を圧搾装置によっ
て圧搾して培養液を絞り出すことによって細胞と培養液
を連続して分離回収することができる。When harvesting the target product, cells and culture liquid are continuously separated and collected by squeezing the culture liquid by squeezing the polymer porous material holding the culture liquid containing the proliferated cells and the target product with a squeezing device. can do.
(発明の効果) 本発明に従い、液体培地を含浸させたウレタンフォーム
をはじめとする高分子多孔質物体に細胞を接種し、この
多孔質物体をスクリュー混練翼によって適切に混練培養
を行うことにより従来の固体培養法のように細胞への酸
素や培地の物質移動過程を律速とせずに培養することが
でき、細胞の増殖率を高め、諸酵素の細胞内活性を高
め、かつ細胞外への分泌作用も促進し、目的生産物の生
産活性を高めることができ、かつ、高分子多孔質物体を
連続してまたは半回分的に細胞培養装置内で移動させ、
連続して圧搾分離することができるので、目的生産物の
生産効率を高めることができる。(Effects of the Invention) According to the present invention, cells are inoculated into a polymer porous body such as urethane foam impregnated with a liquid medium, and the porous body is appropriately kneaded and cultured by a screw kneading blade. Unlike the solid-state culture method described above, cells can be cultured without rate-limiting the oxygen and medium mass transfer processes to the cells, increasing the cell growth rate, increasing the intracellular activity of various enzymes, and secreting them outside the cells. The action can also be promoted, the production activity of the target product can be enhanced, and the polymer porous body can be continuously or semi-batchly moved in the cell culture device,
Since continuous squeeze separation can be performed, the production efficiency of the target product can be increased.
その結果、 1)本発明の細胞培養装置を用いれば各種細胞の細胞増
殖特性に適した培養条件を容易に設定することができ、
特に、従来法に見られる回分操作による固体培養法を連
続して培養させることを可能とし、かつ、目的生産物と
細胞を連続して分離回収することを可能とし工業生産に
多大な効果を与えることができる。As a result, 1) it is possible to easily set culture conditions suitable for the cell growth characteristics of various cells by using the cell culture device of the present invention,
In particular, it makes it possible to continuously culture the solid culture method by batch operation found in the conventional method, and it is possible to continuously separate and recover the target product and cells, which gives a great effect to industrial production. be able to.
2)物質移動過程の改善により、少量の培地で大量の細
胞を増殖させ、工業的に有用な種々の酵素を大量に分泌
させ、有用な目的生産物の生産性を高め、かつ、高濃度
の目的生産物を連続的に培養液から直接分離回収でき、
生産プロセス全体の効率を向上させることが可能とな
る。すなわち、各種細胞による各種抗生物質、各種酵
素、蛋白質、多糖類、生理活性物質、動・植物ホルモン
などの有用物質の生産性を高め、かつ、連続、大量に生
産、分離回収することを容易にした機能集約型バイオリ
アクターということができる。2) By improving the mass transfer process, a large amount of cells can be grown in a small amount of medium, a large amount of various industrially useful enzymes can be secreted, the productivity of useful target products can be increased, and a high concentration of The target product can be continuously separated and collected directly from the culture solution,
It is possible to improve the efficiency of the entire production process. That is, the productivity of useful substances such as various antibiotics, various enzymes, proteins, polysaccharides, physiologically active substances, animal and plant hormones, etc. by various cells can be increased, and continuous, large-scale production, separation and recovery can be easily performed. It can be said that it is a functionally integrated bioreactor.
(実施例) 以下、本発明の実施例を図面を参照しつつ説明する。Embodiments Embodiments of the present invention will be described below with reference to the drawings.
第1図は本発明の細胞培養装置による培養プロセスの好
ましい実施例の構成およびフローシートを示す図であ
る。FIG. 1 is a diagram showing the configuration and flow sheet of a preferred embodiment of the culture process by the cell culture device of the present invention.
細胞培養装置本体Dは基本的に多孔質物体収容部D5と
スクリュー混練翼D2とから成る。多孔質物体収容部D
5には高分子多孔質物体に培養液を無菌的に含浸させ所
定量を供給する多孔質物体供給タンクAより供給ロータ
リーバルブA1及び投入口D3を介して連続的にあるい
はバッチ的に培養液含浸多孔質物体が供給され、また、
増殖させる細胞を多孔質物体に無菌的に接種する細胞供
給タンクBより供給弁B1及び投入口D3を介して培養
液を含んだ高分子多孔質物体が供給されると並行して細
胞が供給され、送風機C1から空調装置C及び投入口D
3を介して温度、湿度が調整された加圧空気が連続して
供給される。供給された細胞と培養液を含む多孔質物体
は多孔質物立収容部D5内で可変速モータD1によって
駆動されるスクリュー混練翼D2により適切に混練混合
され培養が促進される。細胞の増殖後あるいは目的生産
物の生産終了後の高分子多孔質物体は、排出口D4から
円錐型圧搾装置E内へ移送される。そして、この高分子
多孔質物体は、円錐型圧搾装置E内で可変速モータE1
によって駆動される圧搾スクリュー翼E2により培養液
と細胞とに圧搾分離され、培養液は培養液回収タンクF
に、また細胞を含む脱水された高分子多孔質物体は多孔
質物体回収タンクGにそれぞれ分離回収される。細胞培
養装置本体Dの出口に設けられた調圧弁を有する調圧排
気ノズルHおよび培養液回収タンクFに設けられた調圧
排気ノズルF1により細胞培養装置本体Dおよび円錐型
圧搾装置E内の圧力が装置外部より高い圧力に維持され
る。また、目的生産物が細胞内生産物の場合、細胞培養
装置本体Dの出口に配置された無菌洗浄水供給管Iによ
り洗浄水が注入され、細胞を洗浄、圧搾脱水後、高分子
多孔質物体と共に多孔質物体回収タンクGに回収するこ
とができる。The cell culture device body D basically includes a porous object storage portion D5 and a screw kneading blade D2. Porous object storage section D
In FIG. 5, a polymeric porous material is aseptically impregnated with the culture solution, and a predetermined amount is supplied from the porous material supply tank A to continuously or batch-impregnate the culture solution through the supply rotary valve A1 and the inlet D3. A porous body is provided, and also
Cells are supplied in parallel when a macromolecular porous body containing a culture solution is supplied from a cell supply tank B for aseptically inoculating cells to be grown into a porous body via a supply valve B1 and an input port D3. , Blower C1 to air conditioner C and inlet D
Pressurized air whose temperature and humidity are adjusted is continuously supplied via 3. The supplied porous material containing cells and the culture solution is appropriately kneaded and mixed by the screw kneading blade D2 driven by the variable speed motor D1 in the porous material vertical accommodating portion D5 to promote the culture. The polymer porous body after the cells have grown or the target product has been produced is transferred from the outlet D4 into the conical pressing device E. Then, this polymer porous body is provided with a variable speed motor E1 in the conical pressing device E.
The culture solution and cells are squeezed and separated by a squeeze screw blade E2 driven by
In addition, the dehydrated polymer porous body containing cells is separately collected in the porous body recovery tank G. The pressure in the cell culture device body D and the conical squeezing device E is controlled by the pressure control exhaust nozzle H having a pressure control valve provided at the outlet of the cell culture device body D and the pressure control exhaust nozzle F1 provided in the culture solution recovery tank F. Is maintained at a higher pressure than outside the device. When the target product is an intracellular product, washing water is injected through a sterile washing water supply pipe I arranged at the outlet of the cell culture device body D to wash and squeeze and dehydrate the cells, and then the polymeric porous object. At the same time, it can be recovered in the porous object recovery tank G.
第2図は本発明の細胞培養装置の好ましい実施例の詳細
側面図で、第3図はこの細胞培養装置を傾斜させて用い
る場合の実施例の側面図である。FIG. 2 is a detailed side view of a preferred embodiment of the cell culture device of the present invention, and FIG. 3 is a side view of the embodiment when the cell culture device is used while being tilted.
細胞培養装置本体1は片端に細胞と培養液を含んだ高分
子多孔質物体8aが投入され、温度、湿度が調整された
無菌加圧空気が注入される投入口3aと、細胞培養後の
高分子多孔質物体を排出する排出口3bとを有する細胞
を培養する多孔質物体収容部1a、その下端の排出口3
bに接続して設けられ培養終了の細胞を含む高分子多孔
質物体8bを排出する導入管1b、この導入管1bに調
圧排気ノズル1dおよび細胞洗浄水を注入する注入ノズ
ル1cを設けた中空円筒状のものからなる。多孔質物体
収容部1a内に注入された細胞と培養液を含む高分子多
孔質物体8aは、多孔質物体収容部1a片端および導入
管1bに設けられた軸受け1e、1fによって支持され
たスクリュー混練軸2に配列されたスクリュー混練翼2
aが回転することによって適切に混練混合され、投入口
3aから注入される空気と一様に接触し細胞の増殖が促
進され、かつ、多孔質物体収容部1a下流に移動させら
れる。スクリュー混練翼2aに高分子多孔質物体8a、
8bの大きさより小さい目開きの多孔2bを設け多孔翼
とし注入気体の流通を容易とすることができる。また、
スクリュー混練翼2a間に撹拌板2dを設け高分子多孔
質物体の混合をさらに高めることができる。高分子多孔
質物体がスクリュー混練翼2aによって移動させられる
移動量と等量の新しい細胞と培養液を含んだ高分子多孔
質物体8aを投入口3aより連続またはバッチ操作にて
投入することによって、多孔質物体収容部1a内で連続
して細胞を増殖させることができる。細胞の培養期間は
スクリュー混練軸2の回転数とスクリュー混練翼2a間
の混練翼ピッチ2cによって与えられるピッチ速度と多
孔質物体収容部1aの長さによって規定される。したが
って、培養期間の短い細胞の場合は混練翼ピッチ2cを
大きく、また、スクリュー混練軸2の回転数を速くで
き、あるいは、多孔質物体収容部1aの長さを短くする
ことができる。逆に、培養期間の比較的長い細胞の場合
は混練翼ピッチ2cを小さく、また、スクリュー混練軸
2の回転数を遅く、あるいは、多孔質物体収容部1aの
長さを長くすることによって培養期間を長くすることが
できる。さらに、培養期間が長い細胞を培養する場合に
は、多孔質物体収容部1aの投入口3a側を低く傾斜さ
せて配置することにより、高分子多孔質物体8aの自重
を利用し多孔質物体8aをスクリュー混練翼2aよって
移動する方向と逆の方向に移動させスクリュー混練翼2
a間に滞留させ、投入口3aから注入された高分子多孔
質物体8aによる投入口側からの押し出しにより投入量
だけを多孔質物体収容部1aの排出口3b導入管1bに
排出することができる。この場合の培養期間は多孔質物
体収容部1aに保有される高分子多孔質物体8a,8b
の量と投入量から規定される。また、スクリュー混練軸
2の回転数を一時的に速くし、培養終了細胞を含む高分
子多孔質物体8bの一部、望ましくは導入管1bおよび
円錐型圧搾装置4における多孔質物体8bの保有容量に
等しい量を排出し、これと等量の新しい細胞と培養液を
含む高分子多孔質物体8aを投入口3aよりバッチ操作
にて投入することにより半回分培養することができる
(図3参照)。さらに、多孔質物体収容部1aを積層
し、U字形状を有する多孔質物体導入管1bを接続させ
ることによって多孔質物体収容部1aの長さを長くして
培養期間を長くすることもできる(図面省略)。多孔質
物体収容部1aの周囲には恒温ジャケット7が設けられ
ており、下方の入口7aから上方の出口7bへ恒温水を
流すことにより多孔質物体収容部1a内部が一定の温度
に保持されて最適の温度で培養が促進されるようになっ
ている。The cell culture device body 1 has a polymeric porous body 8a containing cells and a culture solution at one end, and an inlet 3a into which sterile pressurized air whose temperature and humidity have been adjusted is injected, and a height after cell culture. Porous substance accommodating portion 1a for culturing cells having an outlet 3b for discharging a molecular porous substance, and an outlet 3 at the lower end thereof
Introducing tube 1b connected to b for discharging a polymeric porous object 8b containing cells after culturing, a hollow provided with an inlet nozzle 1c for injecting a pressure-controlled exhaust nozzle 1d and cell washing water to this introducing tube 1b. It consists of a cylindrical shape. The polymer porous body 8a containing the cells and the culture solution injected into the porous body containing portion 1a is kneaded with a screw supported by bearings 1e, 1f provided at one end of the porous body containing portion 1a and the introduction tube 1b. Screw kneading blade 2 arranged on shaft 2
When a is rotated, it is appropriately kneaded and mixed, uniformly contacts the air injected from the input port 3a, promotes cell growth, and is moved to the downstream of the porous object housing portion 1a. The screw kneading blade 2a has a polymer porous body 8a,
It is possible to facilitate the flow of the injected gas by providing the perforated blades 2b with openings smaller than the size of 8b to form perforated blades. Also,
A stirring plate 2d may be provided between the screw kneading blades 2a to further enhance the mixing of the polymer porous body. By pouring the polymer porous body 8a containing the new cells and the culture liquid in the same amount as the moving amount by which the polymer porous body is moved by the screw kneading blade 2a from the charging port 3a in a continuous or batch operation, It is possible to continuously grow cells in the porous object storage portion 1a. The cell culturing period is defined by the rotation speed of the screw kneading shaft 2, the pitch speed given by the kneading blade pitch 2c between the screw kneading blades 2a, and the length of the porous object accommodating portion 1a. Therefore, in the case of cells having a short culture period, the kneading blade pitch 2c can be increased, the rotation speed of the screw kneading shaft 2 can be increased, or the length of the porous object accommodating portion 1a can be shortened. Conversely, in the case of cells having a relatively long culturing period, the kneading blade pitch 2c is made small, the rotation speed of the screw kneading shaft 2 is slowed, or the length of the porous object accommodating portion 1a is lengthened to make the culturing period longer. Can be lengthened. Furthermore, when culturing cells having a long culturing period, by arranging the inlet 3a side of the porous object accommodating portion 1a with a low inclination, the self-weight of the polymeric porous object 8a is utilized to make the porous object 8a. The screw kneading blade 2a by moving the screw kneading blade 2a in a direction opposite to the direction in which the screw kneading blade 2a moves.
It is possible to discharge only the input amount into the discharge port 3b introduction pipe 1b of the porous object accommodating portion 1a by allowing the polymer porous substance 8a injected from the input port 3a to be retained between a and pushed out from the injection port side. . In the culture period in this case, the polymeric porous objects 8a and 8b held in the porous object housing portion 1a are used.
It is regulated from the amount and the input amount. Further, the rotation speed of the screw kneading shaft 2 is temporarily increased, and a part of the polymer porous body 8b containing the cells after the culturing, preferably, the holding capacity of the introduction body 1b and the porous body 8b in the conical squeezing apparatus 4. A semi-batch culture can be carried out by discharging a polymer porous body 8a containing the same amount of new cells and a culture solution as the above through a batch operation from the charging port 3a (see FIG. 3). . Further, by stacking the porous object storage portion 1a and connecting the U-shaped porous object introduction tube 1b, the length of the porous object storage portion 1a can be increased to prolong the culture period ( Drawing omitted). A constant temperature jacket 7 is provided around the porous object storage portion 1a, and by supplying constant temperature water from the lower inlet 7a to the upper outlet 7b, the inside of the porous object storage portion 1a is maintained at a constant temperature. The culture is promoted at the optimum temperature.
目的生産物収穫の際には、導入管1bに接続された円錐
型圧搾装置4に培養期間の終了した細胞と目的生産物を
含む多孔質物体8bが導入され、細胞と培養液に圧搾分
離される。At the time of harvesting the target product, the porous object 8b containing the cells and the target product after the culturing period is introduced into the conical pressing device 4 connected to the introduction pipe 1b, and the cells and the culture solution are squeezed and separated. It
円錐型圧搾装置4は多孔質物体導入開口部および下端部
多孔質物体排出管4cに設けられた軸受け4e、4dに
よって支持された圧縮スクリュー軸5に配置された全体
の形状がテーパ形状を有する圧搾スクリュー翼5a、こ
の圧搾スクリュー翼5aの先端に接するように配置され
た多孔4bを有する円錐型多孔管4a、この円錐型多孔
管4aの外周に設けられた培養液回収部6からなる。圧
搾スクリュー翼5のスクリュー翼の径は、高分子多孔質
物体の移送方向に従って小さくなっており、圧搾スクリ
ュー翼5は円錐型多孔管4a内に勘合して配置されてい
る。圧搾スクリュー翼5aのピッチ間は下端方向に行く
にしがって小さく、導入された高分子多孔質物体8bは
下端に行くにしたがって容積が圧搾縮小され、含浸して
いた培養液は円錐型多孔管4aに設けられた多孔4bか
ら絞り出され、培養液回収部6に集合し培養液排出ノズ
ル6aから排出される。細胞を含む圧搾脱水された高分
子多孔質物体8cは下端に設けられた排出管4cから排
出される。目的生産物が細胞内生産物の場合導入管1b
に設けられた注入ノズル1cより連続または半連続的に
無菌洗浄水を注入し、細胞を洗浄しつつ洗浄水と培養液
を圧搾脱水し、脱水された細胞を含む高分子多孔質物体
8cを下端排出管4cより連続または半連続的に分離回
収させることができる。円錐型圧搾装置4で圧搾脱水さ
れる高分子多孔質物体8bの量は、圧搾スクリュー軸5
の回転速度を変えることによって調節することができ
る。The conical squeezing device 4 is a squeezing device having a tapered overall shape, which is arranged on a compression screw shaft 5 supported by bearings 4e and 4d provided on a porous object introduction opening and a lower end porous object discharge pipe 4c. It comprises a screw blade 5a, a conical perforated tube 4a having a perforation 4b arranged so as to be in contact with the tip of the compression screw blade 5a, and a culture solution recovery section 6 provided on the outer circumference of the conical perforated tube 4a. The diameter of the screw blade of the squeezing screw blade 5 becomes smaller according to the transport direction of the polymer porous object, and the squeezing screw blade 5 is fitted in the conical porous tube 4a. The space between the pitches of the squeezing screw blades 5a becomes smaller toward the lower end, and the volume of the introduced polymer porous body 8b is squeezed and reduced toward the lower end, and the impregnated culture solution is a conical perforated tube. It is squeezed out from the perforations 4b provided in 4a, gathers in the culture solution recovery section 6, and is discharged from the culture solution discharge nozzle 6a. The squeezed and dehydrated polymer porous body 8c containing cells is discharged from a discharge pipe 4c provided at the lower end. If the target product is an intracellular product, the introduction tube 1b
Aseptic wash water is continuously or semi-continuously injected from the injection nozzle 1c provided in the above to squeeze and dehydrate the wash water and the culture solution while washing the cells, and the polymer porous body 8c containing the dehydrated cells is placed at the lower end. It can be continuously or semi-continuously separated and collected from the discharge pipe 4c. The amount of the polymeric porous object 8b that is pressed and dehydrated by the conical pressing device 4 is determined by the pressing screw shaft 5
It can be adjusted by changing the rotation speed.
また、培養期間の比較的短い細胞を培養するときには、
第4図にしめすようにスクリュー混練軸2にスクリュー
混練翼2aおよび圧搾スクリュー翼5aを同軸上に配置
し、細胞培養装置本体1と円錐圧搾装置を一体化させる
ことができる。この場合、細胞の培養期間はスクリュー
混練翼2の回転数と混練翼ピッチ2cで与えられるピッ
チ速度と多孔質物体収容部1aの長さによって規定され
る。また、円錐型圧搾装置への導入部上部に調圧排気ノ
ズル1dおよび洗浄水注入ノズル1cが配置される。When culturing cells with a relatively short culture period,
As shown in FIG. 4, the screw kneading shaft 2 can be coaxially arranged with the screw kneading blade 2a and the pressing screw blade 5a to integrate the cell culture device body 1 and the conical pressing device. In this case, the cell culturing period is defined by the rotation speed of the screw kneading blade 2, the pitch speed given by the kneading blade pitch 2c, and the length of the porous object storage portion 1a. In addition, a pressure regulating exhaust nozzle 1d and a wash water injection nozzle 1c are arranged above the introduction portion to the conical pressing device.
本発明で用いられる高分子多孔質物体は、圧搾されるこ
とによって容積だけが縮小し細かく破砕されない強度を
有するものであれば足り、例えばウレタンフォームのよ
うな材質であれば良いが、特に限定されない。高分子多
孔質物体の大きさは一辺の長さ或いは直径が2.5mm〜
20mmのものが好ましい。The polymer porous body used in the present invention is sufficient if it has a strength such that only the volume is reduced by being squeezed and is not finely crushed, and it may be a material such as urethane foam, but is not particularly limited. . The size of the porous polymer object is 2.5 mm on a side or the diameter.
20 mm is preferable.
上述された各実施例においては、高分子多孔質物体に含
浸する培養液を絞り出す圧搾装置として、円錐多孔管と
テーパー形の圧搾スクリュー翼とから成る円錐型圧搾装
置が用いられたが、一対の円柱状ロールが対向して配置
され、このロール間に多孔質物体を通過させてこれを圧
搾する様にした別の圧搾装置を使用できることは言うま
でもない。In each of the above-mentioned examples, as the squeezing device for squeezing the culture solution impregnating the polymer porous body, a conical squeezing device consisting of a conical porous tube and a tapered squeezing screw blade was used. It goes without saying that it is possible to use another squeezing device in which the cylindrical rolls are arranged so as to face each other and the porous body is passed between the rolls to squeeze it.
第1図は本発明の細胞培養装置による培養プロセスの好
ましい実施例の構成およびフローシートを示す図、 第2図は本発明の細胞培養装置の好ましい実施例の詳細
側面図、 第3図は第2図の細胞培養装置を傾斜させて用いる場合
の実施側の側面図、および 第4図は本発明の細胞培養装置の別の実施例の詳細側面
図である。 A……多孔質物体供給タンク B……細胞供給タンク C……空調装置、C1……送風機 D……細胞培養装置本体 D1……可変速モータ D2……スクリュー混練翼 D3……投入口 D4……排出口 D5……多孔物質収容部 E……円錐型圧搾装置 E1……可変速モータ E2……圧搾スクリュー翼 F……培養液回収タンク F1……調圧排気ノズル G……多孔質物体回収タンク H……調圧排気ノズル I……洗浄水注入ノズル 1……細胞培養装置本体 1a……多孔質物体収容部 1b……導入管 1c……洗浄水注入ノズル 1d……調圧排気ノズル 2……スクリュー混練軸 2a……スクリュー混練翼、2b……多孔 2c……混練翼ピッチ 2d……撹拌板、3a……投入口、3b……排出口 4……円錐圧搾装置 4a……円錐型多孔管 4b……多孔、4c……排出管 5……圧搾スクリュー軸 5a……圧搾スクリュー翼 6……培養液回収部 7……恒温ジャケット 8a……新しい細胞と培養液含有高分子多孔質物体 8b……培養終了高分子多孔質物体 8c……圧搾脱水後の細胞含有高分子多孔質物体FIG. 1 is a diagram showing a configuration and a flow sheet of a preferred embodiment of the culture process by the cell culture device of the present invention, FIG. 2 is a detailed side view of the preferred embodiment of the cell culture device of the present invention, and FIG. FIG. 2 is a side view of the implementation side when the cell culture device of FIG. 2 is used in a tilted state, and FIG. 4 is a detailed side view of another embodiment of the cell culture device of the present invention. A ... Porous material supply tank B ... Cell supply tank C ... Air conditioner, C1 ... Blower D ... Cell culture device body D1 ... Variable speed motor D2 ... Screw kneading blade D3 ... Input port D4 ... … Discharge port D5 …… Porous substance storage unit E …… Cone type squeezing device E1 …… Variable speed motor E2 …… Squeeze screw blade F …… Culture solution recovery tank F1 …… Pressure adjusting exhaust nozzle G …… Porous substance recovery Tank H ... Pressure-regulating exhaust nozzle I ... Wash water injection nozzle 1 ... Cell culture device body 1a ... Porous object storage part 1b ... Introduction pipe 1c ... Wash water injection nozzle 1d ... Pressure-regulating exhaust nozzle 2 ...... Screw kneading shaft 2a ...... Screw kneading blade 2b ...... Perforation 2c …… Kneading blade pitch 2d …… Stirring plate 3a …… Inlet port 3b …… Discharge port 4 …… Cone squeezing device 4a …… Cone type Perforated tube 4b ... many Holes 4c ... Discharge pipe 5 ... Compressing screw shaft 5a ... Compressing screw blades 6 ... Culture solution collecting section 7 ... Constant temperature jacket 8a ... Polymer cells containing culture medium and new cells 8b. Polymeric porous material 8c ... Cell-containing polymeric porous material after compression dehydration
Claims (4)
細かく破砕されない強度を有する高分子多孔質物体を投
入する投入口を一端に有し、他端に前記高分子多孔質物
体を排出する排出口を有する多孔質物体収容部と、この
多孔質物体収容部内に位置して増殖させようとする細胞
と培養液とを含む前記高分子多孔質物体を混練混合しつ
つ前記投入口から前記排出口まで移動させるスクリュー
混練翼とを有する細胞培養装置本体、および 前記排出口から排出された前記高分子多孔質物体を圧搾
してこの高分子多孔質物体に含浸する液体を絞り出す圧
搾装置を備えてなる細胞培養装置。1. An ejector having at one end an inlet for introducing a polymer porous body having a strength such that the volume is reduced by being squeezed and is not crushed finely, and the other end is for discharging the polymer porous body. A porous object containing portion having an outlet, and the polymer porous object containing cells and a culture solution located in the porous object containing portion to be proliferated and kneading and mixing the mixture from the input port to the outlet. A cell culturing apparatus main body having a screw kneading blade that moves up to, and a squeezing apparatus that squeezes the polymer porous body discharged from the outlet to squeeze the liquid impregnated into the polymer porous body. Cell culture device.
孔管内に嵌合して位置し、前記高分子多孔質物体の移送
方向に従って翼の径が小さくなる全体としてテーパー型
の圧搾スクリュー翼とから成る円錐型圧搾装置である特
許請求の範囲第(1)項記載の細胞培養装置。2. The squeezing device is located in a conical perforated tube and is fitted into the perforated tube. The squeezing screw is of a taper type as a whole in which the diameter of the blade is reduced according to the transfer direction of the polymeric porous object. The cell culture device according to claim (1), which is a conical pressing device including a wing.
物体の大きさより小さい目開きの多孔翼で、かつ翼間に
撹拌板を備えた特許請求の範囲第(1)項または第(2)項記
載の細胞培養装置。3. The screw kneading blade according to claim 1, wherein the screw kneading blade is a porous blade having an opening smaller than the size of the polymeric porous body, and a stirring plate is provided between the blades. The cell culture device according to the item.
くなるように傾斜して配置されている特許請求の範囲第
(1)項ないし第(3)項いずれか1項記載の細胞培養装置。4. The method according to claim 1, wherein the porous object storage portion is arranged so as to be inclined so that the input port side thereof becomes lower.
The cell culture device according to any one of (1) to (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP22748386A JPH0644857B2 (en) | 1986-09-26 | 1986-09-26 | Cell culture device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP22748386A JPH0644857B2 (en) | 1986-09-26 | 1986-09-26 | Cell culture device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6384482A JPS6384482A (en) | 1988-04-15 |
| JPH0644857B2 true JPH0644857B2 (en) | 1994-06-15 |
Family
ID=16861589
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP22748386A Expired - Lifetime JPH0644857B2 (en) | 1986-09-26 | 1986-09-26 | Cell culture device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0644857B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4017979B2 (en) | 2000-10-24 | 2007-12-05 | イー・アイ・デュポン・ドウ・ヌムール・アンド・カンパニー | System and method for removing bulk powder from large bulk containers |
-
1986
- 1986-09-26 JP JP22748386A patent/JPH0644857B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6384482A (en) | 1988-04-15 |
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