JPS59220182A - Cultivation tank - Google Patents

Cultivation tank

Info

Publication number
JPS59220182A
JPS59220182A JP9345283A JP9345283A JPS59220182A JP S59220182 A JPS59220182 A JP S59220182A JP 9345283 A JP9345283 A JP 9345283A JP 9345283 A JP9345283 A JP 9345283A JP S59220182 A JPS59220182 A JP S59220182A
Authority
JP
Japan
Prior art keywords
permeable membrane
water
repellent gas
culture tank
gas
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
Application number
JP9345283A
Other languages
Japanese (ja)
Inventor
Makoto Shoda
誠 正田
Yoichi Ishikawa
陽一 石川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ishikawa Seisakusho Ltd
Original Assignee
Ishikawa Seisakusho Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Ishikawa Seisakusho Ltd filed Critical Ishikawa Seisakusho Ltd
Priority to JP9345283A priority Critical patent/JPS59220182A/en
Publication of JPS59220182A publication Critical patent/JPS59220182A/en
Pending legal-status Critical Current

Links

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
    • C12M23/00Constructional details, e.g. recesses, hinges
    • C12M23/20Material Coatings
    • 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
    • C12M23/00Constructional details, e.g. recesses, hinges
    • C12M23/24Gas permeable parts
    • 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
    • C12M29/00Means for introduction, extraction or recirculation of materials, e.g. pumps
    • C12M29/04Filters; Permeable or porous membranes or plates, e.g. dialysis
    • 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
    • C12M37/00Means for sterilizing, maintaining sterile conditions or avoiding chemical or biological contamination
    • 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
    • C12M41/00Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • C12M41/30Means for regulation, monitoring, measurement or control, e.g. flow regulation of concentration
    • C12M41/32Means for regulation, monitoring, measurement or control, e.g. flow regulation of concentration of substances in solution

Landscapes

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

Abstract

PURPOSE:To provide an aerobic cultivation tank free from ventilation and having little danger of the contamination with sundry germs, by using a water-repellent gas-permeable membrane as a part of the wall contacting with the liquid phase, and attaching a ventilation hole furnished with a water-repellent gas- permeable membrane to the wall contacting with the vapor phase. CONSTITUTION:In the cultivation tank composed of the top plate 1 made of stainless steel, the glass cylinder 2, etc., the bottom plate contacting with the liquid phase is composed of a water-repellent gas-permeable membrane 3, and a ventilation hole 11 furnished with a water-repellent gas-permeable membrane 12 is attached to the wall contacting with the vapor phase to equilibrate the pressure in the tank to atmosphere during the steam sterilization. The shielding of the cultivation tank from the outer atmosphere is made complete by the use of the above water-repellent gas-permeable membrane. The membrane is preferably porous Teflon film. Oxygen is permeated through the water-repellent gas-permeable membrane attached to the wall contacting with the liquid phase, and is dissolved in the culture liquid. The tank has various advantages such as the simplified structure, the lowered danger of the contamination with sundry germs, the retention of bubbles in the cultivation tank, etc.

Description

【発明の詳細な説明】 本発明は培養槽に係る。好気性培養では通常無菌空気を
培養槽に通気して培養する。しかし無菌空気を送るため
にその設備として圧縮空気が必要なばかりでな(、培養
槽にフィルター、空気の出入口、スパージャ−等が必要
になる。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a culture tank. In aerobic culture, sterile air is usually aerated into the culture tank. However, in order to deliver sterile air, not only compressed air is required as equipment (the culture tank also requires a filter, an air inlet/outlet, a sparger, etc.).

これらは装置を複雑にするとともに、雑菌汚染の原因に
なり、さらに泡が発生した場合空気出口から泡とともに
培養液がこぼれ出るおそれがある。また通気によって培
養液が蒸発し、液量の減少が著るしい。
These things complicate the device, cause bacterial contamination, and furthermore, if bubbles are generated, there is a risk that the culture solution will spill out from the air outlet along with the bubbles. In addition, the culture solution evaporates due to aeration, resulting in a significant decrease in the amount of the solution.

好気性培養を行なうに当り効率よく酸素ガスを送り培養
液中に速やかに溶存させる方法が特開昭54−9268
7号公報に教示されている。
JP-A-54-9268 discloses a method for efficiently sending oxygen gas and quickly dissolving it in the culture solution during aerobic culture.
It is taught in Publication No. 7.

これは通気性ある撥水性膜によって形成されたガス相に
酸素ガスを送入し、分圧差により当該膜を介して酸素を
培養液中に溶解させうるものである。
In this method, oxygen gas is introduced into a gas phase formed by an air-permeable water-repellent membrane, and the oxygen can be dissolved into the culture medium through the membrane due to a partial pressure difference.

本発明は上記方法を実現する装置の改良に関するもので
ある。すなわち、液相部に接触している壁の一部を撥水
性ガス透過膜で形成し、さらに気相部に接触する壁に通
気孔を設けたことを特徴とする培養槽である。
The present invention relates to an improvement of a device for implementing the above method. That is, the culture tank is characterized in that a portion of the wall in contact with the liquid phase portion is formed of a water-repellent gas-permeable membrane, and a vent hole is further provided in the wall in contact with the gas phase portion.

本発明は通気をしない好気培養槽を提供するものである
。すなわち本発明は壁の一部を撥水性ガス透過膜で構成
した培養槽であり、その気碧部に接触する壁に通気孔を
設け、蒸気殺菌の際圧バランスをとるのに有用である。
The present invention provides an aerobic culture tank without ventilation. That is, the present invention is a culture tank in which a part of the wall is made of a water-repellent gas-permeable membrane, and a ventilation hole is provided in the wall that contacts the aerobic part, which is useful for maintaining pressure balance during steam sterilization.

通気孔を気碧部と外界を遮断する撥水性ガス透過膜にて
形成すると培養槽と外界の遮断は完全になる。
If the ventilation holes are formed with a water-repellent gas-permeable membrane that blocks the atmosphere from the outside world, the culture tank will be completely isolated from the outside world.

培養槽は円筒状であり、その底面の一部または全部を撥
水性ガス透過膜で構成すると通常の通気式培養槽と同様
に用いることができる。撥水性ガス透過膜としては多孔
性テフロン膜を用いるとよい。この培養槽は通常の攪拌
翼を有する攪拌方式を用いてもよいし、培養槽を振とう
する方式を用いて攪拌してもよい。この培養槽を用いる
と酸素は液相部との接触壁に設けた撥水性ガス透過膜を
透過して培養液中に溶解する。
The culture tank is cylindrical, and if part or all of its bottom is made of a water-repellent gas-permeable membrane, it can be used in the same way as a normal aerated culture tank. A porous Teflon membrane is preferably used as the water-repellent gas-permeable membrane. This culture tank may be stirred using a stirring method using a normal stirring blade, or may be stirred using a method in which the culture tank is shaken. When this culture tank is used, oxygen passes through a water-repellent gas-permeable membrane provided on the wall in contact with the liquid phase and is dissolved in the culture solution.

この培養液を用いるとを気の出入口を他に設けなくても
よいので培養槽が密閉状態となり、設備が簡単になるば
かりでな(雑菌汚染の危険性外へ出ることはない等の利
点を生ずる。撥水性ガス透過膜を透過して培養液が蒸発
するがその蒸発量は通気した場合に比して著るしく小さ
い。
When this culture solution is used, there is no need to provide any other entrances and exits for the air, so the culture tank becomes airtight, which not only simplifies the equipment, but also has the advantage that there is no risk of bacterial contamination. The culture solution passes through the water-repellent gas-permeable membrane and evaporates, but the amount of evaporation is significantly smaller than that in the case of aeration.

また種々の微生物の酸素要求量に対応するには容積に対
する上記ガス透過膜の面積比を加減した培養槽を用いれ
ばよい。
Furthermore, in order to accommodate the oxygen demand of various microorganisms, a culture tank may be used in which the area ratio of the gas permeable membrane to the volume is adjusted.

気相部との接触壁に設けた通気孔は培養槽に培養液を入
れて蒸気殺菌する原種の内外を同一圧力にするのに必要
であり、これがないと液相部に接触している壁を形成す
る撥水性ガス透過膜に圧がかかり、膜を破損する危険性
がある。
Ventilation holes provided on the walls in contact with the gas phase are necessary to maintain the same pressure inside and outside of the original seeds to be steam sterilized by putting the culture solution into the culture tank. There is a risk that pressure will be applied to the water-repellent gas-permeable membrane that forms the membrane, causing damage to the membrane.

次に本発明を添付の図面に従って具体的に説明する。第
1図は本発明の実施例の上面図を、第2図はその縦断面
図を示す。培養槽はステンレス製天板1、ガラス円筒2
及び底面を撥水性ガス透過膜6で形成された容器であっ
て、ガラス円筒2の上下端をそれぞれゴムパツキン4で
密閉している。これらはステンレスリング5と天板1の
間を支柱6及びナツト7で固定しである。天板1にはP
H電極孔8、溶存酸素電極孔9、液フィード孔10及び
通気孔11の各ノズルがある。通気孔は植菌孔としても
用いられる。通気孔11には培養槽の気相部と外界を遮
断する撥水性ガス透過膜12を備えてあり、オートクレ
ーブ殺菌の際圧バランスをとるのに有効である。培養槽
内にはバッンルプレート161.<fイ14、軸受15
、回転軸16、タービン翼17、磁気式攪拌子18等が
備えである。底面の撥水性ガス透過膜6の下にワッシャ
ー19及び金網20を配置して培養液の重量を支持して
いる。この培養槽では酸素はガス透過膜6を透過して培
養液中に溶解する。この溶解速度はガス透過膜60面積
やガス透過性に依存する。ガス透過膜6としてはシリコ
ン薄ML、多孔性テフロン、合成樹脂膜、撥水処理した
金属網等各種用いることができるが、シリコン薄膜の透
過速度は多孔性テフロンに比して隆。以下で、耐熱性、
経済性、使い易さ等の観点からも多孔性テフロン膜がす
ぐれている。
Next, the present invention will be specifically described with reference to the accompanying drawings. FIG. 1 shows a top view of an embodiment of the present invention, and FIG. 2 shows a longitudinal sectional view thereof. The culture tank has 1 stainless steel top plate and 2 glass cylinders.
It is a container whose bottom surface is formed of a water-repellent gas-permeable membrane 6, and the upper and lower ends of the glass cylinder 2 are sealed with rubber gaskets 4, respectively. These are fixed between the stainless steel ring 5 and the top plate 1 with a support 6 and a nut 7. P on top plate 1
There are nozzles including an H electrode hole 8, a dissolved oxygen electrode hole 9, a liquid feed hole 10, and a ventilation hole 11. The vent hole is also used as an inoculation hole. The vent hole 11 is equipped with a water-repellent gas-permeable membrane 12 that blocks the gas phase of the culture tank from the outside world, and is effective for maintaining pressure balance during autoclave sterilization. There is a buntle plate 161 in the culture tank. < f i 14, bearing 15
, a rotating shaft 16, a turbine blade 17, a magnetic stirrer 18, and the like. A washer 19 and a wire mesh 20 are placed under the water-repellent gas-permeable membrane 6 on the bottom to support the weight of the culture solution. In this culture tank, oxygen passes through the gas permeable membrane 6 and dissolves in the culture solution. This dissolution rate depends on the area of the gas permeable membrane 60 and gas permeability. As the gas permeable membrane 6, various materials such as silicon thin ML, porous Teflon, synthetic resin membrane, water-repellent metal mesh, etc. can be used, but the permeation rate of the silicon thin film is higher than that of porous Teflon. Below, heat resistance,
Porous Teflon membranes are also superior in terms of economy and ease of use.

第6図は前実施例の回転機構すなわちステイ14、軸受
15、回転軸16、タービン翼17及び磁気式攪拌子1
8をはずした実施例で、これを回転または往復振とうし
ても、従来の三角7シスコや坂ロフラスコ等の振とう培
養槽と同様に使用できる。この培養槽を振と5すると従
来フラスコでは得られなかった培養液の情報を電極によ
って得ることができること、フラスコは手軽ではある反
面、攪拌式培養槽との相関が得に(いかったが、この培
養槽は形状が似ているので相関が得やすいこと、ガス透
過膜の選択によって高い酸素溶解速度が得られるのでフ
ラスコに比して菌濃度を高め、液量を増やすことができ
る等の利点を生ずる。この実施例で直径7cm、高さ1
4c1nの培養槽の底面をポアサイズ5ミクロン、厚さ
200ミクロンの多孔性テフロン膜で構成した場合と底
面を金属板で構成し内径25Tnmの通気孔にボl栓を
した場合とで酸素の透過速度を比較すると前者が約7倍
早かった。
FIG. 6 shows the rotating mechanism of the previous embodiment, namely the stay 14, bearing 15, rotating shaft 16, turbine blade 17, and magnetic stirrer 1.
8 is removed, and even if it is rotated or shaken reciprocally, it can be used in the same way as a conventional shaking culture tank such as a triangular 7 Cisco or Sakaro flask. By shaking this culture tank, you can obtain information about the culture solution using electrodes that could not be obtained with conventional flasks.Although flasks are convenient, the relationship with a stirred culture tank is advantageous (although it was good, this Culture tanks have advantages such as being similar in shape, making it easy to obtain correlations, and selecting a gas-permeable membrane to achieve a high oxygen dissolution rate, which allows for higher bacterial concentration and larger liquid volume compared to flasks. In this example, the diameter is 7 cm and the height is 1.
Oxygen permeation rate when the bottom of a 4c1n culture tank is made of a porous Teflon membrane with a pore size of 5 microns and a thickness of 200 microns, and when the bottom is made of a metal plate and the vent hole with an inner diameter of 25 Tnm is plugged with a bolt. When compared, the former was about 7 times faster.

この培養槽を回転振とうしながらブイヨン培地による雑
菌汚染テストを4日間行なったが汚染はなかった。この
テスト中培養液が蒸発して減少したので滅菌水を追加し
ながら行なった。
A bacterial contamination test using a bouillon medium was carried out for 4 days while rotating the culture tank, but no contamination was found. During this test, the culture solution evaporated and decreased, so sterile water was added during the test.

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

第1図及び第2図は本発明の一実施例の上面図及び縦断
面図を各々示す。 第3図は他の実施例の一部破さい断面図)第4図は通気
孔の他の実施例を示す。 符号の親羽 1  ステンレス天板 2  ガラス円筒 3  はっ水性ガス透過膜 4  ゴムパツキン 5  ステンレスリング 6  支柱 7  ナツト 8   p)I電極孔 9  溶存酸素電極孔 10  液フィード孔 11 通気孔 12 撥水性ガス透過膜 16 バッフルプレート 14 ステイ 15 軸受 16 回転軸 17 タービン翼 18 磁気式攪拌子 19 ワッシャー 20 金網 ′名 11ヨ ¥ 2 口 石 3 図 藁午)口
1 and 2 show a top view and a vertical sectional view, respectively, of an embodiment of the present invention. FIG. 3 is a partially cutaway sectional view of another embodiment) FIG. 4 shows another embodiment of the ventilation hole. Main wing of code 1 Stainless steel top plate 2 Glass cylinder 3 Water-repellent gas permeable membrane 4 Rubber gasket 5 Stainless steel ring 6 Support 7 Nut 8 p) I electrode hole 9 Dissolved oxygen electrode hole 10 Liquid feed hole 11 Vent hole 12 Water-repellent gas permeable Membrane 16 Baffle plate 14 Stay 15 Bearing 16 Rotating shaft 17 Turbine blade 18 Magnetic stirrer 19 Washer 20 Wire mesh Name 11Y 2 Mouth stone 3 Diagram

Claims (1)

【特許請求の範囲】 1 液相部に接触する壁の一部を撥水性ガス透過膜で形
成し、 $6 さらに気層部に接触する壁に通気孔を設けたことを特徴
とする培養槽。 2 撥水性ガス透過膜にて通気孔を形成したことを特徴
とする第1項記載の培養槽。 6、 培養槽は円筒状であり、その底面の一部または全
部を撥水性ガス透過膜で構成したことを特徴とする第1
項記載の培養槽。 4、 撥水性ガス透過膜が多孔性テフロン膜であること
を特徴とする第1項又は第2項に記載の培養槽。 5 培養槽が振とつ式であることを特徴とする第1項又
は第2項に記載の培養槽。
[Claims] 1. A culture tank characterized in that a part of the wall in contact with the liquid phase portion is formed of a water-repellent gas-permeable membrane, and further vent holes are provided in the wall in contact with the air layer portion. . 2. The culture tank according to item 1, characterized in that the ventilation holes are formed with a water-repellent gas-permeable membrane. 6. The first aspect, characterized in that the culture tank is cylindrical, and a part or all of the bottom of the tank is made of a water-repellent gas-permeable membrane.
Culture tank described in section. 4. The culture tank according to item 1 or 2, wherein the water-repellent gas-permeable membrane is a porous Teflon membrane. 5. The culture tank according to item 1 or 2, wherein the culture tank is of a shaking type.
JP9345283A 1983-05-27 1983-05-27 Cultivation tank Pending JPS59220182A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9345283A JPS59220182A (en) 1983-05-27 1983-05-27 Cultivation tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9345283A JPS59220182A (en) 1983-05-27 1983-05-27 Cultivation tank

Publications (1)

Publication Number Publication Date
JPS59220182A true JPS59220182A (en) 1984-12-11

Family

ID=14082714

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9345283A Pending JPS59220182A (en) 1983-05-27 1983-05-27 Cultivation tank

Country Status (1)

Country Link
JP (1) JPS59220182A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62187596U (en) * 1986-05-22 1987-11-28
US9255243B2 (en) * 2003-10-08 2016-02-09 Wilson Wolf Manufacturing Corporation Cell culture methods and devices utilizing gas permeable materials
US9290730B2 (en) 2005-07-26 2016-03-22 Corning Incorporated Multilayered cell culture apparatus
US9732317B2 (en) 2006-12-07 2017-08-15 Wilson Wolf Manufacturing Corporation Highly efficient gas permeable devices and methods for culturing cells

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62187596U (en) * 1986-05-22 1987-11-28
JPH0353676Y2 (en) * 1986-05-22 1991-11-25
US9255243B2 (en) * 2003-10-08 2016-02-09 Wilson Wolf Manufacturing Corporation Cell culture methods and devices utilizing gas permeable materials
US9410114B2 (en) 2003-10-08 2016-08-09 Wilson Wolf Manufacturing Cell culture methods and devices utilizing gas permeable materials
US9441192B2 (en) 2003-10-08 2016-09-13 Wilson Wolf Manufacturing Cell culture methods and devices utilizing gas permeable materials
USRE49293E1 (en) 2003-10-08 2022-11-15 Wilson Wolf Manufacturing Cell culture methods and devices utilizing gas permeable materials
US9290730B2 (en) 2005-07-26 2016-03-22 Corning Incorporated Multilayered cell culture apparatus
US9845451B2 (en) 2005-07-26 2017-12-19 Corning Incorporated Multilayered cell culture apparatus
US11274273B2 (en) 2005-07-26 2022-03-15 Corning Incorporated Multilayered cell culture apparatus
US11905506B2 (en) 2005-07-26 2024-02-20 Corning Incorporated Multilayered cell culture apparatus
US9732317B2 (en) 2006-12-07 2017-08-15 Wilson Wolf Manufacturing Corporation Highly efficient gas permeable devices and methods for culturing cells
US11377635B2 (en) 2006-12-07 2022-07-05 Wilson Wolf Manufacturing Corporation Highly efficient gas permeable devices and methods for culturing cells

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