JPH1175821A - Biochemical reaction apparatus for culturing several series of cell and biochemical reaction - Google Patents
Biochemical reaction apparatus for culturing several series of cell and biochemical reactionInfo
- Publication number
- JPH1175821A JPH1175821A JP9250105A JP25010597A JPH1175821A JP H1175821 A JPH1175821 A JP H1175821A JP 9250105 A JP9250105 A JP 9250105A JP 25010597 A JP25010597 A JP 25010597A JP H1175821 A JPH1175821 A JP H1175821A
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- Prior art keywords
- cells
- reaction
- reaction solution
- reactor
- cell
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- 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
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/58—Reaction vessels connected in series or in parallel
-
- 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
- C12M35/00—Means for application of stress for stimulating the growth of microorganisms or the generation of fermentation or metabolic products; Means for electroporation or cell fusion
- C12M35/08—Chemical, biochemical or biological means, e.g. plasma jet, co-culture
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- Cell Biology (AREA)
- General Chemical & Material Sciences (AREA)
- Molecular Biology (AREA)
- Clinical Laboratory Science (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、複数種の細胞を反
応液を共有して培養する生化学反応装置及びこれを用い
た生化学反応方法に係り、更に詳細には、一の細胞によ
る反応生産物を他の細胞に作用させて反応させる生化学
反応装置及び生化学反応方法に関するもので、特に生化
学反応による物質変換や物質生産に有効である。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a biochemical reaction apparatus for culturing a plurality of types of cells by sharing a reaction solution and a biochemical reaction method using the same, and more particularly, to a reaction by one cell. The present invention relates to a biochemical reaction apparatus and a biochemical reaction method for causing a product to act on another cell to cause a reaction, and is particularly effective for substance conversion and substance production by a biochemical reaction.
【0002】[0002]
【従来の技術及び発明が解決しようとする課題】従来か
ら、複数の細胞や生理活性物質を収容したリアクターを
直列に連結した反応系が種々用いられている。かかる反
応系では、例えば、嫌気性菌を作用させた反応液を続い
て好気性反応槽に供給したり、1種類の微生物を反応さ
せた後、微生物を濾過し、次の生化学反応に供したりす
ることが行われている。2. Description of the Related Art Conventionally, various reaction systems in which reactors containing a plurality of cells or physiologically active substances are connected in series have been used. In such a reaction system, for example, a reaction solution in which an anaerobic bacterium has acted is subsequently supplied to an aerobic reaction tank, or after reacting one kind of microorganism, the microorganism is filtered and used for the next biochemical reaction. Or that is being done.
【0003】しかしながら、かかる直列反応系において
は、1つの反応を行った後、次の生化学反応に供する前
に、反応液をその反応に適合するように調整する必要が
あった。例えば、好気性反応をさせた後の反応液では、
溶存酸素や基質が消費されているので、次の好気性反応
に供する前に酸素や基質を補給する必要があるという課
題があった。However, in such a series reaction system, after performing one reaction, it is necessary to adjust the reaction solution so as to be suitable for the next biochemical reaction. For example, in the reaction solution after the aerobic reaction,
Since dissolved oxygen and the substrate are consumed, there is a problem that it is necessary to replenish the oxygen and the substrate before the next aerobic reaction.
【0004】一方、動物細胞の培養では、複数種の細胞
を混合して培養し、有用物質を生産した例が報告されて
いる。例えば、肝臓の実質細胞の純粋培養では、アルブ
ミンの生産能は数日で低下するが、星細胞と共培養する
と、アルブミンの生産能は1カ月以上維持できたとの報
告がある。On the other hand, in the case of culturing animal cells, there has been reported an example in which a plurality of types of cells are mixed and cultured to produce a useful substance. For example, it has been reported that in a pure culture of liver parenchymal cells, the ability to produce albumin decreases in a few days, but when co-cultured with stellate cells, the ability to produce albumin could be maintained for one month or more.
【0005】しかしながら、かかる共培養を行うと、増
殖の速い細胞が優勢に増殖して細胞の分布を希望のよう
に制御することが困難であるという課題があり、この現
象は、増殖速度が極端に異なる微生物の共培養系で顕著
である。[0005] However, when such co-culture is performed, there is a problem that rapidly growing cells predominantly proliferate, and it is difficult to control the distribution of cells as desired. This is remarkable in a co-culture system of different microorganisms.
【0006】本発明は、上述のような従来技術の有する
課題に鑑みてなされたものであり、その目的とするとこ
ろは、複数種の細胞を反応液を共有して同時培養ないし
共培養でき、特に、動物細胞や植物細胞の培養におい
て、ある細胞の生産物が他種の細胞の基質や生理活性因
子となり得るような培養系で、各細胞を個別に培養・管
理し得る生化学反応装置及び生化学反応方法を提供する
ことにある。The present invention has been made in view of the above-mentioned problems of the prior art, and an object of the present invention is to allow a plurality of types of cells to be co-cultured or co-cultured by sharing a reaction solution. In particular, in the cultivation of animal cells and plant cells, a biochemical reaction device capable of individually culturing and managing each cell in a culture system in which a product of one cell can be a substrate or a physiologically active factor of another cell, and It is to provide a biochemical reaction method.
【0007】[0007]
【課題を解決するための手段】本発明者は、上記目的を
達成すべく鋭意検討を重ねた結果、反応液調整槽と別個
の細胞又は細胞群を収容した各リアクターとを並列に連
結し、各リアクターから排出された反応液が反応液調整
槽に戻るような構成とすることにより、上記目的が達成
できることを見出し、本発明を完成するに至った。Means for Solving the Problems As a result of intensive studies to achieve the above object, the present inventors have connected a reaction solution adjusting tank and each reactor containing separate cells or cell groups in parallel, The present inventors have found that the above object can be achieved by adopting a structure in which the reaction solution discharged from each reactor returns to the reaction solution adjustment tank, and have completed the present invention.
【0008】即ち、本発明の生化学反応装置は、複数種
の細胞を1種又は2種以上の組み合わせにより個別に収
容する複数個のリアクターと、上記細胞に供給する反応
液を収容した反応液調整槽とを備え、上記反応液調整槽
は上記反応液を上記複数個のリアクターへ並列に送り、
これらリアクターから排出された反応液が上記反応液調
整槽に戻ることにより、上記反応液が上記反応液調整槽
と各リアクター間を循環し、この循環に際し、上記リア
クターから排出された反応液同士が合流し、上記複数種
の細胞が反応液を共用することを特徴とする。That is, the biochemical reaction apparatus of the present invention comprises a plurality of reactors for individually accommodating a plurality of types of cells in one kind or a combination of two or more types, and a reaction solution containing a reaction solution to be supplied to the cells. An adjustment tank, and the reaction solution adjustment tank sends the reaction solution to the plurality of reactors in parallel,
When the reaction liquid discharged from these reactors returns to the reaction liquid adjustment tank, the reaction liquid circulates between the reaction liquid adjustment tank and each reactor, and during this circulation, the reaction liquids discharged from the reactor are separated from each other. The cells are merged, and the plurality of types of cells share a reaction solution.
【0009】また、本発明の生化学反応装置の好適形態
は、上記リアクターの少なくとも1つにおける細胞が、
他のリアクターに移動するのを防止する移動防止手段を
備えることを特徴とする。[0009] In a preferred embodiment of the biochemical reaction device of the present invention, the cells in at least one of the above reactors are:
It is characterized by comprising a movement preventing means for preventing movement to another reactor.
【0010】更に、本発明の生化学反応装置の他の好適
形態は、上記細胞が動物及び/又は植物細胞であること
を特徴とし、特に上記動物細胞が、肝臓を構成する2種
類以上の細胞である場合には、顕著な同時培養ないし共
培養の効果が得られる。Further, another preferred embodiment of the biochemical reaction apparatus of the present invention is characterized in that the cells are animal and / or plant cells, and in particular, the animal cells are two or more kinds of cells constituting a liver. In the case of, a remarkable effect of simultaneous culture or co-culture is obtained.
【0011】また、本発明の生化学反応方法は、上述し
た生化学反応装置を用いることを特徴とする。Further, a biochemical reaction method of the present invention is characterized by using the above-described biochemical reaction device.
【0012】[0012]
【作用】本発明の生化学反応装置及び方法によれば、複
数のリアクター中において、細胞は独立した生化学反応
を共通の反応液又は培養液により行うことできる。ま
た、1つのリアクターにおける生化学反応による生成物
を、他の生化学反応に容易に供することができる。According to the biochemical reaction apparatus and method of the present invention, cells can perform independent biochemical reactions in a plurality of reactors using a common reaction solution or culture solution. In addition, a product of a biochemical reaction in one reactor can be easily supplied to another biochemical reaction.
【0013】[0013]
【発明の実施の形態】以下、本発明について詳細に説明
する。上述の如く、本発明の生化学反応装置は、複数種
の細胞を個別に収容する複数個のリアクターと、これら
細胞に供給する反応液を収容した反応液調整槽とを備え
る。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail. As described above, the biochemical reaction device of the present invention includes a plurality of reactors that individually store a plurality of types of cells, and a reaction solution adjustment tank that stores a reaction solution to be supplied to these cells.
【0014】ここで、リアクターは、培養しようとする
細胞を収容できれば十分であるが、1つのリアクターに
は1種類の細胞を収容してもよいが、複数種の細胞を1
つのリアクターに収容することも可能である。また、本
発明が培養対象とする細胞は、微生物、植物や動物の細
胞であり、これらを収容するリアクターとしては、細胞
を含む培養装置、細胞を固定した担体を収納している容
器や、細胞を空間に封じ込めこの空間に配置したホロー
ファイバーを介してガスや基質を供給するいわゆるホロ
ーファイバー型バイオリアクター及びこれらの組み合わ
せを用いることができる。Here, it is sufficient that the reactor can accommodate the cells to be cultured. One reactor may accommodate one type of cells, but a plurality of types of cells may be accommodated.
It is also possible to accommodate in one reactor. Further, the cells to be cultured by the present invention are microorganisms, plant and animal cells, and as a reactor for accommodating them, a culture device containing cells, a container containing a carrier on which cells are fixed, a cell, A so-called hollow fiber type bioreactor that supplies gas and a substrate through a hollow fiber arranged in this space and a combination thereof can be used.
【0015】また、反応液調整槽は、対象とする細胞が
種々の生化学反応を起こすのに関与する反応液を収容で
きれば十分であり、反応液としては、基質、反応阻害剤
及び生理活性物質などを例示できる。なお、反応液が培
養などで消費されたり、成分変化した場合には、反応液
調整槽に反応液を補給したり、また、一部抜き取って補
給したりすればよい。It is sufficient that the reaction solution adjusting tank can contain a reaction solution involved in causing various kinds of biochemical reactions of target cells. The reaction solution includes a substrate, a reaction inhibitor and a physiologically active substance. And the like. When the reaction solution is consumed in culturing or the like, or the components change, the reaction solution may be supplied to the reaction solution adjusting tank, or a part of the reaction solution may be withdrawn and supplied.
【0016】本発明において、反応液調整槽中の反応液
は、複数のリアクターに対し並列に送られ、これらリア
クターから排出された反応液はこの調整槽へ戻る。即
ち、反応液は反応液調整槽と各リアクターとの間を循環
するが、各リアクターから排出された反応後の反応液
(場合によっては反応生産物を含む反応液)は、排出後
から反応液調整槽までの間、代表的には反応液調整槽で
合流し、排出反応液同士が混合される。In the present invention, the reaction solution in the reaction solution adjusting tank is sent to a plurality of reactors in parallel, and the reaction solution discharged from these reactors returns to the adjusting tank. That is, the reaction solution circulates between the reaction solution adjustment tank and each reactor, and the reaction solution discharged from each reactor after the reaction (in some cases, the reaction solution containing the reaction product) is discharged from the reaction solution. Until the adjustment tank, the reaction liquids typically join in the reaction liquid adjustment tank, and the discharged reaction liquids are mixed.
【0017】そして、上述のような反応液の合流後、反
応液は各リアクターに再び送られるので、各リアクター
中の細胞は反応液を共用することになり、各細胞が反応
液を共有して同時培養ないし共培養されることになる
が、あるリアクターの細胞が反応生産物を生産する場合
には、この反応生産物は反応液に混入され、他のリアク
ターの細胞による生化学反応に供されることになる。After the reaction liquids are combined as described above, the reaction liquid is sent to each reactor again, so that the cells in each reactor share the reaction liquid, and the cells share the reaction liquid. When co-cultured or co-cultured, if a certain reactor cell produces a reaction product, this reaction product is mixed into the reaction solution and subjected to a biochemical reaction by another reactor cell. Will be.
【0018】また、反応液を各リアクターに送る方法と
しては、反応液をポンプで吐出した後、分岐してリアク
ターへ送る方法や、各リアクターに専用ポンプを設けて
リアクターに送る方法、ポンプの代わりに静水圧等の圧
力で圧送する方法や、これらの組み合わせなど各種の方
法が選択できる。なお、各リアクターへの反応液の供給
速度を正確に制御したい場合には、各リアクターに専用
の流量調節機構を設ければよい。The method of sending the reaction solution to each reactor includes a method of discharging the reaction solution by a pump and then branching and sending the reaction solution to the reactor, a method of providing a dedicated pump in each reactor to send the reaction solution to the reactor, and a method using a pump instead of the pump. Various methods can be selected, such as a method of feeding under pressure such as hydrostatic pressure or a combination thereof. When it is desired to accurately control the supply speed of the reaction solution to each reactor, a dedicated flow rate adjusting mechanism may be provided for each reactor.
【0019】また、本発明の生化学反応装置において、
あるリアクターの細胞が他のリアクターへ移動するのを
防止する必要がある場合は、移動防止手段を設ければよ
い。この移動防止手段は、流入を防止すべきリアクター
の上流に設けても、流出を防止すべきリアクターの下流
に設けてもよく、具体的には、細胞を捕捉するフィルタ
ー、加熱殺菌装置、紫外線等の光学的殺菌装置及び放射
殺菌装置などを挙げることができる。Further, in the biochemical reaction device of the present invention,
If it is necessary to prevent cells of a certain reactor from migrating to another reactor, a means for preventing migration may be provided. This movement preventing means may be provided upstream of the reactor to prevent inflow or downstream of the reactor to prevent outflow. Specifically, a filter for capturing cells, a heat sterilizer, ultraviolet light, etc. Optical sterilizer and radiation sterilizer.
【0020】上述の如く、本発明では、リアクターに収
容・保持して培養する細胞としては、微生物、植物及び
動物等の細胞を用いることができる。特に、植物や動物
細胞は、微生物に比較して増殖速度が遅いものが多いの
で、これを含んだリアクターは制御が容易であり、各リ
アクターを制御しながら生化学反応させるのに有効であ
る。As described above, in the present invention, cells such as microorganisms, plants, and animals can be used as cells to be housed and held in the reactor and cultured. In particular, many plant and animal cells have a slower growth rate than microorganisms. Therefore, a reactor containing the same is easy to control, and is effective for performing a biochemical reaction while controlling each reactor.
【0021】また、動物細胞の中でも、肝臓を構成する
細胞は複数種の分化した細胞が互いに影響し合いながら
生化学反応を営んでおり、本発明は、このような系の体
外モデルを容易に実現するものである。即ち、生体内で
は、これらの細胞は互いに接しながら殆ど同じ環境にあ
るが、本発明の生化学反応装置によれば、反応液調整槽
からの共通の反応液や培養液の供給により、生体内とほ
ぼ同じ生化学反応や培養を行うことが可能である。具体
的には、肝臓を構成する実質細胞、星細胞及び繊維芽細
胞等をそれぞれのリアクターで培養し、各リアクターに
は上述の反応液調整槽から共通の反応液や培養液を送れ
ばよいことになる。Among animal cells, the cells constituting the liver perform biochemical reactions while a plurality of types of differentiated cells interact with each other, and the present invention makes it easy to develop an in vitro model of such a system. It will be realized. That is, in a living body, these cells are in almost the same environment while being in contact with each other. However, according to the biochemical reaction device of the present invention, the supply of a common reaction solution or culture solution from the reaction solution adjusting tank causes It is possible to carry out almost the same biochemical reaction and cultivation. Specifically, the parenchymal cells, stellate cells, fibroblasts, etc. constituting the liver are cultured in respective reactors, and a common reaction solution or culture solution may be sent to each reactor from the above-described reaction solution adjustment tank. become.
【0022】また、本発明の生化学反応方法は、上述し
た本発明の生化学反応装置を用いるものであるが、分解
反応、蛋白や核酸等の合成反応、物質変換反応やこれら
の組み合わせなどの各種生化学反応に応用できる。例え
ば、肝実細胞と星細胞をそれぞれ別のリアクター中で培
養し、反応液調整槽を介して共通の培養液を循環しなが
ら培養すると、連続的にアルブミンを生産することがで
きる。本発明は、かかる生化学反応などに特に有効であ
る。The biochemical reaction method of the present invention uses the above-described biochemical reaction apparatus of the present invention, and includes a decomposition reaction, a synthesis reaction of proteins and nucleic acids, a substance conversion reaction, and a combination thereof. Applicable to various biochemical reactions. For example, albumin can be produced continuously by culturing liver real cells and stellate cells in separate reactors, and culturing them while circulating a common culture solution through a reaction solution adjusting tank. The present invention is particularly effective for such biochemical reactions.
【0023】[0023]
【実施例】以下、本発明を図面を参照して更に詳細に説
明するが、本発明はこれら実施例に限定されるものでは
ない。Hereinafter, the present invention will be described in more detail with reference to the drawings, but the present invention is not limited to these embodiments.
【0024】(実施例1)図1は、本発明の生化学反応
装置の一実施例を示す構成図である。同図において、こ
の生化学反応装置は、異なる細胞を収容・保持している
リアクター1及び2と、反応液調整槽3とを備える。本
実施例の装置においては、リアクター1及び2は、反応
液調整槽3からポンプ4によって反応液5の供給を受
け、各リアクターから排出された反応液は調整槽3に戻
り、排出された反応液同士が混合され、再び各リアクタ
ーと調整槽3との間を循環する構成となっている。(Embodiment 1) FIG. 1 is a block diagram showing one embodiment of the biochemical reaction apparatus of the present invention. In this figure, this biochemical reaction apparatus includes reactors 1 and 2 that house and hold different cells, and a reaction solution adjusting tank 3. In the apparatus of the present embodiment, the reactors 1 and 2 receive the supply of the reaction liquid 5 from the reaction liquid adjustment tank 3 by the pump 4, and the reaction liquid discharged from each reactor returns to the adjustment tank 3, and the discharged reaction liquid is returned to the adjustment tank 3. The liquids are mixed and circulated again between each reactor and the adjustment tank 3.
【0025】なお、細胞がリアクター1から調整槽3へ
移動するのを防止したい場合(即ち、当該細胞がリアク
ター2に流入するのを防止したい場合)には、リアクタ
ー1の入口流路6及び/又は出口流路7に細胞の通過を
阻止するフィルター8を設ければよい。また、リアクタ
ー2に特定のガスや液体を供給したい場合には、リアク
ター2の入口流路9に供給流路10を設けることができ
る。When it is desired to prevent cells from moving from the reactor 1 to the regulating tank 3 (ie, to prevent the cells from flowing into the reactor 2), the inlet channel 6 and / or Alternatively, a filter 8 for preventing passage of cells may be provided in the outlet channel 7. When it is desired to supply a specific gas or liquid to the reactor 2, a supply channel 10 can be provided in the inlet channel 9 of the reactor 2.
【0026】次に、本実施例の装置を用いた生化学反応
方法の一例につき説明する。まず、リアクター1及び2
に、細胞の接着の足場となる多孔質の担体、例えば、多
孔質ガラス、セルロースや多孔質ゼラチンビーズ等を充
填し、その担体表面にそれぞれ肝臓を構成する細胞であ
る実質細胞と星細胞とを接着して保持する。そして、調
整槽3に充填した反応液の一例である培養液5をポンプ
4によりリ各アクターに送出し、この培養液5により実
質細胞と星細胞を培養すればよい。なお、この際、調整
槽3では、培養液の溶存酸素、pH及び各種基質濃度を
適切に調整し、均一になるように攪拌することが好まし
い。Next, an example of a biochemical reaction method using the apparatus of this embodiment will be described. First, reactors 1 and 2
Is filled with a porous carrier serving as a scaffold for cell adhesion, for example, porous glass, cellulose or porous gelatin beads, and the like. Glue and hold. Then, a culture solution 5, which is an example of a reaction solution filled in the adjustment tank 3, is sent out to each actor by the pump 4, and the culture solution 5 may be used to culture the parenchymal cells and the stellate cells. In this case, in the adjusting tank 3, it is preferable to appropriately adjust dissolved oxygen, pH and various substrate concentrations of the culture solution, and to stir the mixture so as to be uniform.
【0027】このような反応系では、それぞれの細胞は
他の細胞からの阻害を受けることなく増殖するので、希
望量の細胞数を確保できる。更に、この反応系によれ
ば、生体内のように、1つの細胞の生産物が他の細胞の
蛋白の生産に継続的に影響を与える反応系を実現するこ
とができる。なお、細胞としては、肝臓細胞のような動
物細胞だけではなく、植物細胞や微生物及びこれらの組
み合わせを使用することが可能である。In such a reaction system, each cell proliferates without being inhibited by other cells, so that a desired number of cells can be secured. Further, according to this reaction system, it is possible to realize a reaction system in which the product of one cell continuously affects the production of protein of another cell, as in a living body. As the cells, not only animal cells such as liver cells, but also plant cells, microorganisms, and combinations thereof can be used.
【0028】(実施例2)図2は、本発明の生化学反応
装置の他の実施例を示す構成図であり、2種類の微生物
をそれぞれ別個の培養槽21及び22で培養し、基質槽
23を共有する反応系を示している。上述のように、培
養槽21及び22には異なる微生物が培養されており、
基質槽23と培養槽21及び22とは、ポンプ4を備え
た流路24、25、26及び27で接続されていて、そ
れぞれの培養槽21及び22と基質槽とは循環経路を形
成している。(Embodiment 2) FIG. 2 is a block diagram showing another embodiment of the biochemical reaction apparatus of the present invention. Two types of microorganisms are cultured in separate culture tanks 21 and 22, respectively, and a substrate tank is provided. 23 shows a reaction system sharing 23. As described above, different microorganisms are cultured in the culture tanks 21 and 22,
The substrate tank 23 and the culture tanks 21 and 22 are connected by flow paths 24, 25, 26, and 27 provided with the pump 4, and the respective culture tanks 21 and 22 and the substrate tank form a circulation path. I have.
【0029】また、培養槽22から基質槽23への流路
26の途中には、熱交換パイプ28が熱交換室29中に
配置されており、熱交換室29へは蒸気が出入りして熱
交換パイプ28中の培養液を加熱殺菌できる構成となっ
ている。A heat exchange pipe 28 is provided in the heat exchange chamber 29 in the middle of the flow path 26 from the culture tank 22 to the substrate tank 23, and steam enters and exits the heat exchange chamber 29. The culture solution in the exchange pipe 28 can be heated and sterilized.
【0030】次に、本実施例の装置を用いた生化学反応
方法の一例につき説明する。培養槽21で乳酸菌を培養
して乳酸菌による乳酸発酵が行う一方で、培養槽22で
メタン菌を培養し、メタン発酵を行う。ここで、特許第
1902791号には、メタン菌を含む培養液を加熱処
理した液をメタン発酵液に添加すると、メタン発酵が促
進されることが記載されているが、本発明者は、上記メ
タン菌を含む液を加熱処理した液が、乳酸菌やカビによ
る乳酸生成を促進することを見出した。この現象はメタ
ン菌を加熱処理した液がメタン菌以外の他の菌の生理活
性をも促進する機能を示唆するものである。なお、本実
施例の反応系では、メタン菌を含む液を加熱処理した液
が、乳酸発酵とメタン発酵を促進することになる。ま
た、熱交換室29による加熱処理により、培養液22中
の微生物が培養槽21へ移動しないという利点もある。Next, an example of a biochemical reaction method using the apparatus of this embodiment will be described. While lactic acid bacteria are cultured in the culture tank 21 and lactic acid fermentation is performed by the lactic acid bacteria, methane bacteria are cultured in the culture tank 22 and methane fermentation is performed. Here, Japanese Patent No. 1902791 describes that when a liquid obtained by heat-treating a culture solution containing methane bacteria is added to a methane fermentation solution, methane fermentation is promoted. It has been found that a liquid obtained by heat-treating a liquid containing bacteria promotes lactic acid production by lactic acid bacteria and mold. This phenomenon suggests that the solution obtained by heat treatment of methane bacteria also promotes the physiological activity of other bacteria other than methane bacteria. In the reaction system of the present example, a liquid obtained by heat-treating a liquid containing methane bacteria promotes lactic acid fermentation and methane fermentation. In addition, there is an advantage that the microorganisms in the culture solution 22 do not move to the culture tank 21 by the heat treatment in the heat exchange chamber 29.
【0031】[0031]
【発明の効果】以上説明してきたように、本発明によれ
ば、反応液調整槽と別個の細胞又は細胞群を収容した各
リアクターとを並列に連結し、各リアクターから排出さ
れた反応液が反応液調整槽に戻るような構成とすること
としたため、複数種の細胞を反応液を共有して同時培養
ないし共培養でき、特に、動物細胞や植物細胞の培養に
おいて、ある細胞の生産物が他種の細胞の基質や生理活
性因子となり得るような培養系で、各細胞を個別に培養
・管理し得る生化学反応装置及び生化学反応方法を提供
することができる。As described above, according to the present invention, the reaction solution adjusting tank is connected in parallel with each reactor containing a separate cell or group of cells, and the reaction solution discharged from each reactor is Since it is configured to return to the reaction solution adjusting tank, a plurality of types of cells can be co-cultured or co-cultured by sharing the reaction solution. A biochemical reaction device and a biochemical reaction method capable of individually culturing and managing each cell in a culture system that can serve as a substrate or a bioactive factor for other types of cells can be provided.
【0032】また、本発明においては、複数種の細胞へ
共通の反応液調整槽から反応液を送液するので、調整槽
の個数が少なくて済むだけでなく、培養液の調整の煩雑
さが軽減される。更に、1つの反応の生産物を他の細胞
の反応に供することができる。なお、この生産物は、他
の細胞の基質になることもあるし、生理活性物質になる
こともある。In the present invention, since the reaction solution is sent from a common reaction solution adjusting tank to a plurality of types of cells, not only the number of adjusting tanks is reduced but also the complexity of adjusting the culture solution is reduced. It is reduced. Further, the products of one reaction can be subjected to the reaction of another cell. This product may be a substrate for other cells or a physiologically active substance.
【図1】本発明の生化学反応装置の一実施例を示す構成
図である。FIG. 1 is a configuration diagram showing one embodiment of a biochemical reaction device of the present invention.
【図2】本発明の生化学反応装置の他の実施例を示す構
成図である。FIG. 2 is a configuration diagram showing another embodiment of the biochemical reaction device of the present invention.
1 リアクター 2 リアクター 3 調整槽 4 ポンプ 5 反応液 6 入口流路 7 出口流路 8 フィルター 9 入口流路 10 供給流路 21 リアクター 22 リアクター 23 基質槽 24、25、26、27 流路 28 熱交換パイプ 29 熱交換室 DESCRIPTION OF SYMBOLS 1 Reactor 2 Reactor 3 Adjustment tank 4 Pump 5 Reaction liquid 6 Inlet flow path 7 Outlet flow path 8 Filter 9 Inlet flow path 10 Supply flow path 21 Reactor 22 Reactor 23 Substrate tank 24, 25, 26, 27 Flow path 28 Heat exchange pipe 29 heat exchange room
Claims (5)
合わせにより個別に収容する複数個のリアクターと、上
記細胞に供給する反応液を収容した反応液調整槽とを備
え、 上記反応液調整槽は上記反応液を上記複数個のリアクタ
ーへ並列に送り、これらリアクターから排出された反応
液が上記反応液調整槽に戻ることにより、上記反応液が
上記反応液調整槽と各リアクター間を循環し、 この循環に際し、上記リアクターから排出された反応液
同士が合流し、上記複数種の細胞が反応液を共用するこ
とを特徴とする生化学反応装置。1. A reactor comprising: a plurality of reactors for individually accommodating a plurality of kinds of cells in one kind or a combination of two or more kinds; and a reaction solution adjusting tank containing a reaction solution to be supplied to the cells. The adjustment tank sends the reaction solution to the plurality of reactors in parallel, and the reaction solution discharged from these reactors returns to the reaction solution adjustment tank, so that the reaction solution flows between the reaction solution adjustment tank and each reactor. A biochemical reaction device, wherein the reaction solution discharged from the reactor merges during the circulation, and the plurality of types of cells share the reaction solution.
る細胞が、他のリアクターに移動するのを防止する移動
防止手段を備えることを特徴とする請求項1記載の生化
学反応装置。2. The biochemical reaction device according to claim 1, further comprising a movement preventing means for preventing cells in at least one of the reactors from moving to another reactor.
ることを特徴とする請求項1又は2記載の生化学反応装
置。3. The biochemical reaction device according to claim 1, wherein the cells are animal and / or plant cells.
以上の細胞であることを特徴とする請求項3記載の生化
学反応装置。4. The biochemical reaction device according to claim 3, wherein the animal cells are two or more types of cells constituting a liver.
の生化学反応装置を用いることを特徴とする生化学反応
方法。5. A biochemical reaction method using the biochemical reaction device according to any one of claims 1 to 5.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9250105A JPH1175821A (en) | 1997-09-01 | 1997-09-01 | Biochemical reaction apparatus for culturing several series of cell and biochemical reaction |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9250105A JPH1175821A (en) | 1997-09-01 | 1997-09-01 | Biochemical reaction apparatus for culturing several series of cell and biochemical reaction |
Publications (1)
Publication Number | Publication Date |
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JPH1175821A true JPH1175821A (en) | 1999-03-23 |
Family
ID=17202900
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JP9250105A Pending JPH1175821A (en) | 1997-09-01 | 1997-09-01 | Biochemical reaction apparatus for culturing several series of cell and biochemical reaction |
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Country | Link |
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JP (1) | JPH1175821A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102229887A (en) * | 2011-04-18 | 2011-11-02 | 北京航空航天大学 | In vitro cell co-culturing double flow mechanical force loaded flow chamber apparatus |
WO2015159333A1 (en) * | 2014-04-14 | 2015-10-22 | 株式会社島津製作所 | Cell culturing device, cell culturing system and cell culturing method |
JP6111510B1 (en) * | 2016-05-02 | 2017-04-12 | インテグリカルチャー株式会社 | Growth induction system, growth induction control device, growth induction control method, and growth induction control program |
CN112553044A (en) * | 2020-12-10 | 2021-03-26 | 上海奥浦迈生物科技股份有限公司 | Anti-blocking device for bioreactor cell culture sample inlet |
WO2023026147A1 (en) * | 2021-08-24 | 2023-03-02 | Stellenbosch University | A bioreactor for contactless co-culturing |
WO2024048588A1 (en) * | 2022-08-31 | 2024-03-07 | インテグリカルチャー株式会社 | Cell culture system, cultured meat, and culture supernatant |
-
1997
- 1997-09-01 JP JP9250105A patent/JPH1175821A/en active Pending
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102229887A (en) * | 2011-04-18 | 2011-11-02 | 北京航空航天大学 | In vitro cell co-culturing double flow mechanical force loaded flow chamber apparatus |
WO2015159333A1 (en) * | 2014-04-14 | 2015-10-22 | 株式会社島津製作所 | Cell culturing device, cell culturing system and cell culturing method |
CN106103691A (en) * | 2014-04-14 | 2016-11-09 | 株式会社岛津制作所 | Cell is cultivated with equipment, cell cultivation system and cell culture processes |
JPWO2015159333A1 (en) * | 2014-04-14 | 2017-04-13 | 株式会社島津製作所 | Cell culture device, cell culture system and cell culture method |
US10301586B2 (en) | 2014-04-14 | 2019-05-28 | Shimadzu Corporation | Cell culturing device, cell culturing system and cell culturing method |
JP6111510B1 (en) * | 2016-05-02 | 2017-04-12 | インテグリカルチャー株式会社 | Growth induction system, growth induction control device, growth induction control method, and growth induction control program |
CN112553044A (en) * | 2020-12-10 | 2021-03-26 | 上海奥浦迈生物科技股份有限公司 | Anti-blocking device for bioreactor cell culture sample inlet |
WO2023026147A1 (en) * | 2021-08-24 | 2023-03-02 | Stellenbosch University | A bioreactor for contactless co-culturing |
WO2024048588A1 (en) * | 2022-08-31 | 2024-03-07 | インテグリカルチャー株式会社 | Cell culture system, cultured meat, and culture supernatant |
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