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JPH0449995B2 - - Google Patents
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JPH0449995B2 - - Google Patents

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Publication number
JPH0449995B2
JPH0449995B2 JP19907683A JP19907683A JPH0449995B2 JP H0449995 B2 JPH0449995 B2 JP H0449995B2 JP 19907683 A JP19907683 A JP 19907683A JP 19907683 A JP19907683 A JP 19907683A JP H0449995 B2 JPH0449995 B2 JP H0449995B2
Authority
JP
Japan
Prior art keywords
substrate
amount
yeast
culture
fed
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
JP19907683A
Other languages
Japanese (ja)
Other versions
JPS6091979A (en
Inventor
Norio Shimizu
Kenji Kato
Yoji Otahara
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 JP19907683A priority Critical patent/JPS6091979A/en
Publication of JPS6091979A publication Critical patent/JPS6091979A/en
Publication of JPH0449995B2 publication Critical patent/JPH0449995B2/ja
Granted 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】 〔発明の利用分野〕 本発明は微生物の好気的培養方法に係わり、と
くに酵母培養において基質流加量を制御する方法
及び装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a method for aerobically cultivating microorganisms, and particularly to a method and apparatus for controlling the amount of substrate added in yeast culture.

〔発明の背景〕[Background of the invention]

食・飼料酵母、パン酵母などの酵母菌体の生産
においては培養中に基質を少量ずつ供給する流加
培養法が行われている。この培養を効率よく実施
するには流加した基質が完全に酵母に消費され、
かつエタノール等の副生成物が少ないことが必須
である。
In the production of yeast cells such as food/feed yeast and baker's yeast, a fed-batch culture method is used in which a substrate is supplied little by little during culture. In order to carry out this culture efficiently, the fed substrate must be completely consumed by the yeast.
In addition, it is essential that by-products such as ethanol be small.

従来、培養中の菌体濃度や菌体の活性度を迅速
に測定する手段がないことから、予め定めたプロ
グラムに従い基質を培養槽に流加する方式が行わ
れていた。この方式では槽内の菌体活性に応じた
基質流加が不可能であり、生産性は高くなかつ
た。
Conventionally, since there is no means to rapidly measure the concentration of bacterial cells or the activity of bacterial cells during culture, a method has been used in which substrates are added to a culture tank according to a predetermined program. In this method, it was not possible to feed the substrate in accordance with the bacterial activity in the tank, and the productivity was not high.

[発明の目的] 本発明は前記現状に鑑みてなされたもので、そ
の目的とするところは培養中の基質流加量を適正
に制御することにより、酵母の菌体生産効率の向
上を可能にする方法及び装置を提供するものであ
る。
[Objective of the Invention] The present invention was made in view of the above-mentioned current situation, and its purpose is to improve the efficiency of yeast cell production by appropriately controlling the amount of substrate fed during culture. The present invention provides a method and apparatus for doing so.

〔発明の概要〕[Summary of the invention]

本発明の目的を達成するための基質流加方法は
エタノール等の副生成物の生成をRQの上昇によ
り検知し、基質流加量を減少させるか零にし、つ
ぎに生成した副生成物が酵母により資化されたの
を溶存酸素濃度の上昇で検知し、基質流加量を増
加させることを特徴とする方法である。
The substrate fed-batch method for achieving the purpose of the present invention detects the production of by-products such as ethanol by increasing RQ, reduces or eliminates the amount of substrate fed, and then the generated by-products are transferred to yeast. This method is characterized by detecting the assimilation by the increase in dissolved oxygen concentration and increasing the amount of substrate fed.

つぎに本発明方法を詳細に説明する。本制御方
法を実施するには、エタノールの生成及び消費を
迅速に知る必要があるが、現在のところ培養液中
のエタノール濃度を直接かつ迅速に測定する有効
な手段がない。そこで、本発明者らはエタノール
の生成を呼吸商RQで検知するとともに、エタノ
ールの酵母による消費により溶存酸素濃度が急激
に上昇する現象を発見し、本発明に至つたもので
ある。
Next, the method of the present invention will be explained in detail. To implement this control method, it is necessary to quickly know the production and consumption of ethanol, but at present there is no effective means to directly and quickly measure the ethanol concentration in the culture solution. Therefore, the present inventors detected the production of ethanol using the respiratory quotient RQ, and also discovered a phenomenon in which dissolved oxygen concentration rapidly increases due to consumption of ethanol by yeast, leading to the present invention.

糖を基質とした酵母培養において、RQ=1.0の
場合は良好な菌体増殖を示し、RQ>1.0の場合は
炭酸ガスの生成量が多いことからエタノールの生
成を示している。そこで、RQ>1.0の場合はエタ
ノールが生成したとして、基質流加を減少または
停止する。一方、RQ<1.0の場合は基質不足か、
生成したエタノールを酵母が資化しているかどち
らかであり、エタノールを酵母が十分に消費した
かどうかを判定できない。しかし、基質流加を減
少または停止させた状態で培養液中のエタノール
が酵母に十分に資化されると、酵母による酸素消
費量が減少するため、溶存酸素濃度が急激に上昇
する。この溶存酸素濃度の急激な上昇を検知する
ことにより、エタノールの十分な消費を推測し、
基質流加量を増加させるのである。
In yeast culture using sugar as a substrate, RQ = 1.0 indicates good cell growth, and RQ > 1.0 indicates ethanol production because a large amount of carbon dioxide gas is produced. Therefore, if RQ > 1.0, it is assumed that ethanol has been produced, and the substrate feeding is reduced or stopped. On the other hand, if RQ<1.0, it may be due to insufficient substrate.
Either the yeast is assimilating the produced ethanol, and it cannot be determined whether the yeast has sufficiently consumed the ethanol. However, when the ethanol in the culture solution is sufficiently assimilated by the yeast with substrate feeding reduced or stopped, the amount of oxygen consumed by the yeast decreases, and the dissolved oxygen concentration rapidly increases. By detecting this rapid rise in dissolved oxygen concentration, it is possible to infer sufficient consumption of ethanol.
This increases the amount of substrate fed.

実験例を第1図に示す。培養開始2.5時間で、
呼吸商RQが1.0を越え、エタノールの生成が検知
された。このとき、エタノール濃度は9g/以
上に達しており、対糖収率は低下する傾向にあつ
た。そこで、3時間目から菌体量当りの基質流加
速度(α値と称す)を零として基質流加を停止
し、生成したエタノールを酵母に資化させた。培
養開始から5時間目には、それまでほぼ4〜6
mg/の範囲に制御されていた溶存酸素(DO)
濃度が急速に上昇し、エタノールの資化による減
少が検知されたので、基質流加を再開した。資質
流加の停止時間中、対糖収率は増加傾向にあり、
基質流加再開時に最大値0.53となつた。
An experimental example is shown in FIG. 2.5 hours after the start of culture,
The respiratory quotient RQ exceeded 1.0, and ethanol production was detected. At this time, the ethanol concentration reached 9 g/or more, and the yield relative to sugar tended to decrease. Therefore, starting from the third hour, the substrate flow acceleration per bacterial cell amount (referred to as the α value) was set to zero, and the substrate feeding was stopped, and the produced ethanol was assimilated by the yeast. By the 5th hour after the start of culture, approximately 4 to 6
Dissolved oxygen (DO) controlled in the range of mg/
Substrate feeding was resumed as the concentration rose rapidly and a decrease due to ethanol assimilation was detected. During the suspension time of quality fed batch, the sugar yield tends to increase,
The maximum value reached 0.53 when substrate feeding was restarted.

本発明に用いられる基質としてグルコース、フ
ラクトース、シユクロース及び工業用原料の糖蜜
等がある。また、副原料として通常の培養に用い
られる硫安、尿素、アンモニア水、リン酸一カリ
ウム、酵母エキス、硫酸マグネシウム、硫酸第1
鉄及び各種ビタミン、ミネラルなどがある。
Substrates used in the present invention include glucose, fructose, sucrose, and industrial raw material molasses. In addition, ammonium sulfate, urea, aqueous ammonia, monopotassium phosphate, yeast extract, magnesium sulfate, monosulfuric acid sulfate, which are used in normal culture as auxiliary raw materials.
It contains iron and various vitamins and minerals.

本発明方法の培養装置例を第2図に示す。培養
槽1内に種菌を入れ、基質タンク7より基質を基
質供給ポンプ8により供給する。この時、入口酸
素分圧測定器5、入口ガス量測定器6、出口ガス
の酸素分圧測定器11、炭酸ガス分圧測定器1
2、排ガス量測定器13からのデータを制御用電
子計算機4に入れて呼吸商RQを算出し、これか
らα値を変更して基質流加速度を制御し、その速
度に応じて基質供給ポンプ8を稼働させる。副生
成物の生成が検知され、基質流加が微少、あるい
は零になつている場合は、溶存酸素センサ9の信
号を溶存酸素計10で検知して電気計算機4に送
り、その変化からα値を変えて基質流加速度を制
御する。また培養中は、菌体に酸素が充分に供給
されるように、2mg/以上に維持する必要があ
るが、これは電子計算機4に送られた溶存酸素濃
度データから撹拌機2で回転数、酸素分離機3に
より入口ガス酸素濃度と入口ガス量を制御するこ
とにより溶存酸素濃度を一定値に維持する。
An example of a culture apparatus for the method of the present invention is shown in FIG. Inoculum is placed in a culture tank 1, and a substrate is supplied from a substrate tank 7 by a substrate supply pump 8. At this time, an inlet oxygen partial pressure measuring device 5, an inlet gas amount measuring device 6, an outlet gas oxygen partial pressure measuring device 11, a carbon dioxide gas partial pressure measuring device 1
2. The data from the exhaust gas amount measuring device 13 is input into the control electronic computer 4 to calculate the respiratory quotient RQ, from which the α value is changed to control the substrate flow acceleration, and the substrate supply pump 8 is activated according to the speed. put it into operation. When the production of by-products is detected and the substrate feeding amount is very small or zero, the signal from the dissolved oxygen sensor 9 is detected by the dissolved oxygen meter 10 and sent to the electronic computer 4, and the α value is determined from the change. The substrate flow acceleration is controlled by changing the Also, during cultivation, it is necessary to maintain the oxygen level at 2 mg/min or more so that the bacterial cells are sufficiently supplied with oxygen. By controlling the inlet gas oxygen concentration and the inlet gas amount using the oxygen separator 3, the dissolved oxygen concentration is maintained at a constant value.

〔発明の実施例〕[Embodiments of the invention]

以下、本発明の一実施例を具体的に説明する
が、本発明はこれによりなんら限定されるもので
はない。
Hereinafter, one embodiment of the present invention will be described in detail, but the present invention is not limited thereto.

菌体;Saccharomyces cerevisiae(パン酵母) 培地;グルコース500g、尿素53.75g、
Na2HPO4・2H2O25g、MgSO4・7H2O9.5g、
KC5.5g、クエン酸ナトリウム62.5g、酵母エ
キス12.2g、ビタミン液25ml及びミネラル液25ml
を水道水1に加え、溶解し、PH5.0に調整した。
Bacterial body: Saccharomyces cerevisiae (baker's yeast) Medium: glucose 500g, urea 53.75g,
Na2HPO4 2H2O25g , MgSO47H2O9.5g ,
KC5.5g, sodium citrate 62.5g, yeast extract 12.2g, vitamin liquid 25ml and mineral liquid 25ml
was added to tap water 1, dissolved, and adjusted to pH 5.0.

但し、ビタミン液はビオチン0.04g、ビタミン
B10.08g、ビタミンB62.0g、パントテン酸カル
シウム1.0g及びイノシトール20gを蒸留水1
に溶解して作成し、ミネラル液はCuSO4
5H2O0.05、ZnSO4・7H2O0.8g及びFeSO4
(NH42・6H2O0.3gを蒸留水1に溶解して作
成した。
However, the vitamin liquid contains 0.04g of biotin and vitamin
B 1 0.08g, vitamin B 6 2.0g, calcium pantothenate 1.0g and inositol 20g in distilled water 1
Mineral liquid is prepared by dissolving CuSO4 .
5H2O0.05 , ZnSO47H2O0.8g and FeSO4
It was prepared by dissolving 0.3 g of (NH 4 ) 2 ·6H 2 O in 1 part of distilled water.

培養条件;50溶ジヤーフアーメンターを用
い、温度30℃、PH5.0、溶存酸素濃度を撹拌機回
転数、通気ガスの酸素分圧及び通気量により4〜
6mg/の範囲に制御した。なお、通気ガスの酸
素分圧はエアーコンプレツサと酸素ボンベを用い
て変化させた。槽内圧は0.5Kg/cm2Gに、排ガス
炭酸ガス濃度は20%以内に制御した。初発液量は
15とし、初発菌体濃度は50g/、菌体当りの
基質流加速度は0.3g/g・hにした。
Culture conditions: Using a 50° fermenter, temperature: 30°C, pH: 5.0, dissolved oxygen concentration: 4 to 4 depending on stirrer rotation speed, oxygen partial pressure of aeration gas, and aeration amount
The amount was controlled within the range of 6 mg/. Note that the oxygen partial pressure of the ventilation gas was changed using an air compressor and an oxygen cylinder. The tank internal pressure was controlled at 0.5 Kg/cm 2 G, and the exhaust gas carbon dioxide concentration was controlled within 20%. The initial liquid volume is
15, the initial bacterial cell concentration was 50 g/h, and the substrate flow acceleration per bacterial cell was 0.3 g/g·h.

結果;6時間培養終了点で、エタノール濃度0
g/とし、最終対糖収率0.44とすることができ
た。このとき、流加したグルコースの99.8%が消
費され、菌体濃度は66.3g/に達した。
Result: At the end of 6 hours of culture, ethanol concentration was 0.
g/, and the final sugar yield was 0.44. At this time, 99.8% of the fed glucose was consumed, and the bacterial cell concentration reached 66.3 g/g/.

〔発明の効果〕〔Effect of the invention〕

本発明は、最終的に副生成物を少なくする基質
流加制御が可能になるため、最終対糖収率を向上
させた菌体培養が達成できる効果があり、培養槽
の生産性を向上できる。
The present invention enables substrate fed-batch control that ultimately reduces by-products, which has the effect of achieving bacterial cell culture with an improved final sugar yield, and improves the productivity of the culture tank. .

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

第1図は本発明の実験例を表わす図、第2図は
本発明の培養装置例の概略図である。 1……培養槽、2……撹拌機、3……酸素分離
機、4……制御用電子計算機、5……酸素分圧測
定機、6……入口ガス量測定器、7……基質タン
ク、8……基質供給ポンプ、9……溶存酸素セン
サ、10……溶存酸素計、11……酸素分圧測定
器、12……炭酸ガス分圧測定器、13……排ガ
ス量測定器、14,15,16,17……導管。
FIG. 1 is a diagram showing an experimental example of the present invention, and FIG. 2 is a schematic diagram of an example of a culture apparatus of the present invention. 1... Culture tank, 2... Stirrer, 3... Oxygen separator, 4... Control electronic computer, 5... Oxygen partial pressure measuring device, 6... Inlet gas amount measuring device, 7... Substrate tank , 8... Substrate supply pump, 9... Dissolved oxygen sensor, 10... Dissolved oxygen meter, 11... Oxygen partial pressure measuring device, 12... Carbon dioxide gas partial pressure measuring device, 13... Exhaust gas amount measuring device, 14 , 15, 16, 17... Conduit.

Claims (1)

【特許請求の範囲】 1 酵母の好気的な培養に際し、培養槽へ基質を
流加するにあたり、副生成物が生成した場合は基
質流加量を下げ、副生成物が酵母による資化で減
少した場合は基質流加量を上げる培養方法におい
て、呼吸商が所定値を越えた状況で副生成物が過
度に生成されたと判定して基質流加量を下げ、基
質流加量を下げた状態で溶存酸素濃度が所定値以
上に増加したとき生成された副生成物が十分に資
化されたと判定して基質流加量を上げることを特
徴とする基質流加制御方法。 2 好気的な環境下に置かれた酵母の培養槽、前
記培養槽にガスを供給する装置、前記培養槽から
ガスを排出する装置、それぞれのガスから酵母の
呼吸商を演算する装置、前記培養槽の培養液の溶
存酸素濃度を検出する装置、前記培養槽に基質を
供給する装置を備え、呼吸商が所定値を越えた状
況で副生成物が過度に生成されたと判定して基質
流加量を下げ、基質流加量を下げた状態で溶存酸
素濃度が所定値以上に増加したとき生成された副
生成物が十分に資化されたと判定して基質流加量
を上げることを特徴とする基質流加制御装置。
[Claims] 1. During aerobic cultivation of yeast, when by-products are produced when feeding substrates into a culture tank, the amount of substrate feeding is reduced, and by-products are assimilated by yeast. If it decreases, the amount of substrate fed is increased.In the culture method, if the respiratory quotient exceeds a predetermined value, it is determined that byproducts are excessively produced, and the amount of substrate fed is lowered. 1. A substrate fed-batch control method, characterized in that when the dissolved oxygen concentration increases to a predetermined value or more under the conditions, it is determined that the generated by-products have been sufficiently utilized, and the amount of substrate fed is increased. 2. A yeast culture tank placed in an aerobic environment, a device for supplying gas to the culture tank, a device for discharging gas from the culture tank, a device for calculating the respiratory quotient of yeast from each gas, and the above. It is equipped with a device that detects the dissolved oxygen concentration of the culture solution in the culture tank, and a device that supplies substrate to the culture tank, and when the respiratory quotient exceeds a predetermined value, it is determined that byproducts have been excessively produced, and the substrate flow is stopped. When the dissolved oxygen concentration increases to a predetermined value or more with the amount of substrate added and the amount of substrate fed reduced, it is determined that the generated by-products have been sufficiently utilized, and the amount of substrate fed is increased. Substrate fed-batch control device.
JP19907683A 1983-10-26 1983-10-26 Substrate fed-batch control method and device Granted JPS6091979A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19907683A JPS6091979A (en) 1983-10-26 1983-10-26 Substrate fed-batch control method and device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19907683A JPS6091979A (en) 1983-10-26 1983-10-26 Substrate fed-batch control method and device

Publications (2)

Publication Number Publication Date
JPS6091979A JPS6091979A (en) 1985-05-23
JPH0449995B2 true JPH0449995B2 (en) 1992-08-13

Family

ID=16401703

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19907683A Granted JPS6091979A (en) 1983-10-26 1983-10-26 Substrate fed-batch control method and device

Country Status (1)

Country Link
JP (1) JPS6091979A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH078231B2 (en) * 1985-03-25 1995-02-01 株式会社日立製作所 Culture control method and culture control device
WO1987001129A1 (en) * 1985-08-15 1987-02-26 Amgen Fermentation methods for hepatitis vaccine production
JPH0755149B2 (en) * 1988-05-20 1995-06-14 鐘淵化学工業株式会社 Culture method for increasing lipase activity in cells

Also Published As

Publication number Publication date
JPS6091979A (en) 1985-05-23

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