JPH07177876A - Culture management method - Google Patents

Culture management method

Info

Publication number
JPH07177876A
JPH07177876A JP5346562A JP34656293A JPH07177876A JP H07177876 A JPH07177876 A JP H07177876A JP 5346562 A JP5346562 A JP 5346562A JP 34656293 A JP34656293 A JP 34656293A JP H07177876 A JPH07177876 A JP H07177876A
Authority
JP
Japan
Prior art keywords
culture
concentration
osmotic pressure
microorganisms
glucose
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
JP5346562A
Other languages
Japanese (ja)
Inventor
Kazuhito Hayakawa
和仁 早川
Satogo Takeuchi
聡吾 竹内
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.)
Yakult Honsha Co Ltd
Original Assignee
Yakult Honsha Co 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 Yakult Honsha Co Ltd filed Critical Yakult Honsha Co Ltd
Priority to JP5346562A priority Critical patent/JPH07177876A/en
Publication of JPH07177876A publication Critical patent/JPH07177876A/en
Pending legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

Landscapes

  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Abstract

(57)【要約】 【目的】 微生物の培養管理方法を提供する。 【構成】 微生物(細胞を含む)の培養の管理方法にお
いて、培養工程における培養液の浸透圧の値を指標にし
て、培養を管理する微生物(細胞を含む)の培養管理方
法。更には、予め、培養工程における培養液の浸透圧の
値と、培養液の基質濃度、代謝産物濃度、または微生物
(細胞を含む)濃度の少なくとも1種の値との相関関係
を求め、これを指標にして、培養を管理する微生物(細
胞を含む)の培養管理方法。 【効果】 微生物(細胞を含む)の培養による物質生
産、細胞増殖などのプロセスにおける培養状態の監視及
び制御等を簡便、かつ迅速に行うことができる。
(57) [Summary] [Purpose] To provide a method for controlling the culture of microorganisms. In the method for controlling the culture of microorganisms (including cells), the method for controlling the culture of microorganisms (including cells) is used to control the culture using the osmotic pressure value of the culture solution in the culture step as an index. Furthermore, the correlation between the osmotic pressure value of the culture solution in the culture step and at least one value of the substrate concentration, the metabolite concentration, or the microorganism (including cells) concentration of the culture solution is obtained in advance, and this is calculated. A method for controlling the culture of microorganisms (including cells) that controls the culture as an index. [Effect] It is possible to easily and quickly perform monitoring and control of a culture state in processes such as substance production by culturing microorganisms (including cells) and cell proliferation.

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、及び動物、植
物などの細胞の培養の管理方法に関するものであり、更
に詳しくは、乳酸発酵、アルコール発酵、アミノ酸発酵
等に代表される食品分野、また、抗生物質発酵生産、生
理活性物質発酵生産等に代表される医薬品分野、動物細
胞、植物細胞の増殖等に代表される農業分野、及びその
他の分野における微生物、及び動物、植物などの細胞の
培養による物質生産、細胞増殖などのプロセスの監視及
び制御などに適用するのに有用な当該微生物(細胞を含
む)の培養管理方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for controlling the culture of microorganisms and cells of animals, plants and the like. More specifically, the field of foods represented by lactic acid fermentation, alcoholic fermentation, amino acid fermentation and the like, In addition, fermentation of antibiotics, pharmaceutical fields represented by fermentation of physiologically active substances, animal cells, agricultural fields represented by proliferation of plant cells, and other fields of microorganisms, and cells of animals, plants, etc. The present invention relates to a method for controlling culture of a microorganism (including cells), which is useful for monitoring and controlling processes such as substance production by culture and cell growth.

【0002】[0002]

【従来の技術】近年、微生物、及び動物、植物などの細
胞を培養することによる各種の物質生産技術が開発さ
れ、実用化される中で、当該物質生産などのプロセス監
視及び制御を正確、かつ迅速に行うことが生産技術上き
わめて重要な地位を占めるに至っている。
2. Description of the Related Art In recent years, various substance production techniques by culturing cells of microorganisms, animals, plants and the like have been developed and put into practical use, and process monitoring and control of the substance production can be accurately and accurately performed. Prompt operation has become extremely important in production technology.

【0003】従来、このような微生物、及び動物、植物
などの細胞の培養による物質生産などのプロセス監視及
び制御等を行う方法は、種々開発されているものの、い
ずれの方法も、当該微生物等の培養工程において、培養
液の物質濃度等を逐次測定すると共に、当該培養液中の
物質濃度等の変化及び推移を監視しながら行うものがほ
とんどであり、一般に、例えば、培養工程の適宜の時機
において培養液を採取し、予め濾過処理、除蛋白処理、
希釈処理、有機溶媒による抽出処理等の適宜の前処理を
行ってから、液体クロマトグラフィー、ガスクロマトグ
ラフィー等の分析機器や酵素法などの分析方法で当該培
養液の基質濃度や代謝産物濃度等を測定し、その測定結
果に基づいて培養のプロセス監視及び制御等を行ってい
た。
Conventionally, various methods have been developed for performing process monitoring and control such as production of substances by culturing cells of such microorganisms and cells of animals, plants, etc., but any of these methods has been developed. In the culturing process, most of the things are performed while sequentially measuring the substance concentration and the like of the culture broth and monitoring changes and transitions of the substance concentration and the like in the culture broth, and generally, for example, at an appropriate timing of the culturing process. The culture broth is collected and filtered in advance, deproteinized,
After performing appropriate pretreatment such as dilution treatment and extraction treatment with an organic solvent, the substrate concentration and metabolite concentration etc. of the culture broth can be determined by an analytical method such as liquid chromatography, gas chromatography, etc. or an enzymatic method. The measurement was performed, and the culture process was monitored and controlled based on the measurement result.

【0004】しかしながら、このような方法は、前記の
如く、培養液を採取し、更に、予め、濾過処理、除蛋白
処理、希釈処理等の前処理を施すことが必要であり、更
に、各種分析機器で当該培養液中の特定の物質濃度等を
逐次測定することが必要とされるなど、かなりの労力と
時間のかかる方法であることから、物質生産、細胞増殖
などのプロセスの監視及び制御等を時宜を得て簡便、か
つ迅速に行うことが困難であるという問題点を有してお
り、従って、当業界においては、前記のような培養液中
の物質濃度等を測定し、培養のプロセス監視及び制御等
を実施する従来の方法に代わる新しい培養の管理技術を
開発することが強く要請されている状況にあった。
However, in such a method, as described above, it is necessary to collect the culture broth and further subject it to pretreatment such as filtration treatment, deproteinization treatment, and dilution treatment in advance. Since it is a method that requires a considerable amount of labor and time, for example, it is necessary to sequentially measure the concentration of a specific substance in the culture medium with an instrument, so monitoring and control of processes such as substance production and cell proliferation It has a problem that it is difficult to perform the procedure in a timely, convenient, and rapid manner. Therefore, in the art, the concentration of a substance in a culture solution as described above is measured, and the culturing process is performed. There has been a strong demand to develop a new culture management technique that replaces the conventional method of performing monitoring and control.

【0005】[0005]

【発明が解決しようとする課題】このような状況を踏ま
え、本発明者らは、前記の如き従来技術の問題点を確実
に解決し得ると共に、前記のような培養液中の物質濃度
等の指標に代わる新しい指標を採用し、正確で、簡便、
かつ迅速に培養のプロセスの監視及び制御等の培養の管
理を実施することが可能な全く新しい培養管理方法を開
発することを目標として鋭意研究を積み重ねた結果、培
養工程における培養液の浸透圧の値を指標とすることに
より所期の目的を達成し得ることを見い出し、本発明を
完成するに至った。
Based on such a situation, the present inventors can certainly solve the above-mentioned problems of the prior art, and at the same time, determine the concentration of substances in the culture solution as described above. Accurate, simple and easy to use
As a result of intensive research aimed at developing a completely new culture control method capable of rapidly and rapidly controlling culture control such as monitoring and control of the culture process, It was found that the intended purpose can be achieved by using the value as an index, and the present invention has been completed.

【0006】すなわち、本発明は、従来、微生物、及び
動物、植物などの細胞の培養の管理方法において必須の
手段として必要とされていた培養液の物質濃度等を測定
する手段を採用することなく、当該微生物等の培養によ
る物質生産、細胞増殖などのプロセスの監視及び制御を
正確、かつ迅速に実施することが可能な新しい培養管理
方法を提供することを目的とするものである。
That is, the present invention does not employ means for measuring the substance concentration of the culture solution, which has been required as an essential means in the conventional method for controlling the culture of microorganisms and cells of animals, plants and the like. Another object of the present invention is to provide a new culture management method capable of accurately and promptly carrying out monitoring and control of processes such as production of substances by culturing the microorganisms and cell proliferation.

【0007】また、本発明は、従来の培養管理方法で必
要とされていた培養液の物質濃度等を測定するために不
可欠の各種前処理操作を必要としない簡便な培養管理方
法を提供することを目的とするものである。
Further, the present invention provides a simple culture management method which does not require various pretreatment operations which are indispensable for measuring the concentration of a substance in a culture solution which is required in the conventional culture management method. The purpose is.

【0008】更に、本発明は、培養工程における培養液
の浸透圧を測定するだけで、正確で、簡便、かつ迅速に
培養による物質生産、細胞増殖などのプロセスの監視及
び制御等を行うことが可能な新しい培養管理方法を提供
することを目的とするものである。
Further, according to the present invention, by simply measuring the osmotic pressure of the culture solution in the culturing step, it is possible to accurately, easily and rapidly monitor and control the processes such as the production of substances by culturing and cell proliferation. It is intended to provide a possible new culture management method.

【0009】[0009]

【課題を解決するための手段】このような目的を達成す
る本発明は、以下の(1)〜(2)の技術的手段から構
成されるものである。 (1)微生物(細胞を含む)の培養の管理方法におい
て、培養工程における培養液の浸透圧の値を指標にし
て、培養を管理することを特徴とする微生物(細胞を含
む)の培養管理方法。
The present invention which achieves such an object comprises the following technical means (1) and (2). (1) In a method for controlling the culture of a microorganism (including cells), the method for controlling the culture of a microorganism (including cells) is characterized in that the culture is controlled by using an osmotic pressure value of a culture solution in the culture step as an index. .

【0010】(2)上記(1)記載の培養管理方法にお
いて、予め、培養工程における培養液の浸透圧の値と、
培養液の基質濃度、代謝産物濃度、または微生物(細胞
を含む)濃度の少なくとも1種の値との相関関係を求
め、これを指標にして、培養を管理することを特徴とす
る微生物(細胞を含む)の培養管理方法。微生物(細胞
を含む)の培養の管理方法において、培養液の浸透圧の
値を指標とすることを特徴とする微生物(細胞を含む)
の培養管理方法。
(2) In the culture management method described in (1) above, a value of the osmotic pressure of the culture solution in the culture step is previously set,
Correlation with at least one value of substrate concentration, metabolite concentration, or concentration of microorganisms (including cells) in the culture solution is obtained, and the correlation is used as an index to control the culture. Culture management method). Microorganisms (including cells) characterized by using an osmotic pressure value of a culture solution as an index in a method for controlling the culture of microorganisms (including cells)
Culture management method.

【0011】次に、本発明について更に詳細に説明す
る。本発明の微生物(細胞を含む)の培養管理方法は、
前記の如く、乳酸発酵、アルコール発酵、アミノ酸発酵
などに代表される食品分野、また、抗生物質発酵生産、
生理活性物質発酵生産などに代表される医薬品分野、動
物細胞、植物細胞の大量増殖等に代表される農業分野、
及びその他の分野における微生物、及び動物、植物など
の細胞の培養における物質生産、細胞増殖などのプロセ
スの監視及び制御などに適用されるものであり、その微
生物、細胞の種類、及び発酵方法、培養方法等の種類に
限定されることなく利用することが可能である。また、
本発明でいうところの微生物(細胞を含む)とは、微生
物、及び動物、植物などの細胞を意味するものであり、
その種類及び形態を問わず適宜の微生物、及び動物、植
物の細胞をも含むものとして定義されるものである。
Next, the present invention will be described in more detail. The culture management method of the microorganism (including cells) of the present invention comprises:
As mentioned above, lactic acid fermentation, alcohol fermentation, amino acid fermentation and other food fields, antibiotic fermentation production,
Pharmaceutical field typified by fermentative production of physiologically active substances, agricultural field typified by mass growth of animal cells and plant cells,
And microorganisms in other fields, and substance production in the culture of cells such as animals and plants, monitoring and control of processes such as cell growth, and the like, the microorganisms, cell types, fermentation methods, and culture. It is possible to use without being limited to the type of method. Also,
The term "microorganisms (including cells)" as used in the present invention means microorganisms and cells such as animals and plants,
Regardless of its type and morphology, it is defined as including appropriate microorganisms, cells of animals and plants.

【0012】更に、本発明でいうところの培養液とは、
前記微生物、及び動物、植物などの細胞を一定の液体培
地により培養し、物質生産、細胞増殖などを実施する培
養プロセスにおける当該微生物、及び細胞の培養液を意
味するものであり、いわゆる通常の培養液であれば如何
なるものであってもよく、その種類、組成等に限定され
るものではない。
Further, the culture medium as used in the present invention means
The microorganisms, cells of animals, plants and the like are cultured in a certain liquid medium to mean a culture solution of the microorganisms and cells in a culture process for carrying out substance production, cell proliferation, etc., so-called ordinary culture. Any liquid may be used, and the kind, composition, etc. are not limited.

【0013】次に、本発明においては、培養工程におけ
る培養液の浸透圧を測定することが必要とされるが、当
該浸透圧を測定する方法は、例えば、氷点降下法等を利
用した浸透圧計、望ましくは連続測定可能なオンライン
浸透圧計にて、培養タンク中の培養液の浸透圧を計測す
ればよく、その具体的方法は、適宜の手段でよく、特に
限定されるものではない。
Next, in the present invention, it is necessary to measure the osmotic pressure of the culture solution in the culturing step, and the method of measuring the osmotic pressure is, for example, an osmometer using a freezing point depression method or the like. Desirably, the osmotic pressure of the culture solution in the culture tank may be measured with an online osmometer capable of continuous measurement, and the specific method thereof may be any suitable means, and is not particularly limited.

【0014】本発明者らの研究したところによれば、こ
れまでの研究過程の中で、培養工程の適宜の段階におけ
る培養液の浸透圧の値は、従来の培養管理方法において
指標とされていた基質濃度、代謝産物濃度、又は微生物
(細胞を含む)濃度等のいわゆる培養液中の物質濃度と
一定の相関関係があること、そして当該浸透圧の値を培
養管理の指標として利用し得ることが新しい知見として
見い出され、その結果、微生物、及び細胞の培養におい
て、培養工程における培養液の浸透圧を測定することに
より、当該浸透圧の値を指標として、あるいは予め求め
た関係式により、当該浸透圧の値から基質濃度、代謝産
物濃度、あるいは細胞濃度を算出し、それを指標とし
て、培養の状態を監視することができることが明らかと
なった。
According to the research conducted by the present inventors, the osmotic pressure value of the culture solution at an appropriate stage of the culture process has been used as an index in the conventional culture control method in the research process so far. That there is a certain correlation with the so-called substance concentration in the culture medium such as substrate concentration, metabolite concentration, or microorganism (including cell) concentration, and that the osmotic pressure value can be used as an index for culture control Is found as a new finding, and as a result, in culturing microorganisms and cells, by measuring the osmotic pressure of the culture solution in the culturing step, the value of the osmotic pressure is used as an index, or by a previously determined relational expression, It was clarified that the substrate concentration, metabolite concentration, or cell concentration was calculated from the osmotic pressure value, and the condition of the culture could be monitored using the calculated concentration as an index.

【0015】即ち、浸透圧計、望ましくは連続測定可能
なオンライン浸透圧計にて、培養工程における培養液の
浸透圧を計測することにより、従来のような培養液中の
物質濃度等を直接測定する方法よりも簡便、かつ迅速に
培養液の状態を知ることができることが明らかとなっ
た。
That is, a conventional method for directly measuring the substance concentration in a culture solution by measuring the osmotic pressure of the culture solution in the culturing step using an osmometer, preferably an online osmometer capable of continuous measurement. It has become clear that the state of the culture solution can be known more simply and quickly.

【0016】この場合、例えば、上記関係式は、予め、
培養工程における培養液の浸透圧の測定値と、当該培養
液の基質濃度、代謝産物濃度、又は微生物、及び細胞濃
度の少なくとも1種の数値との相関関係を求めることに
より作成することが可能であり、これを指標として培養
の状態を監視することができる。更に、この場合、例え
ば、連続式培養設備における連続培養方法の希釈率、流
加培養方法による新鮮培地の流加速度の制御等の如く、
培養プロセスにおける任意の操作変数の制御に、上記浸
透圧の値あるいはそれから算出される他の状態変数を利
用することも適宜可能である。
In this case, for example, the above relational expression is
It can be created by determining the correlation between the measured value of the osmotic pressure of the culture solution in the culturing step and the numerical value of at least one of the substrate concentration, metabolite concentration, or microorganism and cell concentration of the culture solution. Yes, the condition of culture can be monitored using this as an index. Further, in this case, for example, the dilution rate of the continuous culture method in the continuous culture facility, the control of the flow acceleration of the fresh medium by the fed-batch culture method, etc.
It is also possible to appropriately use the above osmotic pressure value or other state variable calculated from it for controlling any manipulated variable in the culture process.

【0017】培養液の浸透圧の値と対比される当該培養
液中の物質濃度等の具体的内容は、使用する微生物、及
び細胞の種類、産生される物質の種類、培養液の種類、
培養条件、培養形態等によって個別的に設定すればよい
が、その好適な例を幾つか例示すると、例えば、本発明
者らの研究によれば、酵母のアルコール発酵によるエタ
ノール生産の培養プロセスにおける培養管理の場合、培
養液の浸透圧と当該培養液中の残存グルコース濃度、エ
タノール濃度、及び菌体濃度の関係に一定の相関関係が
あることが見い出され、従って、予め、当該各因子の間
の関係式を求めておけば、培養プロセスの適宜の時期に
おいて培養液の浸透圧を測定するだけで、当該浸透圧の
値を指標として、培養液の培養状態を正確で、簡便、か
つ迅速に培養の管理を行うことができることが判った。
The specific contents such as the substance concentration in the culture medium, which is compared with the osmotic pressure value of the culture medium, include the types of microorganisms and cells used, the types of substances produced, the types of culture medium,
Although it may be set individually depending on the culture conditions, the culture form, etc., some suitable examples thereof will be exemplified. In the case of management, it was found that there is a certain correlation in the relationship between the osmotic pressure of the culture solution and the residual glucose concentration, ethanol concentration, and microbial cell concentration in the culture solution. If the relational expression is obtained, the osmotic pressure of the culture solution can be measured at an appropriate time during the culture process, and the value of the osmotic pressure can be used as an index to accurately, simply, and rapidly culture the culture state of the culture solution. It was found that the management of

【0018】また、例えば、乳酸菌の乳酸発酵の培養プ
ロセスにおける培養管理の場合、本発明者らの研究によ
れば、培養液の浸透圧と、培養液の乳酸濃度、菌体増
殖、及び残存グルコース濃度との間には、一定の条件の
もとに、一定の比例関係があることが見い出され、従っ
て、予め、当該各因子の間の関係式を求めておけば、培
養プロセスの適宜の時期において培養液の浸透圧を測定
するだけで、当該浸透圧の値を指標として、培養液の培
養状態を正確で、簡便、かつ迅速に管理することができ
ることが判った。
Further, for example, in the case of controlling the culture in the lactic acid fermentation culture process of lactic acid bacteria, according to the study of the present inventors, the osmotic pressure of the culture solution, the lactic acid concentration of the culture solution, the bacterial growth, and the residual glucose It has been found that there is a constant proportional relationship with the concentration under certain conditions. Therefore, if the relational expression between the factors is obtained in advance, the appropriate timing of the culture process can be obtained. It was found that by simply measuring the osmotic pressure of the culture solution, the culturing state of the culture solution can be controlled accurately, simply and quickly by using the value of the osmotic pressure as an index.

【0019】また、例えば、連続式新鮮培地供給培養設
備におけるクロレラの流加培養方法による培養プロセス
における培養管理の場合、本発明者らの研究によれば、
培養液の浸透圧と、培養液中に残存するグルコース濃度
との間に高い相関性があることが見い出され、従って、
予め、両者の関係式を求めておけば、培養プロセスの適
宜の時期において培養液の浸透圧を測定するだけで、当
該浸透圧の値を指標として、培養液の培養状態を正確
で、簡便、かつ迅速に管理することができ、これによ
り、菌体増殖に同調させてグルコースを流加することが
可能となり、流加培養方式による培養状態の制御を簡
便、かつ迅速に行うことができることが判った。
Further, for example, in the case of culture management in the culture process by the fed-batch culture method of Chlorella in a continuous fresh medium supply culture facility, according to the studies of the present inventors,
It was found that there is a high correlation between the osmotic pressure of the culture and the glucose concentration remaining in the culture, and thus
In advance, if you obtain the relational expression of both, just by measuring the osmotic pressure of the culture solution at an appropriate time of the culture process, using the value of the osmotic pressure as an index, the culture state of the culture solution is accurate, simple, It can be quickly and rapidly managed, which allows glucose to be fed in synchronism with bacterial cell growth, and it has been found that the control of the culture state by the fed-batch culture method can be performed easily and quickly. It was

【0020】このように、本発明によれば、前記した如
く、それぞれ、酵母、乳酸菌、クロレラ等の微生物の培
養プロセスにおける当該微生物の培養管理を、当該培養
液中の浸透圧を測定するだけで、正確で、簡便、かつ迅
速に行うことができるが、かかる結果は、他の微生物、
動物細胞、植物細胞の場合においても同様に得られるこ
とが、本発明者らの総合的、かつ系統的な実験結果から
明らかとなっており、従って、本発明は、これらの微生
物に限らず、当該微生物の場合と同様に、他の微生物、
及び動物、植物等の細胞の場合にも、同様にして適用し
得るものである。
As described above, according to the present invention, as described above, the culture control of the microorganisms in the culture process of the microorganisms such as yeast, lactic acid bacterium, and chlorella can be performed by simply measuring the osmotic pressure in the culture solution. Accurate, convenient, and fast, but the result is that other microorganisms
It is clear from the comprehensive and systematic experimental results of the present inventors that the same can be obtained in the case of animal cells and plant cells. Therefore, the present invention is not limited to these microorganisms, As in the case of the microorganism, other microorganisms,
The same applies to cells such as animals and plants.

【0021】[0021]

【作用】本発明は、前記の如く、微生物(細胞を含む)
の培養の培養プロセスの適宜の時期において測定される
培養液の浸透圧の値は、従来の培養の管理方法の指標と
して使用されている基質濃度、代謝産物濃度、細胞濃度
等の物質濃度の値、更には、細胞の代謝、及び増殖速度
等の値、との間に、一定の条件において、一定の相関関
係を有するという事実を前提として開発されたものであ
り、本発明においては、培養工程における培養液の浸透
圧の値が培養管理の指標として用いられる。従って、本
発明によれば、培養プロセスにおける培養液の浸透圧の
値から、培養液中の基質濃度、代謝産物濃度、細胞濃
度、更に、細胞の代謝及び増殖速度、その他の培養状態
を、正確で、簡便、かつ迅速に監視することが可能であ
り、更には、それらの値に基づいて菌体増殖等に同調さ
せた培養温度の調整や培地の流加、連続培養における希
釈率の最適化の決定等の培養状態に応じた各種の操作変
数の制御等を簡便に実施することができる。
The present invention, as described above, is a microorganism (including cells).
The osmotic pressure value of the culture solution measured at an appropriate time in the culture process of the culture is the value of the substance concentration such as substrate concentration, metabolite concentration, cell concentration, etc. used as an index of the conventional culture control method. Further, it was developed on the premise that there is a certain correlation under certain conditions between the values such as cell metabolism and growth rate, and in the present invention, the culturing step The value of the osmotic pressure of the culture solution in is used as an index for culture control. Therefore, according to the present invention, the substrate concentration, the metabolite concentration, the cell concentration in the culture solution, the cell metabolism and growth rate, and other culture conditions can be accurately determined from the value of the osmotic pressure of the culture solution in the culture process. Therefore, it is possible to monitor easily and quickly. Furthermore, based on these values, the culture temperature is adjusted in synchronization with the bacterial growth, the feeding of the medium, and the optimization of the dilution rate in continuous culture. It is possible to easily carry out the control of various operational variables according to the culture state such as the determination of.

【0022】[0022]

【実施例】続いて、本発明の実施例を示して本発明を更
に具体的に説明するが、本発明は、当該実施例に限定さ
れるものではない。 実施例1 酵母サッカロマイセス・セレビシエによるエタノール発
酵の培養管理 培養液の浸透圧値から残存グルコース濃度、エタノール
濃度、菌体濃度(OD660)を求めて監視することを目的
に、微生物としてSaccharomyces cerevisiae IFD10217
を使用し、これを改変YM培地(酵母エキス0.3%、麦
芽エキス0.3%、ペプトン0.5%、グルコース4.
5%)で、30℃の条件下に、静置培養した。エタノー
ル及びグルコース濃度は、酵素法で測定し、また浸透圧
は、氷点降下法により測定し、273°Kに換算した。
その結果を図1に示す。図1から明らかなように、浸透
圧は、菌体増殖とエタノール濃度に対しては、正の比例
関係を示し、また残存グルコース濃度に対しては、見か
け上、負の比例関係があった。
EXAMPLES Next, the present invention will be described more specifically by showing examples of the present invention, but the present invention is not limited to the examples. Example 1 Culture management of ethanol fermentation by yeast Saccharomyces cerevisiae Saccharomyces cerevisiae IFD10217 as a microorganism for the purpose of obtaining and monitoring residual glucose concentration, ethanol concentration, and bacterial cell concentration (OD660) from the osmotic pressure value of the culture solution.
Using a modified YM medium (yeast extract 0.3%, malt extract 0.3%, peptone 0.5%, glucose 4.
5%) and static culture was carried out under the condition of 30 ° C. The ethanol and glucose concentrations were measured by an enzymatic method, and the osmotic pressure was measured by a freezing point depression method, and converted to 273 ° K.
The result is shown in FIG. As is clear from FIG. 1, the osmotic pressure had a positive proportional relationship with the bacterial cell growth and the ethanol concentration, and had an apparent negative proportional relationship with the residual glucose concentration.

【0023】グルコース以外の栄養源の消費、及びエタ
ノール以外の代謝産物による浸透圧変化は、グルコース
やエタノールの影響に比べると小さく、またグルコース
あるいはエタノールとパラレルに経時変化することが判
ったので、各々の検討は行わなかった。浸透圧と、残存
グルコース濃度、エタノール濃度、及び菌体濃度の関係
を第2図に示す。残存グルコース濃度(g/l)をGr、エ
タノール濃度(g/l)をE、菌体濃度(OD660) をX、また
浸透圧(0sm/kg)をπとすると、培養中に変化する0.3
0〜0.53 0sm/kg の浸透圧の範囲において、最小二
乗法により以下の(1)〜(3)の関係式を得た。
The consumption of nutrients other than glucose and the change in osmotic pressure due to metabolites other than ethanol were smaller than the effects of glucose and ethanol, and it was found that they change with glucose or ethanol in parallel with time. Was not examined. The relationship between osmotic pressure, residual glucose concentration, ethanol concentration, and bacterial cell concentration is shown in FIG. When the residual glucose concentration (g / l) is Gr, the ethanol concentration (g / l) is E, the cell concentration (OD660) is X, and the osmotic pressure (0sm / kg) is π, it changes during culture. Three
In the osmotic pressure range of 0 to 0.530 sm / kg, the following relational expressions (1) to (3) were obtained by the method of least squares.

【0024】 Gr=-185.9 × π + 102.0 (r=-0.996) (1) E = 105.2 × π - 31.3 (r=0.972) (2) X = 24.4 × π - 7.4 (r=0.982) (3)Gr = -185.9 × π + 102.0 (r = -0.996) (1) E = 105.2 × π-31.3 (r = 0.972) (2) X = 24.4 × π-7.4 (r = 0.982) (3)

【0025】この場合は、培養液の浸透圧の経時変化
は、残存グルコース濃度、アルコールの濃度、及び菌体
濃度のいずれとも高い相関関係を示し、培養中の培養液
の浸透圧を測定することで、培養工程の状態が把握でき
ることが判った。従って、酵母によるエタノール発酵の
培養工程における培養液の浸透圧を測定することによ
り、目的とする基質濃度、代謝産物濃度及び細胞濃度の
経時変化を監視できることが明らかとなった。
In this case, the change with time of the osmotic pressure of the culture medium shows a high correlation with all of the residual glucose concentration, the alcohol concentration and the bacterial cell concentration, and the osmotic pressure of the culture medium during the culture should be measured. It was found that the state of the culture process can be grasped. Therefore, it was clarified that by measuring the osmotic pressure of the culture solution in the ethanol fermentation culture process using yeast, it is possible to monitor changes over time in the target substrate concentration, metabolite concentration, and cell concentration.

【0026】実施例2 乳酸菌ラクトバチルス・カゼイによる乳酸発酵の培養管
理 pHの影響を受ける酸の解離率も考慮し、乳酸菌の培養
中の浸透圧による培養監視を検討した。Rogosa培地(J.
Inf. Dis., 110, 258-267, 1962)で、Lactobacillus ca
sei を37℃の条件下で静置培養した。グルコース濃度、
乳酸濃度、菌体濃度(OD660) 、浸透圧、pHの培養経時
変化を図3に示した。浸透圧は、273°Kに換算して
示した。図3から明らかなように、浸透圧は、菌体増殖
と乳酸濃度に対しては正の比例関係を示し、また残存グ
ルコース濃度に対しては、見かけ上、負の比例関係があ
った。
Example 2 Culture Management of Lactic Acid Fermentation by Lactobacillus Lactobacillus casei Considering the dissociation rate of acid affected by pH, the culture monitoring by osmotic pressure during the culture of lactic acid bacteria was examined. Rogosa medium (J.
Inf. Dis., 110, 258-267, 1962) in Lactobacillus ca.
The sei was statically cultured at 37 ° C. Glucose concentration,
The time-dependent changes in the lactic acid concentration, bacterial cell concentration (OD660), osmotic pressure, and pH are shown in FIG. The osmotic pressure was converted and shown at 273 ° K. As is clear from FIG. 3, the osmotic pressure showed a positive proportional relationship with the bacterial cell growth and the lactic acid concentration, and had an apparent negative proportional relationship with the residual glucose concentration.

【0027】浸透圧をπatm (atm) 、溶質の質量モル濃
度をC(mole/kg) 、溶液と純溶媒の熱平衡時の絶対温度
をT(°K)、気体定数(0.082 kg・atm・°K-1・mol
e-1)をRとすると、濃度Cがあまり大きくならない範囲
では、以下の(4)のVan'tHoffの式 πatm =RTC (4) が成り立つ。
The osmotic pressure is π atm (atm), the molar concentration of solute is C (mole / kg), the absolute temperature at the thermal equilibrium of the solution and the pure solvent is T (° K), and the gas constant (0.082 kg.atm. ° K -1 · mol
If e −1 ) is R, the following equation (4) of Van't Hoff π atm = RTC (4) is established in a range in which the concentration C does not become too large.

【0028】従って、浸透圧と温度を測定することによ
り、上記(4)式より、溶質の濃度を算出することがで
きる。ホモ乳酸菌培養において浸透圧変化に関与する主
因子としては、グルコースを主とする栄養源の減少と逆
に増加して行く乳酸がある。更に、乳酸は、培養経時的
に低下する培養液のpHの影響により解離率が小さくな
る。従って、上記実施例1のように、実験値に基づく最
小二乗法による近似式で、各状態変数を浸透圧から算出
することも可能だが、解離率を考慮した理論式を用いた
方がより正確となる。
Therefore, by measuring the osmotic pressure and the temperature, the solute concentration can be calculated from the above equation (4). The main factor involved in osmotic pressure change in homolactic acid bacterium culture is lactic acid which increases contrary to the decrease of glucose-based nutrient source. Furthermore, lactic acid has a small dissociation rate due to the influence of the pH of the culture solution, which decreases over time with the culture. Therefore, although it is possible to calculate each state variable from the osmotic pressure by an approximate expression based on the least squares method based on the experimental value as in Example 1, it is more accurate to use the theoretical expression considering the dissociation rate. Becomes

【0029】そこで、電解質の解離率が50%のときの
pHをpKaとすると、以下の(5)のHenderson-Hass
elbalchの式 pH=pKa + log〔解離濃度〕/〔非解離濃度〕 (5) を変形することにより、解離率(%)は、以下の(6)の式、 解離率={10[pH-pKa]/(10[pH-pKa]+1)}× 100 (6) として求めることができる。
Therefore, assuming that the pH when the dissociation rate of the electrolyte is 50% is pKa, the following (5) Henderson-Hass
Elbalch's formula pH = pKa + log [Dissociation concentration] / [Non-dissociation concentration] (5) is modified to obtain the dissociation rate (%) by the following equation (6) : Dissociation rate = {10 [pH- It can be calculated as pKa] / (10 [pH-pKa] +1)} × 100 (6).

【0030】浸透圧変化に影響を与えるグルコース以外
の窒素源や微量成分等の栄養源の経時変化を各々に測定
することは不可能であり、行っていない。しかしなが
ら、これらは、菌体濃度と比例関係にあり、菌体濃度と
ある定数kとの積として表せる。以上のことから、浸透
圧(0sm/kg)をπ、培養開始時の浸透圧(0sm/kg)をπi
消費グルコース濃度(g/l)をG、菌体濃度(OD660) を
X、生成乳酸濃度(g/l)をLとすると、浸透圧値は、
(6)式により以下の式で得られる。 π=−G/180 + k ・ X + L/90・{10[pH-pKa]/(10[pH-pKa]+1)+1}+ πi (7)
It is impossible or not possible to measure the changes with time of nitrogen sources other than glucose and nutrient sources such as trace components that affect changes in osmotic pressure. However, these are proportional to the bacterial cell concentration and can be expressed as the product of the bacterial cell concentration and a constant k. From the above, osmotic pressure (0sm / kg) is π, osmotic pressure at the start of culture (0sm / kg) is π i ,
When the glucose concentration (g / l) consumed is G, the bacterial cell concentration (OD660) is X, and the produced lactic acid concentration (g / l) is L, the osmotic pressure value is
From the equation (6), the following equation is obtained. π = -G / 180 + k ・ X + L / 90 ・ {10 [pH-pKa] / (10 [pH-pKa] +1) +1} + π i (7)

【0031】乳酸のpKaは3.86、また浸透圧の実
測値と計算値が一致するような定数kを求めると、−
0.0057が得られ、これらを上式に代入すると、 π=-G/180−0.0057・X+L/90・{10[pH-3.86]/(10[pH-3.86]+1)+1}+πi (8) が得られた。
The pKa of lactic acid is 3.86, and when a constant k is obtained such that the actually measured value and the calculated value of the osmotic pressure are the same, −
0.0057 is obtained, and by substituting these into the above equation, π = -G / 180-0.0057 ・ X + L / 90 ・ {10 [pH-3.86] / (10 [pH-3.86] +1) +1 } + Π i (8) was obtained.

【0032】消費グルコースに対する乳酸収率L/G
(g−乳酸/g−グルコース)及び菌体収率X/G(OD
660/g-グルコース)は、実験値より、それぞれ、 L/G=0.85 (9) X/G=0.51 (10) であるから、上記(8)〜(10)の式の連立方程式
を、消費グルコース濃度、乳酸濃度、菌体濃度について
解くと、浸透圧とpHをパラメータとする以下の(1
1)〜(13)の関係式が得られた。
Lactic acid yield L / G based on glucose consumed
(G-lactic acid / g-glucose) and cell yield X / G (OD
660 / g-glucose) is L / G = 0.85 (9) X / G = 0.51 (10) from the experimental values, so simultaneous equations (8) to (10) Solving the equation for glucose concentration, lactate concentration, and bacterial cell concentration, the following (1) with osmotic pressure and pH as parameters
The relational expressions 1) to (13) were obtained.

【0033】 G=(π-πi )/[0.0094・{10[pH-3.86]/(10[pH-3.86]+1)+1}-0.0085] (11) L=(π-πi )/[0.0111・{10[pH-3.86]/(10[pH-3.86]+1)+1}-0.0099] (12) X=(π-πi )/[0.0185・{10[pH-3.86]/(10[pH-3.86]+1)+1}-0.0160] (13)G = (π-π i ) / [0.0094 · {10 [pH-3.86] / (10 [pH-3.86] +1) +1} -0.0085] (11) L = (π-π i ) /[0.0111 ・ {10 [pH-3.86] / (10 [pH-3.86] +1) +1} -0.0099] (12) X = (π-π i ) / [0.0185 ・ {10 [pH-3.86] / (10 [pH-3.86] +1) +1} -0.0160] (13)

【0034】π1 =365mOsm/kg の条件で、この式よ
り算出される各状態変数数値を実線で、実測値をドット
で図4にプロットした。計算値と実測値とはよく一致し
ており、浸透圧とpHを測定することにより、目的とす
る基質濃度、代謝産物濃度、細胞濃度の経時変化を監視
できることが明らかとなった。即ち、この場合は、培養
液の浸透圧の経時変化は、残存グルコース濃度、乳酸濃
度、及び菌体濃度のいずれとも正又は負の高い相関関係
を示し、乳酸菌による乳酸菌発酵の培養中の培養液の浸
透圧を測定することで、培養工程の状態が把握できるこ
とが判った。
Under the condition of π 1 = 365 mOsm / kg, the numerical values of each state variable calculated by this formula are plotted in solid lines and the measured values are plotted in dots in FIG. The calculated value and the measured value are in good agreement, and it was revealed that by measuring the osmotic pressure and the pH, it is possible to monitor the changes over time in the target substrate concentration, metabolite concentration, and cell concentration. That is, in this case, the change with time of the osmotic pressure of the culture medium shows a high positive or negative correlation with any of the residual glucose concentration, the lactic acid concentration, and the bacterial cell concentration, and the culture liquid during the culture of lactic acid bacterium fermentation by lactic acid bacteria. It was found that the state of the culturing process can be grasped by measuring the osmotic pressure of.

【0035】Rogosa培地の代わりにミルクを用いた培養
において、菌体量としてOD660 の代わりに生菌数を測定
したところ同様な結果が得られ、発酵乳製造プロセスの
監視にも活用できた。
In the culture using milk instead of the Rogosa medium, the same result was obtained when the viable cell count was measured instead of OD660 as the cell amount, and it was also useful for monitoring the fermented milk production process.

【0036】実施例3 クロレラ、クロレラ・レギュラリスの流加培養工程にお
ける培養管理 発酵槽によるクロレラの暗培養において、基質であるグ
ルコースによる増殖阻害を受けるので、培養液の浸透圧
値から基質量を制御する流加培養を検討した。Chlorell
a regularis をグルコースと尿素を主成分とする培地に
て、35℃の条件下で、通気攪拌培養を行った(Agr. Bio
l. Chem., 38, 1, 9-18, 1974)。上述の実施例1と同様
に、グルコースと連動して変化する他の基質等も含め
て、グルコースを代表状態変数として、クロレラ培養時
のグルコース濃度Gr(g/l)と273 °Kに換算したときの
浸透圧π(0sm/kg)の関係を検討した。その結果、高い
相関性(図5)があることを見出し、最小二乗法により
以下の関係式を得た。 Gr = 101.6 × π − 4.8 (r=0.995) (14)
Example 3 Culture Management in Fed-Batch Culture Process of Chlorella and Chlorella regularis In dark culture of Chlorella in a fermenter, growth inhibition by glucose as a substrate is observed, and therefore the substrate mass is controlled from the osmotic pressure value of the culture solution. Fed-batch culture was investigated. Chlorell
a regularis was subjected to aeration and agitation culture in a medium containing glucose and urea as main components at 35 ° C (Agr. Bio
l. Chem., 38, 1, 9-18, 1974). In the same manner as in Example 1 described above, glucose was also converted into glucose concentration Gr (g / l) and 273 ° K during chlorella culture using glucose as a representative state variable, including other substrates that change in association with glucose. The relationship between the osmotic pressure π (0 sm / kg) was examined. As a result, it was found that there is a high correlation (FIG. 5), and the following relational expression was obtained by the least squares method. Gr = 101.6 × π − 4.8 (r = 0.995) (14)

【0037】この関係式を利用し、培養液中に残存する
グルコースの濃度を浸透圧値から算出し、グルコース濃
度を3%以下に制御する流加培養を検討した。グルコー
スが枯渇する直前の5g/l のときの浸透圧は88m0sm/kg
、30g/l の時は338m0sm/kgであるので、培養の制御液
として、浸透圧88m0sm/kg になった時点でグルコースを
含む流加培地の添加を始め、338m0sm/kgになるまで添加
を続け、ふたたび浸透圧88m0sm/kg になったところで培
地の流加を行った。この方法を繰り返して培養を続けた
結果を図6に示した。
Using this relational expression, the concentration of glucose remaining in the culture broth was calculated from the osmotic pressure value, and fed-batch culture in which the glucose concentration was controlled to 3% or less was examined. Immediately before glucose depletion, the osmotic pressure at 5g / l is 88m0sm / kg.
Since it is 338m0sm / kg at 30g / l, start the addition of the feed medium containing glucose at the time when the osmotic pressure reached 88m0sm / kg as the culture control solution, and continue to add it until 338m0sm / kg. The medium was fed again when the osmotic pressure reached 88 m0sm / kg again. The result of continuing the culture by repeating this method is shown in FIG.

【0038】クロレラ濃度は、パックドセルボリューム
(PCV ml/l)で表した。浸透圧値に基づく培養系内
でのグルコース濃度の計算値と実測値はよく一致し、グ
ルコースは、枯渇することなく3%以下に制御され、菌
体増殖に同調させて指数的に流加できた。浸透圧値に基
づく流加培養制御は、簡便、かつ迅速で優れた方法であ
ることが判った。
The chlorella concentration was expressed by packed cell volume (PCV ml / l). The calculated value and the measured value of glucose concentration in the culture system based on the osmotic pressure value are in good agreement, and the glucose is controlled to 3% or less without depletion, and can be fed exponentially in synchronization with cell growth. It was Fed-batch culture control based on osmotic pressure was found to be a simple, rapid and excellent method.

【0039】クロレラの場合は、基質としてのグルコー
スが培養工程中に消費されるが、培養初期に添加できる
グルコース濃度は制限があるので、培養途中で適宜追加
する必要がある。また、浸透圧とグルコース濃度に高い
相関があることが判ったので、クロレラの培養管理を、
浸透圧の測定で行うことができることが判った。
In the case of chlorella, glucose as a substrate is consumed during the culturing process, but the glucose concentration that can be added at the initial stage of culturing is limited, so it is necessary to add it appropriately during culturing. In addition, since it was found that there is a high correlation between osmotic pressure and glucose concentration, the culture management of chlorella should be
It has been found that this can be done by measuring the osmotic pressure.

【0040】[0040]

【発明の効果】以上詳述したように、本発明は、微生物
(細胞を含む)の培養の管理方法において、培養工程に
おける培養液の浸透圧の値を指標とすることを特徴とす
る微生物(細胞を含む)の培養管理方法に関するもので
あり、本発明によれば、微生物(細胞を含む)の培養に
よる物質生産、細胞増殖などのプロセスにおける培養状
態の監視及び制御等を簡便、かつ迅速に行うことができ
る。
INDUSTRIAL APPLICABILITY As described above in detail, the present invention relates to a method for controlling the culture of microorganisms (including cells), wherein the osmotic pressure value of the culture solution in the culture step is used as an index. The present invention relates to a method for managing culture of cells (including cells), and according to the present invention, it is possible to easily and quickly monitor and control the culture state in processes such as substance production by culturing microorganisms (including cells) and cell proliferation. It can be carried out.

【0041】また、本発明によれば、予め、培養工程に
おける培養液の浸透圧の値と、培養液の基質濃度、代謝
産物濃度、又は微生物(細胞を含む)濃度の少なくとも
1種の値との相関関係を求め、これを指標にして、微生
物(細胞を含む)の培養のプロセス監視、及び制御等を
正確で、簡便、かつ迅速に管理することができる。
Further, according to the present invention, the osmotic pressure value of the culture solution in the culturing step and the value of at least one of the substrate concentration, the metabolite concentration or the microorganism (including cells) concentration of the culture solution are previously set. It is possible to accurately, easily and swiftly control the process monitoring and control of the culture of the microorganism (including cells) by obtaining the correlation of the above.

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

【図1】酵母の培養プロセスにおける各状態変数の経時
変化を示す。
FIG. 1 shows the time course of each state variable in the yeast culture process.

【図2】酵母の培養プロセスにおける浸透圧と各状態変
数の関係を示す。
FIG. 2 shows the relationship between osmotic pressure and each state variable in the yeast culture process.

【図3】乳酸菌の培養プロセスにおける各状態変数の経
時変化を示す。
FIG. 3 shows changes with time of each state variable in the lactic acid bacterium culture process.

【図4】各状態変数の計算値と実測値の経時変化を示
す。
FIG. 4 shows changes with time in calculated values and measured values of each state variable.

【図5】クロレラの培養プロセスにおける浸透圧とグル
コース濃度との関係を示す。
FIG. 5 shows the relationship between osmotic pressure and glucose concentration in the chlorella culture process.

【図6】浸透圧値から算出したグルコース濃度を指標と
した流加培養における各状態変数の経時変化を示す。
FIG. 6 shows changes with time of each state variable in fed-batch culture using glucose concentration calculated from osmotic pressure as an index.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 微生物(細胞を含む)の培養の管理方法
において、培養工程における培養液の浸透圧の値を指標
にして、培養を管理することを特徴とする微生物(細胞
を含む)の培養管理方法。
1. A method for controlling the culture of microorganisms (including cells), wherein the culture is controlled using the osmotic pressure value of the culture solution in the culture step as an index. Management method.
【請求項2】 上記請求項1記載の培養管理方法におい
て、予め、培養工程における培養液の浸透圧の値と、培
養液の基質濃度、代謝産物濃度、または微生物(細胞を
含む)濃度の少なくとも1種の値との相関関係を求め、
これを指標にして、培養を管理することを特徴とする微
生物(細胞を含む)の培養管理方法。
2. The culture management method according to claim 1, wherein at least the osmotic pressure value of the culture solution in the culturing step and the substrate concentration, metabolite concentration, or microorganism (including cells) concentration of the culture solution are previously set. Find the correlation with one value,
A method for controlling the culture of microorganisms (including cells), characterized by controlling the culture using this as an index.
JP5346562A 1993-12-22 1993-12-22 Culture management method Pending JPH07177876A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5346562A JPH07177876A (en) 1993-12-22 1993-12-22 Culture management method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5346562A JPH07177876A (en) 1993-12-22 1993-12-22 Culture management method

Publications (1)

Publication Number Publication Date
JPH07177876A true JPH07177876A (en) 1995-07-18

Family

ID=18384269

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Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JPH07177876A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003080814A1 (en) * 2002-03-26 2003-10-02 New Century Fermentation Research, Ltd. Method of continuous culture of anaerobic bacterium
WO2007032265A1 (en) * 2005-09-15 2007-03-22 New Century Fermentation Research Ltd. Continuous culture apparatus for alcohol producing bacterium and method of culturing the bacterium
WO2019044837A1 (en) * 2017-08-29 2019-03-07 三菱瓦斯化学株式会社 Method for manufacturing polyester
CN117413773A (en) * 2023-10-26 2024-01-19 南京晓庄学院 Plant tissue culture osmotic pressure difference compensation control system and its implementation method
CN121011258A (en) * 2025-10-27 2025-11-25 湖北希普生物科技有限公司 A method and system for controlling feed fermentation parameters

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003080814A1 (en) * 2002-03-26 2003-10-02 New Century Fermentation Research, Ltd. Method of continuous culture of anaerobic bacterium
CN100434509C (en) * 2002-03-26 2008-11-19 有限会社新世纪发酵研究所 Continuous culture method of anaerobe
WO2007032265A1 (en) * 2005-09-15 2007-03-22 New Century Fermentation Research Ltd. Continuous culture apparatus for alcohol producing bacterium and method of culturing the bacterium
WO2019044837A1 (en) * 2017-08-29 2019-03-07 三菱瓦斯化学株式会社 Method for manufacturing polyester
US11279957B2 (en) 2017-08-29 2022-03-22 Mitsubishi Gas Chemical Company, Inc. Method for producing polyester
CN117413773A (en) * 2023-10-26 2024-01-19 南京晓庄学院 Plant tissue culture osmotic pressure difference compensation control system and its implementation method
CN121011258A (en) * 2025-10-27 2025-11-25 湖北希普生物科技有限公司 A method and system for controlling feed fermentation parameters

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