JPS63202371A - Spin culture apparatus - Google Patents
Spin culture apparatusInfo
- Publication number
- JPS63202371A JPS63202371A JP62036756A JP3675687A JPS63202371A JP S63202371 A JPS63202371 A JP S63202371A JP 62036756 A JP62036756 A JP 62036756A JP 3675687 A JP3675687 A JP 3675687A JP S63202371 A JPS63202371 A JP S63202371A
- Authority
- JP
- Japan
- Prior art keywords
- culture
- exhaust
- liquid
- tank
- exhaust pipe
- 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.)
- Pending
Links
- 239000007788 liquid Substances 0.000 claims abstract description 35
- 238000009423 ventilation Methods 0.000 claims description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 6
- 239000001301 oxygen Substances 0.000 claims description 6
- 229910052760 oxygen Inorganic materials 0.000 claims description 6
- 239000007789 gas Substances 0.000 claims description 5
- 238000007654 immersion Methods 0.000 claims 1
- 238000013019 agitation Methods 0.000 abstract description 7
- 238000005273 aeration Methods 0.000 abstract description 3
- 230000000903 blocking effect Effects 0.000 abstract 1
- 238000007598 dipping method Methods 0.000 abstract 1
- 238000003756 stirring Methods 0.000 description 7
- 238000004113 cell culture Methods 0.000 description 3
- 238000012258 culturing Methods 0.000 description 3
- 239000012531 culture fluid Substances 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 description 2
- 235000015097 nutrients Nutrition 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 206010011224 Cough Diseases 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 230000004663 cell proliferation Effects 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000001963 growth medium Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229930000044 secondary metabolite Natural products 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/50—Means for positioning or orientating the apparatus
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F29/00—Mixers with rotating receptacles
- B01F29/40—Parts or components, e.g. receptacles, feeding or discharging means
- B01F29/403—Disposition of the rotor axis
- B01F29/4033—Disposition of the rotor axis inclined
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F29/00—Mixers with rotating receptacles
- B01F29/60—Mixers with rotating receptacles rotating about a horizontal or inclined axis, e.g. drum mixers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/40—Mixers using gas or liquid agitation, e.g. with air supply tubes
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/10—Rotating vessel
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/06—Nozzles; Sprayers; Spargers; Diffusers
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/20—Degassing; Venting; Bubble traps
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Zoology (AREA)
- Wood Science & Technology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Organic Chemistry (AREA)
- Biomedical Technology (AREA)
- Microbiology (AREA)
- Sustainable Development (AREA)
- Biotechnology (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Clinical Laboratory Science (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
この発明はことに植物の細胞や組織(以下単に細胞等と
いう)を大量に効率よく培養するのに適した回転式培養
装置に関する。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates in particular to a rotary culture device suitable for efficiently culturing a large amount of plant cells and tissues (hereinafter simply referred to as cells).
従来技術
発酵分野におけるように微生物を大量に培養する場合に
は一般に、撹拌翼を備えた通気培養槽が使用されている
が、植物の細胞等を培養する場合にもこうした通気培養
槽を使用する試みがなされている。細胞等の培養装置に
おける撹拌は主として細胞等の沈澱を防ぎ、細胞等が増
殖するのに必要な栄養源や酸素と充分に接触させるため
におこなわれるが、植物の細胞等を培養する場合には、
微生物の場合と異なり、撹拌強度の影響を比較的受は易
く、撹拌強度が強過ぎると増殖の低下や停止を来たし、
その結果二次代謝産物の生産を効率よく行えないことが
多い、この点撹拌翼を使用するタイプの培養装置は攬袢
時に局部的に強い撹拌力が加わり、しかも撹拌翼の斜め
下方の培養槽底部付近に沈澱した細胞等が凝集する傾向
もあって細胞等の培養装置として使用するのは不向きで
ある。Conventional technology When cultivating microorganisms in large quantities as in the field of fermentation, aerated culture tanks equipped with stirring blades are generally used, but such aerated culture tanks are also used when cultivating plant cells, etc. Attempts are being made. Stirring in cell culturing equipment is mainly done to prevent cells from settling and to bring them into sufficient contact with the nutrients and oxygen necessary for cell proliferation, but when culturing plant cells, etc. ,
Unlike microorganisms, they are relatively susceptible to the influence of agitation intensity, and if agitation intensity is too strong, growth may decrease or stop.
As a result, the production of secondary metabolites often cannot be carried out efficiently.For this reason, in culture equipment that uses stirring blades, strong stirring force is applied locally at the time of loading, and the culture tank is located diagonally below the stirring blades. It is not suitable for use as a cell culture device because the cells that have settled near the bottom tend to aggregate.
こうした問題を解消するために培養槽自身が回転する回
転式円筒型培養装置を使用して植物の細胞等を培養する
試みもなされている。この方式の培養装置によれば、均
一な撹拌を行うことができるとともに回転数を適宜選択
することによって撹拌強度を自由に変えることができ、
また細胞等の沈澱や凝集を少なくすることができる等の
利点があり、近年この種の培養装置に関する改善提案も
いくつかなされている0日本発酵工学会講演要旨集、昭
和56年(1981年)247頁、特開昭58−134
989号等に示される如きものがそれである。In order to solve these problems, attempts have been made to culture plant cells and the like using a rotating cylindrical culture device in which the culture tank itself rotates. According to this type of culture device, it is possible to perform uniform stirring, and the stirring intensity can be freely changed by appropriately selecting the rotation speed.
It also has the advantage of being able to reduce sedimentation and aggregation of cells, etc., and several improvement proposals have been made for this type of culture device in recent years.0 Japanese Society of Fermentation Engineering Abstracts, 1981 247 pages, JP-A-58-134
This is the case as shown in No. 989.
発明が解決しようとする問題点
上述の回転式円筒型培養装置では、培養槽の軸心部に細
胞等や栄養源を含む培地を供給したり、生成物を含む培
養液を外部に排出するための供給排出管、培養液に酸素
を供給するためのエアーの給気管、排気口を培養液上方
に位置させたエアーの排気管等を通し、培養槽をその回
りに回転させるようにしているが、培養槽の回転に伴い
内壁面に付着する細胞等を含む培養液(以下単に培養液
等という)が滴下して排気口に付着し、それが次第にそ
の量を増して固化し、排気口を塞ぐことがある。とくに
排気口が上向きに向けられる場合、排気管内に培養液等
が入り込み詰りか生じ易くなる。Problems to be Solved by the Invention In the above-mentioned rotary cylindrical culture device, it is difficult to supply a culture medium containing cells, etc. and nutrients to the axial center of the culture tank, and to discharge a culture solution containing products to the outside. The culture tank is rotated around it through a supply and exhaust pipe, an air supply pipe for supplying oxygen to the culture solution, an air exhaust pipe with an exhaust port located above the culture solution, etc. As the culture tank rotates, the culture solution (hereinafter simply referred to as culture solution) containing cells, etc. that adheres to the inner wall surface drips and adheres to the exhaust port, which gradually increases in volume and solidifies, causing the exhaust port to It may get blocked. In particular, if the exhaust port is directed upward, culture fluid or the like may enter the exhaust pipe and cause clogging.
この発明は上記の問題を解消し、排気管の詰りを防止し
ようとするものである。This invention aims to solve the above problems and prevent clogging of the exhaust pipe.
問題点の解決手段
本発明はそのため排気路に接続される少くとも二個の互
いに連通ずる排気管の排気口を回転方向に適当間隔で培
養槽内に設けて培養槽と一体となって回転させ、これに
より各排気口の培養液への浸漬と浮−ヒを交互に繰返し
て排気管内の培養液等の固化を防止し、流動性を維持し
て−の排気口が培養液より浮上したとき管内の培養液等
が培養液側に流れ落ち、上記排気管と排出路が通気状態
に維持されるようにしたものである。すなわち本発明は
培養槽自身が回転して培養液を撹拌する回転式培養装置
において、培養液へ酸素含有ガスを供給する給気管と、
培養槽内に回転方向に適当間隔で設けられ、それぞれが
培養槽の回転に伴い培養液への浸漬と培養液からの浮上
とを交互に繰返す二個以上の排気口と、一端にそれぞれ
該排気口を備えて互いに連通し、培養槽と一体となって
回転するとともに固定の排気路と通気する排気管とを備
え、培養液等に浸される通気口より排気管内に入り込ん
だ培養液等が培養槽の回転による通気口の液面上への浮
上に伴い該管内を排気口側とは逆向きに流れ落ち、上記
排気管と排気路を通気状態にするようにしたことを特徴
とするものである。Means for Solving the Problems The present invention therefore provides at least two exhaust ports of mutually communicating exhaust pipes connected to an exhaust path, which are provided in the culture tank at appropriate intervals in the direction of rotation, and are rotated integrally with the culture tank. By doing this, each exhaust port is alternately immersed and floated in the culture solution to prevent the culture solution, etc. in the exhaust pipe from solidifying and maintain fluidity. The culture solution in the tube flows down to the culture solution side, and the exhaust pipe and discharge path are maintained in an aerated state. That is, the present invention provides a rotary culture device in which the culture tank itself rotates to agitate the culture solution.
Two or more exhaust ports are provided in the culture tank at appropriate intervals in the rotational direction, and each of them alternately immerses in the culture solution and floats up from the culture solution as the culture tank rotates, and the exhaust port is provided at one end. It is equipped with a vent that communicates with each other, rotates together with the culture tank, and has a fixed exhaust passage and an exhaust pipe that vents, and the culture solution, etc. that enters the exhaust pipe through the vent that is immersed in the culture solution, etc. It is characterized in that as the culture tank rotates, the liquid floats above the liquid surface at the vent and flows down the inside of the tube in the opposite direction to the exhaust port, thereby bringing the exhaust pipe and the exhaust path into a ventilated state. be.
培養槽は円筒形、球形、楕円形その他種々の形状のもの
を用いることができるが、そのなかで球形の培養槽を使
用するのが望ましい。Although various shapes such as cylindrical, spherical, elliptical, etc. can be used as the culture tank, it is preferable to use a spherical culture tank.
培養槽はまた水平軸線の回りを回転するようにしてもよ
いが、好ましくは排気路との連結部分に設けられる軸封
部分が上向きとなるように回転軸線を水平面に対し、傾
斜させるのが望ましく、とくに好ましくは5″″から4
5°の範囲に培養槽内に入れられる培養液の量によって
傾斜角度を調整できるようになっているのが望ましい、
培養液等を軸封部分に接触させると、細胞等が摺動面に
挟まれてt員傷したり雑菌で汚染されたりしがちである
が、軸封部分を上向きにして傾斜させることにより回転
式培養装置が有する利点を損なうことなく軸封部分に培
養液等が接触するのを防止することができ、したがって
細胞等の損傷や雑菌による汚染を防止して培養を長時間
円滑にかつ効率よく行うことができる。The culture tank may also rotate around a horizontal axis, but it is preferable that the axis of rotation be inclined with respect to the horizontal plane so that the shaft seal provided at the connection with the exhaust path faces upward. , particularly preferably from 5″″ to 4
It is desirable that the inclination angle can be adjusted within a range of 5° depending on the amount of culture solution put into the culture tank.
When a culture solution or the like comes into contact with the shaft seal, cells, etc. tend to get caught between the sliding surfaces and get damaged or contaminated with germs, but by tilting the shaft seal upward, rotation can be prevented. Without sacrificing the advantages of a type culture device, it is possible to prevent culture fluid from coming into contact with the shaft seal, thus preventing damage to cells and contamination by bacteria, allowing smooth and efficient culture for a long time. It can be carried out.
ここでいう酸素含有ガスとしては無菌処理したエアーが
代表的な例として挙げられる。A typical example of the oxygen-containing gas mentioned here is sterilized air.
給気管は給気口を培養液中に漬けるだけでもよいが、好
ましくはスパージャ−のような気体噴出用多孔中空体を
連結して培養液中に浸し、これより気体を噴出させるよ
うにする。これにより酸素移動容景係数(k、)を必要
な値まで高めることが容易にできるようになるとともに
培養槽自体の回転によるffl拌の他に通気撹拌も併せ
て行うことができるようになり、通気量と培養槽の回転
数を適宜選ぶことによって細胞の培養にとって好ましい
撹拌状態、すなわち細胞が損傷せず、溶存酸素量が充分
にあるなどの状態にして培養を行うことができる。The air supply pipe may be simply immersed in the culture solution at its air supply port, but preferably, a porous hollow body for blowing out gas, such as a sparger, is connected to the tube and immersed in the culture solution, from which gas is blown out. This makes it easy to increase the oxygen transfer visibility coefficient (k,) to the required value, and also allows for aeration agitation in addition to ffl agitation by rotating the culture tank itself. By appropriately selecting the amount of aeration and the rotational speed of the culture tank, it is possible to perform cell culture under agitation conditions that are favorable for cell culture, ie, in a state in which the cells are not damaged and there is a sufficient amount of dissolved oxygen.
培養槽の回転により培養液への浸漬と浮上を交互に繰返
す排気口は培養槽の回転持金ての排気口が一時的に培養
液に浸漬するようになっていてもよいが、好ましくは少
くとも一つの排気口が常に培養液の液面上に位置し露出
するようにされる。The exhaust port, which alternately immerses and floats in the culture solution as the culture tank rotates, may be such that the exhaust port of the rotating holder of the culture tank is temporarily immersed in the culture solution, but it is preferable that the exhaust port is temporarily immersed in the culture solution. One of the exhaust ports is always positioned above the surface of the culture solution and exposed.
各排気管は互いに直接連結され、連結部分より軸方向に
突出する分岐管を設けてもよいが(この場合該分岐管が
排気路に回転可能に連結される)、好ましくは排気路に
回転可能に接続される液溜りに連結される。この液溜り
には常に培養槽内の液面レベルと同一液面レベルの培養
液が貯えられ、液面上方において通気管及び通気路にそ
れぞれ通気される。Each exhaust pipe may be directly connected to each other, and a branch pipe may be provided that protrudes axially from the connecting portion (in this case, the branch pipe is rotatably connected to the exhaust pipe), but preferably the branch pipe is rotatably connected to the exhaust pipe. connected to a liquid reservoir connected to. This liquid reservoir always stores a culture liquid at the same liquid level as the liquid level in the culture tank, and is ventilated above the liquid level to the ventilation pipe and the ventilation path, respectively.
実施例
円筒形の培養槽1は上下方向に傾斜され、一端の斜め上
向きに突設される筒部2で架台3に、他端の斜め下向き
に突設される軸部4で架台5にそれぞれ回転可能に軸支
されている。そして筒部2内の一側面には断面が倒T形
の液溜り6が添設され、これより一対の排気管7が直径
方向に逆向きに伸び、培養槽1の一側面に排気口8を対
称位置に開口させている。液溜り6の端部は二重管構造
をなして小径部6bが大径部6aより突出し、通気室9
aと排気室9bよりなる空気室9(固定の排気路)の通
気室9aに上記大径部6aが、排気室9bに小径部6b
がそれぞれ回転可能に接続され、両者の接続部がメカニ
カルシールなど既知の方法によって軸封されている。空
気室9にはまた排気室9bに排気管1)が、通気室9a
に通気管12がそれぞれ連結される一方、大径部6aに
は通気室9aと連通ずる通気管13が連結され、該通気
管13は培養槽1に沿って下向きに伸び、下端付近で培
養槽内に突出し、突出端部に多孔中空体のスパージャ−
14を側面に隣接させて連結している。しかして無菌処
理されたエアーが通気管12、通気室9a及び通気管1
3を経てスパージャ−14より噴出される。なお培養槽
1の回転は例えば軸部4の延長上に回転数の調整操作が
可能な減速機を含む歯車伝動装置を設け、該装置にモー
タを連結して行われる。培養槽1にはまた培養液等15
が入れられ、液溜り6にも培養液等が入り込んで同一レ
ベルに維持されるが、入れられる培養液等の最大量は排
気口8と排気室9bの通気が維持され、かつ軸封部分が
培養液等に浸されない程度、すなわち図示する程度まで
にされる。Embodiment A cylindrical culture tank 1 is tilted in the vertical direction, and a cylindrical portion 2 protruding diagonally upward at one end is connected to a pedestal 3, and a shaft portion 4 protruding diagonally downward at the other end is connected to a pedestal 5. Rotatably supported. A liquid reservoir 6 with an inverted T-shaped cross section is attached to one side of the cylindrical portion 2, from which a pair of exhaust pipes 7 extend in opposite directions in the diametrical direction, and an exhaust port 8 is attached to one side of the culture tank 1. are opened at symmetrical positions. The end of the liquid reservoir 6 has a double pipe structure, with a small diameter part 6b protruding from a large diameter part 6a, and a ventilation chamber 9.
The air chamber 9 (fixed exhaust path) consisting of the air chamber 9a and the exhaust chamber 9b has the large diameter portion 6a in the ventilation chamber 9a, and the small diameter portion 6b in the exhaust chamber 9b.
are rotatably connected to each other, and the joints between the two are sealed by a known method such as a mechanical seal. The air chamber 9 also has an exhaust pipe 1) in the exhaust chamber 9b, and an exhaust pipe 1) in the ventilation chamber 9a.
A vent pipe 12 is connected to each of the vent pipes 12, and a vent pipe 13 that communicates with the vent chamber 9a is connected to the large diameter portion 6a. A sparger that protrudes inward and has a porous hollow body at the protruding end.
14 are connected adjacent to the sides. Thus, the sterilized air is transferred to the ventilation pipe 12, the ventilation chamber 9a and the ventilation pipe 1.
3 and is ejected from the sparger 14. The rotation of the culture tank 1 is carried out, for example, by providing a gear transmission device including a speed reducer capable of adjusting the rotation speed on an extension of the shaft portion 4, and connecting a motor to the device. Culture tank 1 also contains culture solution etc.
The culture solution, etc. enters the liquid reservoir 6 and is maintained at the same level, but the maximum amount of culture solution, etc. that can be put in is determined by maintaining ventilation between the exhaust port 8 and the exhaust chamber 9b, and by ensuring that the shaft seal part is kept at the same level. It is kept to the extent that it is not immersed in the culture solution, that is, to the extent shown in the figure.
本装置によれば、培養槽内の培養液等15は培養槽lの
回転に伴う撹拌とスパージャ−14から噴出するエアー
による通気撹拌とにより撹拌され、また一対の排気口8
は培養槽の回転に伴い培養槽等への浸漬と浮上を交互に
繰返し、液面上に浮上した排気口より液面に浮上したエ
アーが排出される。According to this device, the culture liquid etc. 15 in the culture tank is agitated by the rotation of the culture tank l and the ventilation agitation by the air ejected from the sparger 14, and also by the pair of exhaust ports 8.
As the culture tank rotates, it alternately dips into the culture tank and floats up, and the air that floats to the liquid surface is discharged from the exhaust port that floats above the liquid surface.
なお培養液等15の液面が図示するレベルにあるとき排
気管7が水平になると、再排気口8がともに一時的に培
養液等15に浸漬するようになるが、再排気口8がとも
に液中に浸漬するのは極く僅かな時間であり、排気に格
別支障をもう(ことはない。Note that if the exhaust pipe 7 becomes horizontal when the liquid level of the culture solution, etc. 15 is at the level shown in the figure, both the re-exhaust ports 8 will be temporarily immersed in the culture solution, etc. 15; The time it takes to be immersed in the liquid is extremely short, and there is no particular problem with evacuation.
発明の効果
本発明の回転式培養装置は以上のように、互いに連通す
る複数の排気管が培養槽と一体となって回転し、これに
より各排気口が培養液等への浸漬と浮上を交互に繰返し
て培養液等に浸される排気口を通じて排気等内に入り込
んだ培養液等を上記排気口の液面上への浮上に伴い排気
口と逆向きに、すなわち中心部側に流れ落し、排気路と
通気させるようにしたもので、排気口が浮上した際一部
の培養液等が管内に残留し、内壁面に付着するようなこ
とがあっても培養液等への漫消時に咳液と接触して流動
性を有するようになるため固化することがなく、したが
って管内の閉塞が防止され、通気性が維持される。Effects of the Invention As described above, in the rotary culture apparatus of the present invention, the plurality of exhaust pipes communicating with each other rotate together with the culture tank, and thereby each exhaust port alternately immerses and floats in the culture solution, etc. The culture solution, etc. that has entered the exhaust gas etc. through the exhaust port, which is repeatedly immersed in the culture solution, etc., flows in the opposite direction of the exhaust port, that is, toward the center, as it floats above the liquid surface of the above-mentioned exhaust port, It is designed to ventilate with the exhaust passage, so even if some of the culture solution, etc. remains in the tube when the exhaust port floats to the surface and adheres to the inner wall, it will prevent coughing when the culture solution, etc. Since it comes into contact with liquid and becomes fluid, it does not solidify, thus preventing clogging in the pipe and maintaining breathability.
図は本発明に係る回転式1g養装置の概略図である。
l・・培養槽 6・・液溜り 7・・排気管8・・
排気口 9・・空気室 1)・・排気管12.13
・・通気管 14・・スパージャ−15・・培養
液The figure is a schematic diagram of a rotary 1g feeding device according to the present invention. l...Culture tank 6...Liquid pool 7...Exhaust pipe 8...
Exhaust port 9...Air chamber 1)...Exhaust pipe 12.13
・・Vent pipe 14・・Sparger 15・・Culture solution
Claims (5)
養装置において、培養液へ酸素含有ガスを供給する給気
管と、培養槽内に回転方向に適当間隔で設けられ、それ
ぞれが培養槽の回転に伴い培養液への浸漬と培養液から
の浮上とを交互に繰返す二個以上の排気口と、一端にそ
れぞれ該排気口を備えて互いに連通し、培養槽と一体と
なって回転するとともに固定の排気路と通気する排気管
とを備え、培養液等に浸される通気口より排気管内に入
り込んだ培養液等が培養槽の回転による通気口の液面上
への浮上に伴い該管内を排気口側とは逆向きに流れ落ち
、上記排気管と排気路を通気状態にするようにしたこと
を特徴とする回転式培養装置(1) In a rotary culture device in which the culture tank itself rotates and agitates the culture solution, an air supply pipe that supplies oxygen-containing gas to the culture solution and an air supply pipe that is installed at appropriate intervals in the rotation direction in the culture tank, and each is connected to the culture tank. Two or more exhaust ports that alternately repeat immersion in the culture solution and floating from the culture solution as the tank rotates, and each have the exhaust ports at one end, communicate with each other, and rotate as one with the culture tank. At the same time, it is equipped with a fixed exhaust passage and an exhaust pipe for ventilation, and the culture solution, etc. that enters the exhaust pipe through the vent, which is immersed in the culture solution, floats to the liquid surface of the vent due to the rotation of the culture tank. A rotary culture device characterized in that the flow flows down the inside of the pipe in a direction opposite to the exhaust port side, so that the exhaust pipe and the exhaust path are in a ventilated state.
求の範囲第1項記載の回転式培養装置(2) The rotary culture device according to claim 1, wherein the culture tank is tilted with the exhaust port facing upward.
連結される特許請求の範囲第1項記載の回転式培養装置(3) The rotary culture device according to claim 1, wherein the exhaust pipe is connected to a liquid reservoir rotatably connected to the exhaust path.
許請求の範囲第1項乃至3項記載の回転式培養装置(4) The rotary culture device according to claims 1 to 3, wherein at least one exhaust port is always located above the liquid level.
結される特許請求の範囲第1項記載の回転式培養装置(5) The rotary culture device according to claim 1, wherein the air supply pipe is connected to a sparger that is immersed in a culture solution or the like.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62036756A JPS63202371A (en) | 1987-02-18 | 1987-02-18 | Spin culture apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62036756A JPS63202371A (en) | 1987-02-18 | 1987-02-18 | Spin culture apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63202371A true JPS63202371A (en) | 1988-08-22 |
Family
ID=12478586
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62036756A Pending JPS63202371A (en) | 1987-02-18 | 1987-02-18 | Spin culture apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63202371A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100365379B1 (en) * | 2000-07-27 | 2002-12-18 | 삼성종합화학주식회사 | A Reactor for Manufacture of a Chemicals |
JP2010524460A (en) * | 2007-04-20 | 2010-07-22 | コアステム シーオー エルティディ | Cell culture tube and mass cell culture apparatus including the same |
CN102154100A (en) * | 2011-01-07 | 2011-08-17 | 郑州威瑞生物技术有限公司 | Potential difference circulating bioreactor |
CN103764267A (en) * | 2011-09-02 | 2014-04-30 | 东洋炭素株式会社 | Powder stirring device |
-
1987
- 1987-02-18 JP JP62036756A patent/JPS63202371A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100365379B1 (en) * | 2000-07-27 | 2002-12-18 | 삼성종합화학주식회사 | A Reactor for Manufacture of a Chemicals |
JP2010524460A (en) * | 2007-04-20 | 2010-07-22 | コアステム シーオー エルティディ | Cell culture tube and mass cell culture apparatus including the same |
JP4948645B2 (en) * | 2007-04-20 | 2012-06-06 | コアステム シーオー エルティディ | Cell culture tube and mass cell culture apparatus including the same |
CN102154100A (en) * | 2011-01-07 | 2011-08-17 | 郑州威瑞生物技术有限公司 | Potential difference circulating bioreactor |
CN103764267A (en) * | 2011-09-02 | 2014-04-30 | 东洋炭素株式会社 | Powder stirring device |
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