JP2984748B2 - Method for culturing microorganisms using air-permeable membrane - Google Patents

Method for culturing microorganisms using air-permeable membrane

Info

Publication number
JP2984748B2
JP2984748B2 JP4719990A JP4719990A JP2984748B2 JP 2984748 B2 JP2984748 B2 JP 2984748B2 JP 4719990 A JP4719990 A JP 4719990A JP 4719990 A JP4719990 A JP 4719990A JP 2984748 B2 JP2984748 B2 JP 2984748B2
Authority
JP
Japan
Prior art keywords
culture
culturing
microorganism
tube
permeable membrane
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
JP4719990A
Other languages
Japanese (ja)
Other versions
JPH03251169A (en
Inventor
昭一 小林
輝夫 天知
尚人 池本
伸一 國崎
恭一 須川
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.)
NORINSUISANSHO SHOKUHIN SOGO KENKYUSHOCHO
SANTORII KK
Original Assignee
NORINSUISANSHO SHOKUHIN SOGO KENKYUSHOCHO
SANTORII KK
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 NORINSUISANSHO SHOKUHIN SOGO KENKYUSHOCHO, SANTORII KK filed Critical NORINSUISANSHO SHOKUHIN SOGO KENKYUSHOCHO
Priority to JP4719990A priority Critical patent/JP2984748B2/en
Publication of JPH03251169A publication Critical patent/JPH03251169A/en
Application granted granted Critical
Publication of JP2984748B2 publication Critical patent/JP2984748B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • C12M25/00Means for supporting, enclosing or fixing the microorganisms, e.g. immunocoatings
    • C12M25/10Hollow fibers or tubes
    • 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
    • C12M29/10Perfusion
    • 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)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Zoology (AREA)
  • Biomedical Technology (AREA)
  • Sustainable Development (AREA)
  • Microbiology (AREA)
  • Biotechnology (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Immunology (AREA)
  • Clinical Laboratory Science (AREA)
  • Analytical Chemistry (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Abstract

PURPOSE:To continuously and efficiently obtain a highly active enzyme liquid and a high concentration fungi liquid by culturing a microorganism using an air-transmissible membrane. CONSTITUTION:A liquid culture medium containing a microorganism other than mushrooms is fed through a pump 2 to a microorganism culturing system 3 in which an air-transmissible membrane such as a cloth or a sheet consisting of silicone and waterproofing-finished fiber is wound and then fed through a concentration-measuring equipment 3 and pump 4 to a culture liquid- exchanging and concentrating system 5. The microorganism is recovered and then the culture medium is circulated to liquid storage tank 6.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、通気性膜を用いた微生物の培養法に関し、
詳しくはシリコン製通気性膜から酸素を供給しながら連
続的に微生物を培養することを特徴とする微生物の培養
方法に関する。尚、本発明で言う微生物とはキノコ類お
よび藻類を除く微生物を意味し、細菌、酵母、カビ、放
線菌などが含まれる。
The present invention relates to a method for culturing microorganisms using a gas permeable membrane,
More specifically, the present invention relates to a method for culturing microorganisms, which comprises continuously culturing microorganisms while supplying oxygen from a gas permeable membrane made of silicon. In the present invention, the term "microorganism" refers to a microorganism other than mushrooms and algae, and includes bacteria, yeasts, molds, actinomycetes, and the like.

[従来の技術及び発明が解決しようとする課題] 微生物の培養法と言えば、通常はフスマ、大豆などを
用いた固体培養、フラスコ、ジャーファーメンターを用
いた液体培養である。特に、液体培養においては大量培
養が可能なことから工業的に一般に利用されており、滅
菌空気を吹き込み、滅菌培地を連続的に供給する連続培
養システムもある。しかし、これらの方法では、酸素供
給のための空気吹き込み、攪拌が必要であり、培養液の
取り出しも簡単ではない。
[Problems to be Solved by the Prior Art and the Invention] Speaking of the microorganism culturing method, it is usually a solid culture using a bran, a soybean, or the like, and a liquid culture using a flask or a jar fermenter. In particular, liquid culture is widely used industrially because large-scale culture is possible, and there is also a continuous culture system in which sterilized air is blown and a sterilized medium is continuously supplied. However, these methods require air blowing and stirring for oxygen supply, and it is not easy to remove the culture solution.

一般に好熱性菌の高温による培養では、菌の増殖が悪
く、酵素などの生産能が低く、実用化が困難であり、学
術的な研究が主であった。したがって、これまでの好熱
性菌類の培養では、生産される酵素剤が高価となるの
で、現状では食品工業への応用はほとんど不可能であ
る。
Generally, when thermophilic bacteria are cultured at a high temperature, the growth of the bacteria is poor, the productivity of enzymes and the like is low, and it is difficult to put them to practical use. Therefore, in the conventional culture of thermophilic fungi, the enzyme agent produced is expensive, and at present it is almost impossible to apply it to the food industry.

[課題を解決するための手段] そこで本発明者らは好熱性酵素産生菌、さらには好熱
性酵素の生産コストを培養の効率化、連続化によって低
減化することを試み、鋭意検討の結果、通気性膜を利用
することにより効率的に微生物を連続生産できることを
見い出し、本発明を完成したのである。
[Means for Solving the Problems] The present inventors have tried to reduce the production cost of thermophilic enzyme-producing bacteria, and furthermore, the production cost of thermophilic enzymes by increasing the efficiency and continuity of cultivation. The present inventors have found that microorganisms can be continuously produced efficiently by using a gas permeable membrane, and have completed the present invention.

本発明の方法では各種の通気性膜が利用できるが、水
を通さず(水蒸気は通しても、通さなくてもいずれでも
よい)酸素、炭酸ガスを通し、オートクレーブでき、機
械的強度の強いものが望ましい。
Although various air-permeable membranes can be used in the method of the present invention, those which can be autoclaved by passing oxygen or carbon dioxide gas without passing water (which may or may not pass water vapor) and having high mechanical strength can be used. Is desirable.

ポリエチレンでの酸素透過性は30μmの厚さでも25℃
において最大で6,000cc/m2・day・atmであり、炭酸ガス
透過性は本値の3〜4倍である。しかし、最近開発され
たシリコンでの透過性は100μmの厚さでも酸素で365,0
00cc/m2・day・atm、炭酸ガスで1,165,000cc/m2・day・
atmにも達する。そこで本発明者らは本素材および各種
通気性膜での微生物培養について鋭意検討し、通気性膜
を用いれば、微生物培養が従来より効率的に、連続的に
高活性酵素液、高濃度菌液を得られることを見い出し
て、本発明を完成したのである。
Oxygen permeability of polyethylene is 25 ℃ even at 30μm thickness
, The maximum is 6,000 cc / m 2 · day · atm, and the carbon dioxide permeability is 3 to 4 times this value. However, the permeability of recently developed silicon is 365,0 with oxygen even at a thickness of 100 μm.
00cc / m 2 · day · atm , 1,165,000cc / m 2 · day · in carbon dioxide
Atm also reaches. Therefore, the present inventors have studied diligently about the microorganism cultivation with the present material and various gas permeable membranes, and by using the gas permeable membrane, the microorganism cultivation is more efficient than in the past, and the highly active enzyme solution and the high concentration bacterial solution are continuously obtained. Thus, the present invention has been completed.

本発明を以下に示す。 The present invention is described below.

本発明は管状のシリコン製通気性膜を用いた微生物の
培養方法に関するものである。詳しくは、 (1)管状のシリコン製通気性膜の管内に、連続的に接
種培地および/または液体培地を供給して微生物(キノ
コ類および藻類を除く)を培養することを特徴とする微
生物(キノコ類および藻類を除く)の培養方法。
The present invention relates to a method for culturing microorganisms using a tubular silicon gas permeable membrane. Specifically, (1) a microorganism characterized by culturing microorganisms (excluding mushrooms and algae) by continuously supplying an inoculation medium and / or a liquid medium into a tube of a tubular silicon gas-permeable membrane ( Culture method (excluding mushrooms and algae).

(2)管状のシリコン製通気性膜を基材の外表面に固定
して用いることを特徴とする微生物(キノコ類および藻
類を除く)の培養方法。
(2) A method for culturing microorganisms (excluding mushrooms and algae), which comprises using a tubular silicon gas-permeable membrane fixed to the outer surface of a substrate.

(3)管状のシリコン製通気性膜の管内で、培養液を濃
縮しながら培養することを特徴とする微生物(キノコ類
および藻類を除く)の培養方法。
(3) A method for culturing microorganisms (excluding mushrooms and algae), which comprises culturing the culture solution while concentrating the culture solution in a tube made of a tubular silicon gas-permeable membrane.

(4)培養終了後の培養液を管状のシリコン製通気性膜
の管内を通過させて濃縮することを特徴とする微生物
(キノコ類および藻類を除く)の培養方法。
(4) A method for culturing microorganisms (excluding mushrooms and algae), wherein the culture solution after completion of the culturing is passed through a tube of a gas-permeable silicon membrane and concentrated.

通気性膜の中、現在のところ本発明の方法に最適な素
材はシリコンであり、加工の仕方によって通気性を所望
の程度に変えることができ、また機械的強度が強いため
にシステムとして利用しやすい。また、シート状、管
状、その他各種の形状に加工でき、極めて有用な素材で
ある。最近、本素材を細管状に加工し、人工肺に用いて
いるが、これは本素材の通気性を利用したものである。
本性質を微生物培養に利用したものが本発明の方法であ
り、これまで本素材を何人も微生物培養に利用した例は
なく、ましてや、培養に成功した例はない。また、本発
明の方法では素材としてシリコンに限らず、セルロー
ス、セラミックスなどの表面を防水加工したもの、その
他、通気性に優れた素材であれば利用できる。
Among the breathable membranes, silicon is currently the most suitable material for the method of the present invention, and the breathability can be changed to a desired degree depending on the processing method, and the mechanical strength is high. Cheap. Further, it is a very useful material that can be processed into a sheet shape, a tubular shape, and other various shapes. Recently, this material has been processed into a thin tube and used for an artificial lung, which utilizes the breathability of the material.
The method of the present invention uses this property for culturing microorganisms. There is no example of using this material for culturing microorganisms, and there is no example of successful culturing. Further, in the method of the present invention, the material is not limited to silicon, but any material having excellent air permeability, such as a material obtained by waterproofing the surface of cellulose, ceramics, or the like, can be used.

シリコン素材は疎水性表面をもつために培養液の通過
が容易であり、高濃度培養液でも通過でき、本培養シス
テムでは通気性が著しく優れていることから酸素要求量
に応じて酸素が膜を通過する。
Since the silicon material has a hydrophobic surface, it can easily pass through the culture medium, and can pass through even high-concentration culture medium.This culture system has a remarkably excellent air permeability. pass.

シリコンの形状は微生物の培養に適合するものであれ
ば、特に制限はないが、管状が便利である。
The shape of silicon is not particularly limited as long as it is suitable for culturing microorganisms, but a tubular shape is convenient.

管の大きさは管の厚さにより適当に選択するが、例え
ば、100μmの厚さでは管径3.0×3.2mm、200μmの厚さ
では3.6×4.0mm程度が適当である。平膜の場合は300×3
00mm角を用い、底をメッシュで補強する。
The size of the tube is appropriately selected depending on the thickness of the tube. For example, a tube diameter of 3.0 × 3.2 mm for a thickness of 100 μm and a size of 3.6 × 4.0 mm for a thickness of 200 μm are appropriate. 300 × 3 for flat membrane
Using a 00 mm square, the bottom is reinforced with a mesh.

200μmの管を用いた場合、図1のように、基材の外
表面に円筒に巻き付ける、水平および/または垂直に置
くなどする。平板上に管を並べた場合は、通気の効率を
考慮し、少しずつスペースを設け、10段以上にも重ねる
ことができる。基本的には、このように設備した長い管
に培養液を循環または通過させるが、適当な箇所(図1
の補助培地タンク参照)に液面を一定に保てる貯液槽を
付けると便利である。貯液槽はシステム内の液量を一定
に保ち、新しい培地を常に補給できるようにセットして
おくとよい。
When a 200 μm tube is used, as shown in FIG. 1, the tube is wound around a cylinder on the outer surface of the substrate, or placed horizontally and / or vertically. When the pipes are arranged on a flat plate, a space can be provided little by little in consideration of the efficiency of ventilation, and the pipes can be stacked in ten or more stages. Basically, the culture solution is circulated or passed through a long tube provided in such a manner.
It is convenient to attach a storage tank that can keep the liquid level constant to the auxiliary medium tank. The storage tank is preferably set so that the amount of liquid in the system is kept constant and a fresh medium can always be supplied.

また、本発明の方法では、20m以上の長い管を用いた
り、乾燥条件下では、培養液が極端に濃縮され、通液が
困難となったり、細菌の増殖速度が低下することがある
ので、この他、逆流止めを備えた新鮮培地(培地濃度は
任意に選択する)供給装置をつけるとよい。
In addition, in the method of the present invention, a long tube of 20 m or more is used, or under a dry condition, the culture solution is extremely concentrated, and it becomes difficult to pass the solution, or the growth rate of bacteria may be reduced. In addition, a fresh medium (medium concentration is arbitrarily selected) supply device provided with a backflow stopper may be provided.

さらに、微生物の種類、培養条件によっては培養時間
の経過とともに増殖阻害物質が蓄積して増殖速度が低下
することもある。このような場合、システムの適当な箇
所に限外濾過膜または菌を通過させず、その他の成分を
通過させる通常の濾過素材、透析膜をセットし、増殖阻
害物質を除去しながら連続培養する。この方式によれ
ば、微生物が生産する各種物質を連続的に取り出すこと
もできる。
Furthermore, depending on the type of microorganism and the culturing conditions, the growth inhibitory substance may accumulate over the culturing time and the growth rate may decrease. In such a case, an ordinary filtration material and a dialysis membrane that allow other components to pass therethrough without passing through an ultrafiltration membrane or a bacterium to an appropriate portion of the system are set, and continuous culture is performed while removing growth inhibitors. According to this method, various substances produced by microorganisms can be continuously taken out.

シリコン管を用いた本培養法では、管の長さ、流量を
調節してセットしさえすればよい。
In the main culture method using a silicon tube, the length and flow rate of the tube need only be adjusted and set.

初発菌液の濃度、培養済み菌液の引出しの量比は培養
速度、その他の条件により任意に選択すればよいが、通
常は種菌液を2〜10%を新鮮培地に加えて出発液とすれ
ば、2日で培養は完了する。
The concentration of the initial bacterial solution and the ratio of the amount of the cultured bacterial solution to be withdrawn may be arbitrarily selected depending on the culture rate and other conditions. Usually, 2 to 10% of the inoculum solution is added to a fresh medium, and the starting solution is prepared. For example, the culture is completed in two days.

培養終了液は次の種菌として一部を出発槽に戻して新
鮮培地を追加し、培養を続行すればよい。
A part of the culture termination solution may be returned to the starting tank as the next inoculum, a fresh medium may be added, and the culture may be continued.

管の末端で培養が終了するように流速、管の長さを調
節すれば、単に管を通過させるだけでよいが、管の長さ
をこの半分にすれば2回循環させた後、98〜90%の培養
液を引き出して、新鮮培地を追加し培養を続ける。
If the flow rate and the length of the tube are adjusted so that the culture is completed at the end of the tube, it is sufficient to simply pass through the tube. Withdraw 90% of the culture, add fresh medium and continue culturing.

培養液濃度は分光光度計で測定し、一定以上の吸光度
に達っしたら、自動的に引出し、新鮮培地を加えるよう
にセットすることもできる。
The concentration of the culture solution is measured by a spectrophotometer, and when the absorbance reaches a certain level or more, the medium can be automatically withdrawn and set to add a fresh medium.

微生物の種類としては前述の如く、キノコ類および藻
類以外であればよく、例えば好熱菌のサーマス属、バチ
ルス属のステアロサーモフィルスなどで効率的に適用で
きる、この他、通常のバチルス属菌、シュードモナス属
菌、乳酸菌、ストレプトマイセス属菌、光合成菌、その
他多くの種類があるが、いずれでも本発明の方法が適用
できる。また、これらを二種以上混合して培養すること
もできる。さらに、動物、植物の、細胞および/または
組織の培養にも本発明の方法を適用できる。
As described above, the type of microorganism may be other than mushrooms and algae, and can be efficiently applied to, for example, thermophilic bacteria of the genus Thermus and Bacillus, such as stearothermophilus. Pseudomonas, lactic acid bacteria, Streptomyces, photosynthetic bacteria, and many other types, and the method of the present invention can be applied to any of them. Further, two or more of these can be mixed and cultured. Furthermore, the method of the present invention can be applied to cell and / or tissue culture of animals and plants.

[実施例] 次に実施例を以て本発明をさらに詳細かつ具体的に説
明するが、これらに限定されるものではない。
EXAMPLES Next, the present invention will be described in more detail and specifically with reference to Examples, but it should not be construed that the invention is limited thereto.

実施例1 菌株としてサイクロデキストリン合成酵素を生産する
バチルス属好熱性菌KF9−10(FERM P−8718)を用い、
培地としてフスマ、硫安、炭カル培地を用いて、65℃、
4ml/minの流速で培養した。システムは図1のような形
であり、厚さ200μm、管径3.6×4.0mmのシリコン管10m
をアクリル板上にセットし、培地供給装置を付けた200m
lの貯槽に液面を1cm以下にしたものである。植菌液を
(培地供給装置を除く)システム全体に満たし、ペリス
タリックポンプを用いて循環培養した結果、2日で0.5T
HU/mlのサイクロデキストリン合成酵素活性をもつ培養
液が得られた。尚、対照として500mlの三角フラスコに1
00mlの培地を容れて培養した結果は0.01〜0.05THU/mlで
あった。
Example 1 A thermophilic bacterium belonging to the genus Bacillus KF9-10 (FERM P-8718) which produces cyclodextrin synthase was used as a strain.
Using bran, ammonium sulfate, charcoal medium as a medium, 65 ° C,
The cells were cultured at a flow rate of 4 ml / min. The system has a shape as shown in Fig. 1, a silicon tube 10m with a thickness of 200μm and a diameter of 3.6 x 4.0mm.
Set on an acrylic plate, 200 m
The liquid level is set to 1 cm or less in the storage tank of l. As a result of inoculating the inoculum into the entire system (excluding the medium supply device) and circulating culture using a peristaltic pump, 0.5 T was obtained in 2 days.
A culture solution having a cyclodextrin synthase activity of HU / ml was obtained. As a control, place 1 in a 500 ml Erlenmeyer flask.
The result of culturing in a medium containing 00 ml was 0.01 to 0.05 THU / ml.

実施例2 厚さ100μm、管径3.6×4.0mmのシリコン管10mをアク
リル板上にセットした以外は、実施例1と同様にし、1T
HU/mlの酵素活性をもつ溶媒液を得た。
Example 2 1T, except that a silicon tube 10 m having a thickness of 100 μm and a diameter of 3.6 × 4.0 mm was set on an acrylic plate.
A solvent solution having an enzyme activity of HU / ml was obtained.

実施例3 過度な乾燥を防止するために水蒸気飽和チャンバー内
で実施例1と同様に培養した結果、0.8THU/mlの酵素活
性をもつ培養液を得た。また、管の中間に1/2希釈培地
の補給装置を付けて循環培養した結果、活性は1.2THU/m
lに上昇した。
Example 3 As a result of culturing in a water vapor saturation chamber in the same manner as in Example 1 to prevent excessive drying, a culture solution having an enzyme activity of 0.8 THU / ml was obtained. In addition, as a result of circulating culturing with a 1/2 dilution medium replenishing device in the middle of the tube, the activity was 1.2 THU / m
l rose.

実施例4 厚さ200μm、管径3.6×4.0mmのシリコン管230mをア
クリル板にセットし、スペース5〜10cmをとって、5段
にし、各段毎に通常の培養に用いる1/2〜1/10の濃度の
培地を含む希薄培地補給装置を付け、流速2ml/minで培
養した結果、2日培養後から0.5THU/mlの酵素活性をも
つ培養液が連続的に得られた。また、この培養液を同じ
シリコン管に、乾燥状態で通過させると2mで1/4まで濃
縮された。
Example 4 A silicon tube 230 m having a thickness of 200 μm and a tube diameter of 3.6 × 4.0 mm was set on an acrylic plate, and a space of 5 to 10 cm was taken to form 5 stages, and each stage was used for normal culture. As a result of culturing at a flow rate of 2 ml / min with a diluted medium supply device containing a medium having a concentration of / 10, a culture solution having an enzyme activity of 0.5 THU / ml was continuously obtained after 2 days of culture. When this culture solution was passed through the same silicon tube in a dry state, it was concentrated to 2/4 at 2 m.

[発明の効果] 本発明の方法によれば、これまで好気性菌の培養で主
として使用されてきたジャーファーメンターでの培養と
比べてより効率的となり、連続化が著しく簡単になるの
で、微生物による酵素生産、有用物質の生産に広く適用
できる。特に、高温での培養では溶存酸素量が少なく、
微生物の生産能が十分に発揮できない場合が多いようで
あるが、本発明の方式を用いれば、必要に応じて酸素の
供給ができ、酵素などの有用物質の生産が安定化され、
さらに生産能が高くなる。また、本培養法は各種装置と
の組合せが容易にでき、有用物質の連続生産のために限
外濾過膜を組合せれば、培地の補給にも便利である。
[Effects of the Invention] According to the method of the present invention, culturing in a jar fermenter, which has been mainly used in culturing aerobic bacteria, becomes more efficient, and continuity is greatly simplified. Widely applicable to the production of enzymes and useful substances. In particular, when cultured at high temperature, the amount of dissolved oxygen is small,
It seems that in many cases, the ability to produce microorganisms cannot be sufficiently exhibited.However, if the method of the present invention is used, oxygen can be supplied if necessary, and the production of useful substances such as enzymes is stabilized,
Further, the productivity is increased. In addition, the main culturing method can be easily combined with various devices, and if an ultrafiltration membrane is combined for continuous production of a useful substance, the medium can be conveniently supplied.

さらに光合成菌でも本発明の方法を応用でき、例え
ば、光照射をしながら連続培養できる。
Furthermore, the method of the present invention can be applied to photosynthetic bacteria, for example, continuous culture can be performed while irradiating light.

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

第1図はシリコン管を筒型にセットしたシステム全体を
示したものである。本システムは培養管を中心とし、貯
槽(リザーブタンク)、培地または水供給装置(補助培
地タンク)、濃縮または透析装置(培地交換、濃縮シス
テム)、自動濃度センサーからなり、必要に応じて組み
合わせることができる。
FIG. 1 shows the entire system in which a silicon tube is set in a cylindrical shape. This system mainly consists of a culture tube, a storage tank (reservoir tank), a medium or water supply device (auxiliary medium tank), a concentration or dialysis device (medium exchange, concentration system), and an automatic concentration sensor, which can be combined as necessary. Can be.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 國崎 伸一 大阪府茨木市双葉町16丁目16番地3号 (72)発明者 須川 恭一 大阪府高槻市氷室町1丁目1番地10号 (56)参考文献 特開 昭51−110089(JP,A) 特開 昭56−61988(JP,A) 特開 昭52−122687(JP,A) (58)調査した分野(Int.Cl.6,DB名) C12N 1/00 - 7/08 C12M 1/00 - 3/10 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Shinichi Kunizaki 16-16-16 Futaba-cho, Ibaraki-shi, Osaka (72) Inventor Kyoichi Sugawa 1-1-1 Himurocho, Takatsuki-shi, Osaka (56) Reference Document JP-A-51-110089 (JP, A) JP-A-56-61988 (JP, A) JP-A-52-122687 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) C12N 1/00-7/08 C12M 1/00-3/10

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】管状のシリコン製通気性膜の管内に、連続
的に接種培地および/または液体培地を供給して微生物
(キノコ類および藻類を除く)を培養することを特徴と
する微生物(キノコ類および藻類を除く)の培養方法。
1. A microorganism (mushroom) characterized by culturing microorganisms (excluding mushrooms and algae) by continuously supplying an inoculation medium and / or a liquid medium into a tube of a tubular silicone gas permeable membrane. Cultivation method (excluding species and algae).
【請求項2】管状のシリコン製通気性膜を基材の外表面
に固定して用いることを特徴とする請求項1記載の培養
方法。
2. The culture method according to claim 1, wherein a tubular silicon gas-permeable membrane is used by fixing it to the outer surface of the substrate.
【請求項3】管状のシリコン製通気性膜の管内で、培養
液を濃縮しながら培養することを特徴とする請求項1記
載の培養方法。
3. The culturing method according to claim 1, wherein the culturing is performed while concentrating the culture solution in a tube of a tubular silicon gas permeable membrane.
【請求項4】培養終了後の培養液を管状のシリコン製通
気性膜の管内を通過させて濃縮することを特徴とする請
求項1記載の培養方法。
4. The culture method according to claim 1, wherein the culture solution after completion of the culture is passed through a tubular gas-permeable silicon membrane to be concentrated.
JP4719990A 1990-03-01 1990-03-01 Method for culturing microorganisms using air-permeable membrane Expired - Lifetime JP2984748B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4719990A JP2984748B2 (en) 1990-03-01 1990-03-01 Method for culturing microorganisms using air-permeable membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4719990A JP2984748B2 (en) 1990-03-01 1990-03-01 Method for culturing microorganisms using air-permeable membrane

Publications (2)

Publication Number Publication Date
JPH03251169A JPH03251169A (en) 1991-11-08
JP2984748B2 true JP2984748B2 (en) 1999-11-29

Family

ID=12768464

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4719990A Expired - Lifetime JP2984748B2 (en) 1990-03-01 1990-03-01 Method for culturing microorganisms using air-permeable membrane

Country Status (1)

Country Link
JP (1) JP2984748B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU722744B2 (en) * 1996-12-30 2000-08-10 Toshirou Sekine Apparatus for culturing microalgae

Also Published As

Publication number Publication date
JPH03251169A (en) 1991-11-08

Similar Documents

Publication Publication Date Title
US4442206A (en) Method of using isotropic, porous-wall polymeric membrane, hollow-fibers for culture of microbes
EP1751269B1 (en) Membrane bioreactor
US4440853A (en) Microbiological methods using hollow fiber membrane reactor
JPH03164169A (en) Cell culture
Robertson et al. Dual aerobic hollow‐fiber bioreactor for cultivation of Streptomyces aureofaciens
Roy et al. Microbial hollow fiber bioreactors
Chung et al. Aerobic fungal cell immobilization in a dual hollow‐fiber bioreactor: Continuous production of a citric acid
US5342765A (en) Method of producing extracellular products from aerobic microorganisms
Ogawa et al. Production of kojic acid by membrane-surface liquid culture of Aspergillus oryzae NRRL484
Ichii et al. Development of a new commercial-scale airlift fermentor for rapid growth of yeast
JP2984748B2 (en) Method for culturing microorganisms using air-permeable membrane
JPS63248396A (en) Production of dihydrooxoisophorone
JPH01225475A (en) Culture apparatus
JPS5743685A (en) L-glutamic oxidase
JPH0659206B2 (en) Bioreactor
FI85503B (en) FOERFARANDE FOER FRAMSTAELLNING AV POLYOLER GENOM PAO INDUSTRIELL SKALA BASERAD FERMENTATION AV SOCKER.
CA1210719A (en) Method of immobilizing enzymes
JPH09155388A (en) Denitrification device using biological catalyst
Sheldon et al. An investigation of biphasic growth kinetics for Phanerochaete chrysosporium (BKMF-1767) immobilised in a membrane gradostat reactor using flow-cells
WO2001058501A1 (en) Apparatus and process for removal of carbon dioxide in a bioreactor system
JPH0740916B2 (en) Bioreactor for alcohol fermentation
FR2238759A1 (en) Bacterial cell concentrates - for inoculating milk or starter solns in cheese mfr. produced by diffusion fermentation
Chung et al. Hollow fiber bioreactors with internal aeration circuits
CN118006432A (en) Biological induction hollow fiber membrane and CO2Preparation method of microalgae-trapping culture reactor
JPH0279974A (en) Biocatalyst and bioreactor using the same

Legal Events

Date Code Title Description
S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

EXPY Cancellation because of completion of term