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JPS6018392B2 - High-yield culture method for microorganisms - Google Patents
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JPS6018392B2 - High-yield culture method for microorganisms - Google Patents

High-yield culture method for microorganisms

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Publication number
JPS6018392B2
JPS6018392B2 JP56194517A JP19451781A JPS6018392B2 JP S6018392 B2 JPS6018392 B2 JP S6018392B2 JP 56194517 A JP56194517 A JP 56194517A JP 19451781 A JP19451781 A JP 19451781A JP S6018392 B2 JPS6018392 B2 JP S6018392B2
Authority
JP
Japan
Prior art keywords
microorganisms
amount
culture
added
adjuster
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
Application number
JP56194517A
Other languages
Japanese (ja)
Other versions
JPS5898085A (en
Inventor
伸生 松下
正治 西海
正勝 藤本
範夫 清水
正雄 上野
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP56194517A priority Critical patent/JPS6018392B2/en
Publication of JPS5898085A publication Critical patent/JPS5898085A/en
Publication of JPS6018392B2 publication Critical patent/JPS6018392B2/en
Expired legal-status Critical Current

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  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Description

【発明の詳細な説明】 本発明は、微生物の高収率培養法に係り、特に、増殖に
伴なし、酸あるいはアルカリ性物質を代謝する微生物を
高収率培養するのに好適な微生物の高収率培養法に関す
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a high-yield cultivation method for microorganisms, and in particular, to a high-yield cultivation method for microorganisms suitable for high-yield cultivation of microorganisms that metabolize acid or alkaline substances as they grow. Regarding rate culture method.

従来、微生物の培養法としては、炭素源となる基質の全
量を培養開始前に供給する方法又は培養途中においても
炭素源となる基質を粥給する方法が慣用されている。
Conventionally, methods for culturing microorganisms include a method in which the entire amount of a substrate serving as a carbon source is fed before the start of culture, or a method in which a substrate serving as a carbon source is fed in gruel even during the cultivation.

しかし、前者の微生物の培養法では、培養開始時に大量
の炭素源が存在するため、炭素源により微生物の増殖が
阻害されるという問題があり、又、後者の微生物の培養
法では、炭素源の濃度を一定に保つことができるので長
期間安定した培養を維持できるが、微生物による炭素源
の消費速度の変化が大きいため、炭素源である基質の供
給方法によって次のような問題点があった。
However, in the former method of culturing microorganisms, there is a problem that the growth of microorganisms is inhibited by the presence of a large amount of carbon source at the start of the culture, and in the latter method, the growth of microorganisms is inhibited by the carbon source. Since the concentration can be kept constant, stable culture can be maintained for a long period of time, but because the consumption rate of the carbon source by microorganisms changes greatly, the following problems arise depending on the method of supplying the substrate, which is the carbon source. .

【11 予め設定された一定量の基質を逐次又は連続的
に供給する方法では、微生物による炭素源の消費速度の
変化に基質の供給量が追随できない場合、炭素源に過不
足が生じ微生物の増殖が阻害される。
[11] In the method of sequentially or continuously supplying a predetermined amount of substrate, if the amount of substrate supplied cannot keep up with changes in the rate of consumption of carbon sources by microorganisms, an excess or deficiency of carbon sources may occur, resulting in the proliferation of microorganisms. is inhibited.

■ 炭素源が有機酸である場合は、培地のPHを指礎に
して炭素源である基質を供孫舎する方法があるが、この
場合は、微生物による有機酸の消費に伴い培地の解が上
昇することが必要であり、炭素源が限定される。
■ When the carbon source is an organic acid, there is a method of subtracting the carbon source substrate based on the pH of the culture medium. carbon sources are limited.

‘3} 炭素源が中性である場合は、溶存酸素濃度を指
標にして炭素源である基質を供給する方法があるが、現
状の溶存酸素濃度計には、ドリフト、感度低下等の問題
があり、正確な溶存酸素濃度値が得られないため、基質
供孫合を精密に缶。
'3} If the carbon source is neutral, there is a method of supplying the carbon source substrate using the dissolved oxygen concentration as an indicator, but current dissolved oxygen concentration meters have problems such as drift and reduced sensitivity. However, since accurate dissolved oxygen concentration values cannot be obtained, the substrate donor mixture must be prepared precisely.

御することができない。本発明は、上記諸問題の解決を
目的としたもので、pH調整剤の添加量を測定し、該添
加量に基づいて炭素源である基質の供給速度を制御する
ことを特徴とし、微生物の高収率を達成することができ
る微生物の高収率培養法を提供するものである。
I can't control it. The present invention is aimed at solving the above-mentioned problems, and is characterized by measuring the amount of a pH adjuster added and controlling the supply rate of a substrate, which is a carbon source, based on the amount added. The present invention provides a high-yield culture method for microorganisms that can achieve high yields.

本発明の−実施例を図面により説明する。Embodiments of the present invention will be described with reference to the drawings.

図面は、本発明を実施した微生物の高収率培養装置の系
統図で、培養槽10には、溶存酸素濃度調節装置、例え
ば、回転数可変装直が設けられた駆動装置11で回転駆
動する機梓翼12が回転可能に内設され、その上部には
、例えば、アルカリあるいは酸の貯蔵タンクに電磁弁、
調節弁を設けたpH調節装置13と、基質供給速度調節
装置、例えば、流量可変ポンプ14と、圧力調節装置、
例えば、排気流量調節弁15と、圧力測定装置、例えば
、圧力計16とがそれぞれ設置され、その中間部には、
pH測定装置、例えば、pH電極17と、温度測定装置
、例えば、側温抵抗体18と、溶存酸素濃度測定装置、
例えば、溶存酸素濃度計19とがそれぞれ設置され、そ
の下部には、通気用導管20が連結されている。
The drawing is a system diagram of a high-yield culturing device for microorganisms according to the present invention, in which a culture tank 10 is rotatably driven by a drive device 11 equipped with a dissolved oxygen concentration adjusting device, for example, a variable rotation speed device. A mechanical wing 12 is rotatably disposed inside the wing 12, and a solenoid valve, for example, for an alkali or acid storage tank is installed on the upper part of the wing 12.
A pH adjustment device 13 provided with a control valve, a substrate supply rate adjustment device such as a variable flow rate pump 14, a pressure adjustment device,
For example, an exhaust flow rate control valve 15 and a pressure measuring device, such as a pressure gauge 16, are installed, and in the middle thereof,
A pH measuring device, for example, a pH electrode 17, a temperature measuring device, for example, a side temperature resistor 18, a dissolved oxygen concentration measuring device,
For example, a dissolved oxygen concentration meter 19 is installed, and a ventilation conduit 20 is connected to the lower part thereof.

又、培養槽10に周設されたジャケット21には、温度
調節装置、例えば、冷却水流量調節弁22が設けられて
いる。圧力計16と、pH電極17と、側温抵抗体18
と、溶存酸素濃度計19とは、アナログ/デジタル変換
装置、例えば、マルチプレクサ付で多点処理可能なA/
D変換器23にそれぞれ接続され、又、駆動装置1 1
と、pH調節装魔13と、流量可変ポンプ14と、排気
流量調節弁15と、冷却水流量調節弁22とは、A/D
変換器23と接続された演算・制御・記憶・入出力装置
、例えば、キーボード付のミニコン24にそれぞれ接続
されている。培養槽10に培地25を張込み例えば、微
生物が好気性である場合は、通気用導管20より通気し
培養が開始される。
Further, a jacket 21 surrounding the culture tank 10 is provided with a temperature control device, for example, a cooling water flow control valve 22. Pressure gauge 16, pH electrode 17, side temperature resistor 18
The dissolved oxygen concentration meter 19 is an analog/digital converter, for example, an A/D converter equipped with a multiplexer and capable of multi-point processing.
are respectively connected to the D converter 23, and the drive devices 1 1
, the pH adjustment device 13, the variable flow rate pump 14, the exhaust flow rate control valve 15, and the cooling water flow rate control valve 22.
The converter 23 is connected to an arithmetic/control/storage/input/output device, for example, a minicomputer 24 with a keyboard. A culture medium 25 is filled in the culture tank 10 and, for example, if the microorganism is aerobic, the culture is started by aeration through the aeration conduit 20.

培養中は、pH電極17、汝山温抵抗体18、溶存酸素
濃度計19及び圧力計16により、培地25のpH、温
度、溶存酸素濃度及び培養槽10の圧力を測定し、これ
らの測定値をA/D変換器23でそれぞれディジタル値
に変換した後に、ミニコン24に入力され、ここで、別
に入力されている各設定値と比較演算され、その結果に
よりミニコン24から制御出力信号を、pH調節装置1
3と、冷却水流量調節弁22と、駆動装置11と、排気
流量調節弁15とにそれぞれ出力することにより、培地
25のpH、温度、溶存酸素濃度及び培養槽10の圧力
の環境条件は、微生物の増殖に好ましい条件に制御され
る。このように、培養中の培地25のpHは、常時設定
値になるように制御されるが、この時、pHの変化速度
は、培地25のpHを設定値に制御するに要したpH調
節装置13から培地25へのpH調節剤の添加量に比例
する。
During culturing, the pH, temperature, and dissolved oxygen concentration of the culture medium 25 and the pressure of the culture tank 10 are measured using the pH electrode 17, the Yosan thermoresistor 18, the dissolved oxygen concentration meter 19, and the pressure gauge 16, and these measured values are measured. After each is converted into a digital value by the A/D converter 23, it is input to the mini-computer 24, where it is compared with each set value that has been input separately, and based on the result, the mini-computer 24 outputs a control output signal to the pH value. Adjustment device 1
3, the cooling water flow rate control valve 22, the drive device 11, and the exhaust flow rate control valve 15, the environmental conditions of the pH of the culture medium 25, temperature, dissolved oxygen concentration, and pressure of the culture tank 10 are Conditions are controlled to favor the growth of microorganisms. In this way, the pH of the medium 25 during cultivation is always controlled to the set value, but at this time, the rate of change of pH is determined by the pH adjustment device required to control the pH of the medium 25 to the set value. 13 to the amount of pH adjuster added to the medium 25.

従って、FH調節剤の添加量を、例えば、pH調節装置
13の電磁弁の1回の関弁で添加されるpH調整剤を一
定量とし、その添加頻度を一定期間積算した添加回数に
pH調節装置13の電磁弁の1回の開弁で添加されるp
H調整剤の一定量を乗ずることにより測定し、この測定
されたpH調整剤の添加量をもとに演算式‘1によりミ
ニコン24で演算してミニコン24から流量可変ポンプ
14に制御出力信号を出力することにより塔地25には
、適正な供給速度にて基質が供給される。F=C・N・
q ………‘1}ここで・、 F:基質供給速度 C:菌種によって定まる定数 N:pH調整剤の添加頻度を一定期間積算した添加回数
q:pH調節装置の電磁弁の1回の開弁で添加されるp
H調整剤の一定量このような、微生物の高収率培養法で
は、培養中の培地のpHが常時設定値になるように制御
される際のpHの変化速度と比例関係にある培地のpH
を設定値とするに要したpH調整剤の添加量により、培
地への基質供給速度を制御することで、培養中の炭素源
の過不足を防止することができる。
Therefore, the amount of FH adjuster added is, for example, a fixed amount of pH adjuster added by one solenoid valve of the pH adjuster 13, and the addition frequency is adjusted to the number of times of addition over a certain period of time. P added with one opening of the solenoid valve of the device 13
It is measured by multiplying by a certain amount of the pH adjuster, and based on the measured amount of the pH adjuster added, the minicomputer 24 calculates according to the calculation formula '1, and the minicomputer 24 sends a control output signal to the variable flow rate pump 14. By outputting the substrate, the substrate is supplied to the tower base 25 at an appropriate supply rate. F=C・N・
q......'1} Here, F: Substrate supply rate C: Constant determined by the bacterial species N: Number of additions obtained by integrating the addition frequency of the pH adjuster over a certain period q: One time of the solenoid valve of the pH adjuster P added at valve opening
Fixed amount of H adjuster In such a high-yield culture method for microorganisms, the pH of the medium is proportional to the rate of change in pH when the pH of the medium during cultivation is controlled to always be at the set value.
By controlling the rate of substrate supply to the culture medium depending on the amount of pH adjuster added to bring the pH value to the set value, it is possible to prevent excess or deficiency of carbon source during culture.

本発明は、以上説明したように、増殖に伴なつて酸ある
いはアルカリ性物質を代謝する微生物を、環境条件を微
生物の増殖に好ましい条件に制御しつつ、pH調整剤の
添加量を測定し、該添加量に基づいて基質供給速度を制
御する微生物の高収率培養法であるので、培養中の炭素
源の過不足を防止でき、微生物の高収率を達成できる効
果がある。
As explained above, the present invention measures microorganisms that metabolize acid or alkaline substances as they grow by measuring the amount of a pH adjuster added while controlling the environmental conditions to conditions favorable for the growth of microorganisms. Since this is a high-yield culture method for microorganisms that controls the substrate supply rate based on the amount added, it is possible to prevent excess or deficiency of carbon source during culture, and has the effect of achieving a high yield of microorganisms.

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

図面は、本発明の−実施例を説明するもので、本発明を
実施した微生物の高収率培養装置の系統図である。 10・・・・・・培養槽、11・・・・・・駆動装置、
12・・・・・・縄梓翼、13・・・・・・餌調節装置
、14・・・・・・流量可変ポンプ、15・・・・・・
排気流量調節弁、16・・・・・・圧力計、17…・・
・pH電極、18・・・・・・測定抵抗体、19・・・
・・・溶存酸素濃度計、20・・・・・・通気用導管、
21・・・・・・ジャケット、22・・・・・・冷却水
流量調節弁、23....・・A/D変換器、24・・
・・・・ミニコン。
The drawing explains an embodiment of the present invention, and is a system diagram of a high-yield culturing apparatus for microorganisms in which the present invention is implemented. 10... Culture tank, 11... Drive device,
12...Road Azusa Tsubasa, 13...Bait adjustment device, 14...Variable flow rate pump, 15...
Exhaust flow rate control valve, 16... Pressure gauge, 17...
・pH electrode, 18... Measuring resistor, 19...
... Dissolved oxygen concentration meter, 20 ... Ventilation conduit,
21...Jacket, 22...Cooling water flow rate control valve, 23. .. .. ..・・A/D converter, 24・・
...Minicomputer.

Claims (1)

【特許請求の範囲】 1 増殖に伴なつて酸あるいはアルカリ性物質を代謝す
る微生物を、環境条件を微生物の増殖に好ましい条件に
制御しつつ培養する方法において、pH調整剤の添加量
を測定し、該添加量に基づいて基質供給速度を制御する
ことを特徴とする微生物の高収率培養法。 2 前記pH調整剤の添加量を、既知の一定量を遂次添
加し、その添加頻度を一定期間積算した添加回数に既知
の一定量を乗ずることにより測定する特許請求の範囲第
1項記載の微生物の高収率培養法。
[Scope of Claims] 1. A method for culturing microorganisms that metabolize acid or alkaline substances as they grow while controlling environmental conditions to conditions favorable for the growth of microorganisms, including measuring the amount of a pH adjuster added, A high-yield culture method for microorganisms, characterized in that the substrate supply rate is controlled based on the amount added. 2. The method according to claim 1, wherein the amount of the pH adjuster added is measured by sequentially adding a known constant amount, and multiplying the addition frequency by the known constant amount by adding up the addition frequency over a certain period of time. High-yield culture method for microorganisms.
JP56194517A 1981-12-04 1981-12-04 High-yield culture method for microorganisms Expired JPS6018392B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56194517A JPS6018392B2 (en) 1981-12-04 1981-12-04 High-yield culture method for microorganisms

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56194517A JPS6018392B2 (en) 1981-12-04 1981-12-04 High-yield culture method for microorganisms

Publications (2)

Publication Number Publication Date
JPS5898085A JPS5898085A (en) 1983-06-10
JPS6018392B2 true JPS6018392B2 (en) 1985-05-10

Family

ID=16325844

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56194517A Expired JPS6018392B2 (en) 1981-12-04 1981-12-04 High-yield culture method for microorganisms

Country Status (1)

Country Link
JP (1) JPS6018392B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61224982A (en) * 1985-03-29 1986-10-06 Hitachi Ltd Method of controlling ph of culture tank
JP2686108B2 (en) * 1988-10-07 1997-12-08 株式会社日立製作所 Fed-batch culture method and apparatus for microorganisms
JP3958089B2 (en) * 2002-03-26 2007-08-15 有限会社新世紀発酵研究所 Continuous culture of anaerobic bacteria

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
JOURNAL OF FERMENTATION TECHNOLOGY V56=1978 *

Also Published As

Publication number Publication date
JPS5898085A (en) 1983-06-10

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