JPH0779677B2 - Incubator - Google Patents

Incubator

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Publication number
JPH0779677B2
JPH0779677B2 JP3287215A JP28721591A JPH0779677B2 JP H0779677 B2 JPH0779677 B2 JP H0779677B2 JP 3287215 A JP3287215 A JP 3287215A JP 28721591 A JP28721591 A JP 28721591A JP H0779677 B2 JPH0779677 B2 JP H0779677B2
Authority
JP
Japan
Prior art keywords
culture
liquid
gas
outlet
cells
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP3287215A
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Japanese (ja)
Other versions
JPH0595779A (en
Inventor
泰典 遠矢
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Ebara Corp
Original Assignee
Ebara Corp
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Publication date
Application filed by Ebara Corp filed Critical Ebara Corp
Priority to JP3287215A priority Critical patent/JPH0779677B2/en
Publication of JPH0595779A publication Critical patent/JPH0595779A/en
Publication of JPH0779677B2 publication Critical patent/JPH0779677B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS 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
    • C12M31/00Means for providing, directing, scattering or concentrating light
    • C12M31/10Means for providing, directing, scattering or concentrating light by light emitting elements located inside the reactor, e.g. LED or OLED
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS 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
    • C12M21/00Bioreactors or fermenters specially adapted for specific uses
    • C12M21/02Photobioreactors
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M27/00Means for mixing, agitating or circulating fluids in the vessel
    • C12M27/10Rotating vessel

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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Chemical & Material Sciences (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Zoology (AREA)
  • Genetics & Genomics (AREA)
  • Biotechnology (AREA)
  • Sustainable Development (AREA)
  • Microbiology (AREA)
  • Biomedical Technology (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Molecular Biology (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は微生物及び/又は細胞を
培養する培養装置に係り、特に光合成微生物及び/又は
動植物細胞ないしプロトプラスト等の培養に好適な回転
ドラム式培養装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a culture device for culturing microorganisms and / or cells, and more particularly to a rotating drum type culture device suitable for culturing photosynthetic microorganisms and / or animal / plant cells or protoplasts.

【0002】[0002]

【従来の技術】従来、微生物及び/又は細胞の培養装
置、特に液体培養装置においては、固定タンクを設け気
体の供給と培地の混合を目的として、プロペラ式攪拌装
置、マグネティックスターラー、エアリフト方式用のド
ラフトチューブ等が用いられて来た。また、回分式培養
装置においては、モノー式、レシプロ式等の振とう機や
ローラーボトルのように振動や回転させることにより混
合と気液接触を行う装置が用いられている。しかしなが
ら、これらは小型の装置に限られている。
2. Description of the Related Art Conventionally, in a culturing apparatus for microorganisms and / or cells, particularly a liquid culturing apparatus, a fixed tank is provided and a propeller-type stirring device, a magnetic stirrer, and an air lift system are used for the purpose of gas supply and medium mixing. Draft tubes and the like have been used. Further, in the batch-type culture device, a device for performing mixing and gas-liquid contact by vibrating or rotating like a shaker such as a mono-type or reciprocating type shaker or a roller bottle is used. However, these are limited to small devices.

【0003】[0003]

【発明が解決しようとする課題】工業化にあたっては、
大量培養と生産(増殖)量の精密制御が求められている
が、従来の固定タンク式では次の様な欠点があった。 (1)培養装置内に散気管、攪拌装置、各種のセンサー
類、ドラフトチューブなど、様々な障害物が存在してい
るため、槽内液の流れに滞留部分が多く生じ、そこへ培
養菌体、藻体あるいは細胞などが濃厚に付着する。 (2)散気装置、攪拌装置を用いても、必ずしもガス溶
解効率は高くなく、通常大量のガスを供給しなければな
らない。 (3)強度の弱い微生物や細胞培養などにおいては、攪
拌装置により強い剪断流を起こす方法は適用し難い。 そこで、本発明は、上記問題点を改善した槽内の不均一
化を防ぎ、培養細胞に損傷が少ない気液接触効率のよい
培養装置を提供することを課題とする。
[Problems to be Solved by the Invention] In industrialization,
Although large-scale culture and precise control of production (growth) amount are required, the conventional fixed tank system has the following drawbacks. (1) Due to various obstacles such as air diffuser, agitator, various sensors, draft tube, etc. in the culture device, a lot of stagnation occurs in the flow of the liquid in the tank, and the cultured bacterial cells enter there. , Algal cells or cells adhere to the surface. (2) Even if an air diffuser or a stirrer is used, the gas dissolution efficiency is not always high, and a large amount of gas must be supplied. (3) It is difficult to apply a method of causing a strong shear flow by a stirring device to a microorganism having weak strength or cell culture. Therefore, it is an object of the present invention to provide a culture device which has improved the above-mentioned problems, prevents non-uniformity in the tank, and has less gas-liquid contact efficiency with less damage to cultured cells.

【0004】[0004]

【課題を解決するための手段】上記課題を解決するため
に、本発明では、微生物及び/又は細胞等を培養する培
養装置において、少なくとも一端に固定連結部を備えた
回転培養容器と、該培養容器を水平軸方向に保持しつつ
回転させる駆動装置を有し、前記固定連結部に液流入口
ならびに流出口、ガス流入口ならびに流出口、及び光導
入口をそれぞれ設け、これらを前記培養容器内と連通さ
せると共に、該液流出口より固液分離装置を解して液流
入口へ培養液の一部を循環させる液循環機構と、該ガス
流出口より排出するガスの一部をガス流入口に循環させ
るガス循環機構とを有することを特徴とする培養装置と
したものである。前記装置において、液流出口には、前
記培養容器内で上向に開口する流出管を有すると共に、
該流出管の高さを上下に調整できるように配備するのが
よい。
In order to solve the above-mentioned problems, in the present invention, in a culture device for culturing microorganisms and / or cells, etc., a rotary culture vessel having a fixed connection portion at least at one end, and the culture are provided. It has a driving device for rotating the container while holding it in the horizontal axis direction, and a liquid inlet and an outlet, a gas inlet and an outlet, and a light inlet are respectively provided in the fixed connection part, and these are provided in the culture container. Communicated with
In addition, the solid-liquid separation device is opened from the liquid outlet and the liquid flow
A liquid circulation mechanism for circulating a part of the culture liquid to the inlet, and the gas
Circulate a part of the gas discharged from the outlet to the gas inlet.
And a gas circulation mechanism . In the device, the liquid outlet has a front
With an outflow pipe that opens upward in the culture container,
To arrange the outlet pipe so that the height can be adjusted up and down.
Good.

【0005】ここで、培養容器は回転する形状であれば
良く、円筒形、円錐台形、球形、樽形、ボトル形等、適
宜選定できる。また固定連結部は、培養容器の回転軸の
片端に設置しても、両端に設置しても良い。培養容器の
容積が大なる場合には、それ以外のものは光放散体を含
めて、培養器の両端の固定連結部にそれぞれ設けること
ができ、またそれぞれの部品について、強度の面からも
有利である。
Here, the culture vessel may be of any rotating shape, and can be appropriately selected from a cylindrical shape, a truncated cone shape, a spherical shape, a barrel shape, a bottle shape and the like. Further, the fixed connecting portion may be installed at one end or both ends of the rotating shaft of the culture container. When the volume of the culture container is large, other components, including the light diffuser, can be provided at the fixed connection parts at both ends of the incubator, and each component is also advantageous in terms of strength. Is.

【0006】この固定連結部は自立式でも、駆動装置と
接続した構成としてもかまわない。固定連結部は、培養
容器内外の流入・流出の連結部位で、ここから培養器内
に例えば、光放散体、散気管、液体の供給管および溢流
管等の流通手段を突出させる。また支持部位でもあっ
て、回転する培養器内に固定して位置させたい物、例え
ば、付着物剥離用ワイパー(スクレーパー)、各種セン
サー等も、固定連結部より必要により突出させることが
できる。
The fixed connecting portion may be self-supporting or connected to a driving device. The fixed connection part is a connection part of inflow and outflow inside and outside the culture container, and from this, a flow means such as a light diffuser, an air diffusing pipe, a liquid supply pipe and an overflow pipe is projected into the incubator. Further, it is also a support site, and an object to be fixedly positioned in the rotating incubator, for example, a wiper (scraper) for removing adhered substances, various sensors, and the like can be made to protrude from the fixed connecting portion as necessary.

【0007】本発明の培養容器への液の張込み量は、混
合培養液流出管の位置を上下に移動することにより自由
に調整することができ、容積効率がほぼ100%の条件
でも運転することが可能であるが、ガスの溶解効率を高
いレベルに維持するために、通常は、容積効率を50〜
70%の範囲に設定して運転することが好ましい。さら
に、装置からの排出液(菌体混合液)は固液分離装置に
よって菌体と培養終了液とに分離するが、培養残液中に
はなお菌体増殖に必要な有機物あるいは各種の有効な微
量成分が残留している。従って、培養残液を装置に供給
する原液に合流させ残留成分を繰返し再利用するのがよ
い。
The amount of the liquid poured into the culture container of the present invention can be freely adjusted by moving the position of the mixed culture liquid outflow pipe up and down, and the operation is performed even under the condition that the volumetric efficiency is almost 100%. However, in order to maintain the gas dissolution efficiency at a high level, the volume efficiency is usually 50 to 50%.
It is preferable to set and operate in the range of 70%. Further, the liquid discharged from the device (mixture of bacterial cells) is separated into a bacterial cell and a culture-finished liquid by a solid-liquid separation device. Trace components remain. Therefore, it is recommended to combine the residual culture solution with the undiluted solution supplied to the equipment to reuse the residual components repeatedly .
Yes.

【0008】ガス類は装置外から任意の滅菌手段を介し
てブロワー等によって供給し、散気管によって回転する
培養容器の各部に均一になるように曝気を行うが、特に
脆弱な微生物、細胞、プロトプラストについては散気管
を使用せず、気液界面から拡散させてもよい。ガス類の
供給方法は、一過性でもよいが、その利用効率に限界が
ある。したがって、本発明では装置内溶液の散気による
攪拌をさらに強める目的も兼ねて、装置からの排出ガス
をガス供給管に連結して繰り返し利用し、コスト低減を
も同時に達成することができる。最終的な排出ガスは滅
菌工程を経て系外へ排出されることは言うまでもない。
Gases are supplied from the outside of the device through an arbitrary sterilizing means by a blower or the like, and aeration tubes are used to aerate each part of the rotating culture container so as to be uniform, but particularly fragile microorganisms, cells and protoplasts are used. For the above, the diffuser may be diffused from the gas-liquid interface without using an air diffuser. The gas supply method may be transient, but its utilization efficiency is limited. Therefore, in the present invention, also for the purpose of further enhancing the agitation of the solution in the device by aeration, the exhaust gas from the device is connected to the gas supply pipe and repeatedly used, and the cost can be reduced at the same time. It goes without saying that the final exhaust gas is discharged to the outside of the system through the sterilization process.

【0009】またガス溶解効率向上のため容器内の圧力
を上げ、液中のガス分圧の上昇を行うことができるが培
養器には十分強度をもった材質の容器が必要である。し
たがって、光合成微生物又は細胞といえども不透明の金
属製の容器が使用される。この場合は後述のような容器
内への光供給手段を設けることが必要である。光合成細
菌、微細藻類あるいは植物細胞やプロトプラスト等の光
培養において用いる光放散体は、光ファイバーによって
伝送された人工光及び/又は太陽光を培養容器内に高密
度、かつ均一に分散できるものであり、その材質は石英
ガラス製、PMMA製(ポリメチルメタクリレート)、
その他公知のものが適用できる。
Further, in order to improve the gas dissolution efficiency, the pressure in the container can be raised to raise the partial pressure of the gas in the liquid, but the incubator requires a container made of a material having sufficient strength. Therefore, an opaque metal container is used even for photosynthetic microorganisms or cells. In this case, it is necessary to provide a light supply means into the container as described later. Photosynthetic bacteria, microalgae or light diffusers used in photoculture of plant cells or protoplasts are those that can disperse artificial light and / or sunlight transmitted by an optical fiber in a culture container at high density, and uniformly. The material is quartz glass, PMMA (polymethylmethacrylate),
Other known materials can be applied.

【0010】また、PMMAやその他の樹脂などのロッ
ドの表面に溝や傷等をつけて加工したり、あるいは前記
した各種の光放散体に光を乱反射する各種の粒状物を分
散、封入する方法を採用するとよい。この場合、装置内
液に均等に光を放散させるためには、表面に付ける傷や
溝あるいは微粒子の密度は、接続点から遠くなるほど大
きくするのがよい。また、各種の光放散体は強度の強い
透明な物質で保護体をつくり、保護する方法が好まし
い。
Further, a method of forming grooves or scratches on the surface of a rod of PMMA or other resin, or dispersing or enclosing various kinds of particulate matter that diffusely reflects light in the various light diffusers described above. Should be adopted. In this case, in order to evenly diffuse the light in the liquid in the apparatus, it is preferable that the density of scratches, grooves or fine particles on the surface be increased as the distance from the connection point increases. Further, it is preferable that various light diffusers are protected by forming a protector with a strong transparent material.

【0011】[0011]

【作用】本発明の培養装置において、細胞乃至はプロト
プラスト及び/又は微生物と液体培地の混合物(以後、
混合液=MLと略記する)は培養容器内壁を濡らし薄膜
を形成する。このためガスの溶解効率が高く、かつ培養
に対する傷害を与えにくい。但し、比較的物理的なスト
レスに耐性の強い微生物等については、槽内に散気装置
を設けても良い。槽自体が回転するため、槽の一部に培
養が集積することがなくMLの状態は均一に設定でき
る。また本発明の装置は連続培養系としても構成できる
ので、流入基質・希釈率等を調節することにより、ケモ
スタット、タービドスタット等として培養の増殖を制御
することができる。なお、ガス体及び液体として供給さ
れた基質の残りを返送して利用効率を高めた構造によ
り、安価で省資源的な培養ができる。
In the culture device of the present invention, a mixture of cells or protoplasts and / or microorganisms and a liquid medium (hereinafter,
The mixed solution = abbreviated as ML) wets the inner wall of the culture vessel to form a thin film. Therefore, the gas dissolution efficiency is high, and the culture is less likely to be damaged. However, an air diffuser may be provided in the tank for microorganisms and the like that are relatively resistant to physical stress. Since the tank itself rotates, the culture does not accumulate in a part of the tank and the ML state can be set uniformly. Further, since the device of the present invention can be configured as a continuous culture system, the growth of the culture can be controlled as a chemostat, turbidostat or the like by adjusting the inflowing substrate, the dilution ratio and the like. In addition, due to the structure in which the gas body and the rest of the substrate supplied as a liquid are returned to improve the utilization efficiency, inexpensive and resource-saving culture can be performed.

【0012】以上のように、本発明はデリケートな培養
対象についても、大量培養が可能であり、かつ連続培養
系を構成できる精密制御可能なリアクタとして工業的な
利用範囲が広い。適用例として生理活性物質(増殖因子
・酵素・抗生物質等)を産生する細菌・酵母・放線菌類
等の微生物(例えば形質導入された大腸菌や海洋性バチ
ルス等)の培養槽として、また特定物質の資化微生物に
よる処理装置として、また分離細胞やウィルス等の培養
装置等が挙げられる。また加圧下での培養にも適用でき
るので、深海の耐圧性微生物用のリアクタとしても適用
できる。また、光合成微生物、光合成細胞乃至クロロプ
ラスト等の培養には、導光体、光放散体を設置できるよ
う構成するので、より有効に培養することができる。
As described above, the present invention has a wide industrial application range as a precisely controllable reactor capable of mass-culturing even a delicate culture object and constituting a continuous culture system. As an application example, it is used as a culture tank for microorganisms (such as transduced Escherichia coli and marine bacillus) that produce physiologically active substances (growth factors, enzymes, antibiotics, etc.), such as bacteria, yeast, actinomycetes, and Examples of the treatment device using assimilating microorganisms include a culture device for isolated cells and viruses. Further, since it can be applied to culture under pressure, it can also be applied as a reactor for pressure-resistant microorganisms in the deep sea. Further, since a light guide and a light diffuser can be installed in the culture of the photosynthetic microorganism, the photosynthetic cell or chloroplast, the culture can be performed more effectively.

【0013】[0013]

【実施例】以下、本発明を図面を用いて具体的に説明す
るが、本発明はこれらに限定されない。 実施例1 この実施例は、円筒形で両端に支持連結部を配した装置
を用いて光合成微生物の培養を行う場合を説明する。図
1は、光合成微生物培養装置(以下、培養装置という)
の断面説明図である。図2は、図1の装置の液体とガス
体の流れを説明するフロー概略図である。図1におい
て、1は回転培養容器、2は固定連結部である。培養容
器1と固定連結部2とは回転可能でかつ漏れないように
連結されている。培養容器1は、駆動装置4(回転数は
5の回転計によって表示される)の駆動により、これに
接して回転ロール3が回転し、この回転を培養容器1に
伝達する。培養容器1の緩慢な回転によって装置内のM
Lは培養容器の内壁に沿ってフィルム状の薄膜が形成さ
れ、ガス吹込管8、散気管9から供給されたガスが極め
て有効に利用される。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be specifically described below with reference to the drawings, but the present invention is not limited to these. Example 1 This example describes the case of culturing a photosynthetic microorganism by using a device having a cylindrical shape and supporting connection portions arranged at both ends. FIG. 1 shows a photosynthetic microorganism culture device (hereinafter referred to as a culture device).
FIG. FIG. 2 is a schematic flow diagram illustrating the flow of liquid and gas in the device of FIG. In FIG. 1, 1 is a rotary culture container, and 2 is a fixed connection part. The culture container 1 and the fixed connection part 2 are rotatably connected so as not to leak. The culture container 1 is driven by a driving device 4 (the rotation speed is indicated by a tachometer of 5), and the rotating roll 3 rotates in contact with the drive device 4 and transmits the rotation to the culture container 1. The slow rotation of the culture vessel 1 causes the M in the apparatus to rotate.
As for L, a film-like thin film is formed along the inner wall of the culture vessel, and the gas supplied from the gas blowing pipe 8 and the air diffusing pipe 9 is used very effectively.

【0014】固定連結部2にはガス吹込管8、散気管
9、ガス排出管(ガス循環管)(図−2)8′、複数の
光放散体7(通常さや管6によって保護されている。図
3に固定軸の縦断面図を示す)。培養容器の内壁の付着
物を機械的に剥離するためのワイパー11が設置されて
おり、また図2に記載のように原水流入管15、ML流
出管16が設置されており、特にML流出管16は、そ
の高さを上下することによって培養装置内溶液の液張込
み量(容積効率)を自由に調整することができる。また
図1に示したように培養装置の液張込み量(水位10
A,B)によって、培養装置に光エネルギーを導入する
光拡散体の数も適当に増減することができる。
The fixed connecting portion 2 has a gas blowing pipe 8, an air diffusing pipe 9, a gas discharging pipe (gas circulating pipe) 8 '(FIG. 2) 8', and a plurality of light diffusers 7 (usually protected by a sheath 6). Fig. 3 shows a vertical sectional view of the fixed shaft. A wiper 11 for mechanically peeling off deposits on the inner wall of the culture vessel is installed, and a raw water inflow pipe 15 and an ML outflow pipe 16 are installed as shown in FIG. The volume of the solution in the culture device (volumetric efficiency) can be freely adjusted by increasing or decreasing the height of 16. In addition, as shown in FIG.
Depending on A and B), the number of light diffusers for introducing light energy into the culture device can be appropriately increased or decreased.

【0015】図2において培養容器1内に適量の光合成
細菌、微細藻類あるいは特定の細胞(以後、培養とい
う)を接種し、原液流入管15からそれぞれの微生物及
び/又は細胞類の増殖に適した培養液を連続的に注入す
る。培養容器1は前記の通り緩慢な速度で回転し、散気
管9から供給されたガス体と液中及び装置内壁にフィル
ム状に持ちあげられるMLに供給ガスが効率よく吸収さ
れる。また、装置内のMLの攪拌、混合は培養容器の回
転の他、装置内に設置された複数の光放散体のバッフル
効果によっても緩慢に行われるので、培養に対して衝撃
を与えることはない。
In FIG. 2, an appropriate amount of photosynthetic bacteria, microalgae or specific cells (hereinafter referred to as culture) is inoculated into the culture container 1 and is suitable for the growth of each microorganism and / or cells from the stock solution inflow pipe 15. The culture solution is continuously infused. The culture vessel 1 rotates at a slow speed as described above, and the supply gas is efficiently absorbed in the gas body and liquid supplied from the air diffusing tube 9 and in the ML which is carried in a film form on the inner wall of the apparatus. Further, the stirring and mixing of ML in the device is performed slowly not only by the rotation of the culture container but also by the baffle effect of a plurality of light diffusers installed in the device, so that there is no impact on the culture. .

【0016】培養が必要量増殖したMLはML流出管1
6によって装置外に取り出されるが、例えばセラミック
フィルター、メンブレンフィルターなどの所謂膜によっ
て構成された固液分離装置20によって培養17と分離
液18に分離される。なお培養の分離には沈殿・遠心分
離等の手段を用いてもよい。培養17は有用物質生産あ
るいはその他の目的に有効利用できる。分離液18は前
記した目的のために原水流入管15に返送され、培養装
置内で、残留する有効成分が培養に繰り返し利用され
る。
The ML that has grown in the required amount of culture is the ML outflow tube 1
Although it is taken out of the apparatus by 6, it is separated into a culture solution 17 and a separation solution 18 by a solid-liquid separation apparatus 20 composed of a so-called membrane such as a ceramic filter or a membrane filter. It should be noted that means such as precipitation and centrifugation may be used for the separation of the culture. The culture 17 can be effectively used for producing useful substances or for other purposes. The separated liquid 18 is returned to the raw water inflow pipe 15 for the above-mentioned purpose, and the remaining active ingredient is repeatedly used for culture in the culture device.

【0017】光合成微生物及び/又は細胞類の培養に必
要な光エネルギーは、太陽光19を太陽光集光装置12
によって、及び/又は人工光発生装置13からの人工光
は光伝送用ファイバー14によって装置内に取りつけら
れた光放散体7と連結され、複数の光放散体から液中に
高密度かつ均一に分散、供給される。一方、培養に必要
なガス体はブロワー21によって図示されていない滅菌
工程を経てガス吹込管8を経由して装置内の散気管に送
られ、菌体に供給されるが、装置からの排出ガスはガス
循環管8′を経由してブロワー9の吸気側に連結され、
各種微生物により繰り返し利用される。余剰(発生)ガ
スは、余剰ガス排出管8″から図示されていない滅菌工
程を経て系外に排出される。
The light energy necessary for culturing the photosynthetic microorganisms and / or cells converts sunlight 19 into sunlight concentrator 12.
And / or the artificial light from the artificial light generating device 13 is connected to the light diffuser 7 mounted in the device by the optical transmission fiber 14 to disperse the light uniformly from the plurality of light diffusers in the liquid at high density. , Supplied. On the other hand, the gas body necessary for culture is sent to the air diffuser pipe in the device through the gas blowing pipe 8 through the sterilization process (not shown) by the blower 21 and is supplied to the bacterial cells, but the exhaust gas from the device is discharged. Is connected to the intake side of the blower 9 via the gas circulation pipe 8 ',
It is repeatedly used by various microorganisms. The surplus (generated) gas is discharged from the surplus gas exhaust pipe 8 ″ to the outside of the system through a sterilization process (not shown).

【0018】[0018]

【発明の効果】本発明によれば、前記詳述した構成とし
たことにより、次のような作用効果を奏する。 (1)断面が円形の横型回転ドラム式の培養装置とした
ことにより、装置内壁の気相部分に装置内液がフィルム
状の薄膜となり、供給ガスが液側に効果的に移動し、従
来技術よりは遙かに少ないガス量で微生物あるいは細胞
類を大量培養することができる。 (2)槽自体が回転するため、培養装置内に気液及び菌
体を混合するための機械的攪拌装置がなくてもよく、培
養に強い剪断力を与えることがなく、細胞類に損傷を与
えないので、デリケートな対象の大量培養に好適であ
る。 (3)微生物あるいは細胞培養に必要な基質類あるいは
ガス体は、返送あるいは循環により繰り返し利用される
ので、基質を有効に利用できる。(4)連続培養装置として用いることが可能で、希釈率
等の培養条件を微妙に調整することが容易に行える。
According to the present invention, with the above-described detailed structure, the following operational effects can be obtained. (1) By adopting a horizontal rotary drum type culture device having a circular cross section, the liquid inside the device becomes a film-like thin film in the gas phase portion of the inner wall of the device, and the supply gas is effectively moved to the liquid side. It is possible to mass-culture microorganisms or cells with a much smaller amount of gas. (2) Since the tank itself rotates, there is no need for a mechanical stirring device for mixing gas-liquid and bacterial cells in the culture device, which does not give strong shearing force to the culture and damages the cells. Since it is not given, it is suitable for large-scale culture of delicate objects. (3) Substrates or gas bodies necessary for culturing microorganisms or cells are repeatedly used by returning or circulating, so that the substrates can be effectively used. (4) It can be used as a continuous culture device and the dilution rate
It is possible to easily finely adjust the culture conditions such as.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の光合成微生物培養装置の断面説明図で
ある。
FIG. 1 is a cross-sectional explanatory view of a photosynthetic microorganism culture device of the present invention.

【図2】図1の装置の液体とガスの流れを説明するフロ
ー概略図である。
FIG. 2 is a schematic flow diagram illustrating the flow of liquid and gas in the device of FIG.

【図3】固定軸の縦断面図である。FIG. 3 is a vertical sectional view of a fixed shaft.

【符号の説明】[Explanation of symbols]

1:培養容器、2:固定連結部、3:回転ロール、4:
駆動装置、5:回転計、6:さや管、7:光ファイバー
(光放散体)、8:ガス吸込管、8′:ガス循環管、
9:散気管、10:水位、11:ワイパー、15:原液
流入管、16:菌体混合液(ML)流出管
1: Culture vessel, 2: Fixed connection part, 3: Rotating roll, 4:
Drive device, 5: tachometer, 6: sheath tube, 7: optical fiber (light diffuser), 8: gas suction tube, 8 ': gas circulation tube,
9: Air diffuser, 10: Water level, 11: Wiper, 15: Stock solution inflow tube, 16: Bacterial cell mixture (ML) outflow tube

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 微生物及び/又は細胞等を培養する培養
装置において、少なくとも一端に固定連結部を備えた回
転培養容器と、該培養容器を水平軸方向に保持しつつ回
転させる駆動装置を有し、前記固定連結部に液流入口な
らびに流出口、ガス流入口ならびに流出口、及び光導入
口をそれぞれ設け、これらを前記培養容器内と連通させ
ると共に、該液流出口より固液分離装置を介して液流入
口へ培養液の一部を循環させる液循環機構と、該ガス流
出口より排出するガスの一部をガス流入口に循環させる
ガス循環機構とを有することを特徴とする培養装置。
1. A culture device for culturing microorganisms and / or cells, comprising a rotary culture container having a fixed connection portion at least at one end, and a drive device for rotating the culture container while holding the culture container in a horizontal axis direction. , A liquid inlet and an outlet, a gas inlet and an outlet, and a light inlet are respectively provided in the fixed connection part, and these are communicated with the inside of the culture vessel, and the liquid outlet is connected via a solid-liquid separation device. Liquid inflow
A liquid circulation mechanism for circulating a part of the culture liquid to the mouth, and the gas flow
Circulate a part of the gas discharged from the outlet to the gas inlet
A culture apparatus having a gas circulation mechanism .
【請求項2】 前記液流出口には、前記培養容器内で上2. The liquid outlet is located above the culture container.
向に開口する流出管を有すると共に、該流出管の高さをHas an outlet pipe that opens in the direction of
上下に調整できるように配備したことを特徴とする請求Claims that are arranged so that they can be adjusted up and down
項1記載の培養装置。Item 1. The culture device according to item 1.
JP3287215A 1991-10-08 1991-10-08 Incubator Expired - Lifetime JPH0779677B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3287215A JPH0779677B2 (en) 1991-10-08 1991-10-08 Incubator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3287215A JPH0779677B2 (en) 1991-10-08 1991-10-08 Incubator

Publications (2)

Publication Number Publication Date
JPH0595779A JPH0595779A (en) 1993-04-20
JPH0779677B2 true JPH0779677B2 (en) 1995-08-30

Family

ID=17714543

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3287215A Expired - Lifetime JPH0779677B2 (en) 1991-10-08 1991-10-08 Incubator

Country Status (1)

Country Link
JP (1) JPH0779677B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2974814B1 (en) * 2011-05-06 2017-06-02 Acta Alga FIRMLY PHOTOBIOREACTOR FOR THE CULTURE OF PHOTOSYNTHETIC MICROORGANISMS
CN114052664B (en) * 2021-11-19 2024-03-29 上海市胸科医院 Method and device for monitoring tissue engineering curative effect

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58134989A (en) * 1982-02-03 1983-08-11 Mitsui Petrochem Ind Ltd Cylindrical rotary cultivation apparatus
JPH01289479A (en) * 1988-05-17 1989-11-21 Takashi Mori Rotational culturing vessel for plant
JPH03112481A (en) * 1989-09-26 1991-05-14 Hiroyuki Kikuchi Apparatus for culturing algae

Also Published As

Publication number Publication date
JPH0595779A (en) 1993-04-20

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