JPS6258986A - Cultivation of aerobic microorganism - Google Patents

Cultivation of aerobic microorganism

Info

Publication number
JPS6258986A
JPS6258986A JP60198866A JP19886685A JPS6258986A JP S6258986 A JPS6258986 A JP S6258986A JP 60198866 A JP60198866 A JP 60198866A JP 19886685 A JP19886685 A JP 19886685A JP S6258986 A JPS6258986 A JP S6258986A
Authority
JP
Japan
Prior art keywords
anode
potential
culture
electrode
microorganism
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
JP60198866A
Other languages
Japanese (ja)
Inventor
Harufumi Miwa
三輪 治文
Yasuhiro Kimura
康弘 木村
Takashi Tanaka
崇 田中
Yasutsugu Yamada
山田 耕從
Yoshio Kawahara
河原 義雄
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.)
Ajinomoto Co Inc
Original Assignee
Ajinomoto Co Inc
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 Ajinomoto Co Inc filed Critical Ajinomoto Co Inc
Priority to JP60198866A priority Critical patent/JPS6258986A/en
Publication of JPS6258986A publication Critical patent/JPS6258986A/en
Pending legal-status Critical Current

Links

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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Immobilizing And Processing Of Enzymes And Microorganisms (AREA)
  • Enzymes And Modification Thereof (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Abstract

PURPOSE:To reduce the volume of oxygen to be supplied without reducing the amount of a useful substance produced, by providing an anode in a culture fluid, applying a voltage capable of oxidizing the components of the respiratory system of the microorganism to carry out cultivation. CONSTITUTION:An anode (working electrode) is provided in a culture fluid of an aerobic microorganism, e.g. aerobic bacterium, actinomyces, yeast, mold or basidiomycete, and a voltage is applied through a cathode (counter electrode) for passing through a current or a standard electrode to be a potential standard to the anode. The potential to be applied to the anode is a potential sufficient to oxidize an electron carrier of the respiratory system held by the microorganism to be cultivated, i.e. cytochrome, and is preferably such a potential as not cause the decomposition of water.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、好気性微生物の培養方法に関し、更に詳細に
は、好気性微生物を、通常の通気量以下で培養し、有用
物質を生産させる方法に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for culturing aerobic microorganisms, and more specifically, a method for culturing aerobic microorganisms under a normal aeration rate or less to produce useful substances. Regarding the method.

〔従来の技術〕[Conventional technology]

好気性微生物を培養して有用物質を生産させる方法は、
工業的に極めて広範に行われている。このような好気性
微生物の培養においては、通気を行うことが一般に不可
欠であり、この通気量が不十分であると、発酵生産物の
収量が十分に上らない。この通気に要するコストは微生
物の培養による有用物質の生産コストのかなりの比重を
占めている。したがって、有用物質の生産量を低下させ
ることなく通気量すなわち酸素の供給量を少なくするこ
とができれば、極めて有利である。
The method of culturing aerobic microorganisms to produce useful substances is
It is widely used industrially. In the cultivation of such aerobic microorganisms, aeration is generally essential, and if the amount of aeration is insufficient, the yield of fermentation products will not be sufficiently high. The cost required for this aeration accounts for a considerable proportion of the cost of producing useful substances by culturing microorganisms. Therefore, it would be extremely advantageous if the amount of aeration, ie, the amount of oxygen supplied, could be reduced without reducing the production of useful substances.

一方、微生物の培養液に電極を浸漬し、通電しながら培
養を行うことにより有用物質の生産量を向上させようと
する試みがある。たとえば、特公昭53−28992号
公報にはグルタミン酸生産菌を培養して、グルタミン酸
を生産させる方法において、培養液中に陰極を設置し、
この培養液とイオン交換膜により隔離された電解液中に
陽極を設置し、培養液中に可溶性酸化還元物質を添加し
、これを介してグルタミン酸生産閑に電子を与えて還元
し、グルタミン酸の生産能を高めるという方法が記載さ
れている。しかし、この方法は、酸素供給量の低減を目
的としたものではなく、またこの方法によって、有用物
質の生産量を低下させることなく酸素の供給量を少なく
することはできない。
On the other hand, there has been an attempt to improve the production amount of useful substances by immersing an electrode in a culture solution of microorganisms and performing the culture while applying electricity. For example, Japanese Patent Publication No. 53-28992 describes a method for culturing glutamic acid-producing bacteria to produce glutamic acid, in which a cathode is installed in the culture solution,
An anode is installed in an electrolyte solution that is separated from this culture solution by an ion exchange membrane, and a soluble redox substance is added to the culture solution, which gives electrons to the glutamic acid production enzyme and reduces it, producing glutamic acid. A method to improve the ability is described. However, this method is not intended to reduce the amount of oxygen supplied, and it is not possible to reduce the amount of oxygen supplied without reducing the production amount of useful substances.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

したがって本発明の目的は、好気性微生物の培養方法に
おいて、有用物質の生産量を低下させることなく、酸素
の供給量を少なくすることができる方法を提供すること
である。本願明細書において口有用物質」とは微生物が
産生ずる物質のほか、菌体自身も含むものとする。
Therefore, an object of the present invention is to provide a method for culturing aerobic microorganisms in which the amount of oxygen supplied can be reduced without reducing the production amount of useful substances. As used herein, the term "orally useful substances" includes not only substances produced by microorganisms but also the microbial cells themselves.

〔問題点を解決するための手段〕[Means for solving problems]

本発明者は、種々検討の結果、培養液中に陽極を設置し
、この陽極に微生物の呼吸系成分を酸化しうる電位をか
けて培養を行うことにより上記目的が達成できることを
見出し、本発明を完成するに至った。
As a result of various studies, the present inventor found that the above object can be achieved by installing an anode in the culture solution and culturing by applying a potential that can oxidize the respiratory system components of microorganisms to the anode, and the present invention. I was able to complete it.

本発明は、好気性微生物の培養方法において、培養液中
に設置した陽極に微生物の呼吸系成分を酸化しうる電位
をかけて培養することを特徴とする微生物の培養方法で
ある。
The present invention is a method for culturing aerobic microorganisms, which comprises culturing by applying a potential capable of oxidizing respiratory system components of microorganisms to an anode placed in a culture solution.

本発明方法により培養される好気性微生物としては、好
気性細菌、放線菌、酵母、糸状菌、担子菌などが挙げら
れる。これらの1種または2種以上を、通常の培養に使
用されている炭素源や窒素源等を含む培地に接種し、培
養液中に設置した陽極に電位をかけて、酸素または空気
を供給し、あるいは供給することなく、培養を行う。
Examples of aerobic microorganisms that can be cultured by the method of the present invention include aerobic bacteria, actinomycetes, yeast, filamentous fungi, and basidiomycetes. One or more of these types are inoculated into a medium containing carbon sources, nitrogen sources, etc. that are used for normal culture, and a potential is applied to the anode placed in the culture solution to supply oxygen or air. , or without feeding.

本発明を実施するには、陽極すなわち作用極と、電流を
流すための陰極すなわち対極と、電位基準となる基準極
とを備えた3種式電極、あるいは作用極と対極のみから
なる2種式電極等が用いられる。
To carry out the present invention, three types of electrodes are available, each comprising an anode or working electrode, a cathode or counter electrode for passing a current, and a reference electrode serving as a potential reference, or two types of electrodes include only a working electrode and a counter electrode. Electrodes and the like are used.

作用極には、酸化インジウム、酸化ニッケル、酸化スズ
、酸化チタン等の金属酸化物半導体からなる電極;ある
いはグラファイト、カーボン等の炭素質導電性支持体や
金、白金、銀、ニッケル等の金属支持体の表面にメディ
エータ−やプロモーターを被覆してなる電極が有利に使
用される。
The working electrode is an electrode made of a metal oxide semiconductor such as indium oxide, nickel oxide, tin oxide, or titanium oxide; or a carbonaceous conductive support such as graphite or carbon, or a metal support such as gold, platinum, silver, or nickel. Advantageously, electrodes are used in which the body surface is coated with a mediator or promoter.

メディエータ−とは、メチルビオロゲンやフェリシアン
化カリ等の酸化還元物質であって、微生物の呼吸系成分
すなわちチトクロムと電極との間の電子の授受を媒介し
うる物質である。メディエータ−は培養液中に存在させ
てもよいが、前記のとおり導電性支持体表面に被覆して
使用するのが有利である。支持体表面への被覆は、メゾ
イエ−クーを水のような適当な溶媒に溶解し、その溶液
中に支持体を浸漬して表面に吸着させるか、メチルビオ
ロゲンのようなメディエータ−のばあいには、支持体表
面で電解重合を行ってポリマー化することにより被覆す
るか、あるいはフェリシアン化カリのようなメディエー
タ−のばあいには、支持体表面にあらかじめ適当なポリ
マー、たとえばポリビニルピリジンのメタノール溶液に
支持体を浸漬してその表面にポリマーを被覆したのち、
このポリマー被覆支持体をメディエータ−の溶液に浸漬
して、被覆ポリマー表面にメディエータ−を吸着させる
など、種々の方法により行うことができる。
The mediator is a redox substance such as methyl viologen or potassium ferricyanide, and is a substance that can mediate the transfer of electrons between a respiratory system component of a microorganism, that is, a cytochrome, and an electrode. Although the mediator may be present in the culture solution, it is advantageous to coat the surface of the conductive support as described above. The surface of the support can be coated by dissolving mesoiecous in a suitable solvent such as water and immersing the support in the solution to adsorb it onto the surface, or in the case of a mediator such as methyl viologen. is coated by electrolytic polymerization on the surface of the support, or in the case of a mediator such as potassium ferricyanide, a suitable polymer such as methanol of polyvinylpyridine is coated on the surface of the support in advance. After immersing the support in the solution and coating the surface with the polymer,
This can be carried out by various methods, such as immersing this polymer-coated support in a mediator solution to allow the mediator to be adsorbed onto the surface of the coated polymer.

またプロモーターは、前記導電性支持体および微生物の
呼吸系成分すなわちチトクロムの両者に対して親和性を
もち、両者の間に一定の空間を形成し、電子の授受すな
わち酸化を円滑に行わせるという機能を有するものであ
る。このようなプロモーターとしては、ビビリミジンや
ジャーナル・オブ・エレクトロアナリティカル・ケミス
トリー(J、 [Electroanal、 Chem
、)  178.  (1984)、69〜86頁に記
載されたメルカプトピリジン、ジスルフィド等の化合物
、特に73〜74頁の表1の、プロモーターとして適切
なものとして記載されているもの等が使用できる。これ
らのプロモーターを導電性支持体表面に被覆するには、
ブロモ−クーの水溶液に支持体を所定時間、たとえば2
〜3分間浸漬してプロモーターを表面に吸着させた後、
水洗すればよい。
In addition, the promoter has an affinity for both the conductive support and the respiratory system components of microorganisms, ie, cytochromes, and has the function of forming a certain space between the two and facilitating the transfer of electrons, that is, oxidation. It has the following. Such promoters include bivirimidin and the Journal of Electroanalytical Chemistry (J, [Electroanal, Chem.
, ) 178. (1984), pages 69-86, such as mercaptopyridine, disulfide, etc., and especially those listed as suitable promoters in Table 1, pages 73-74, can be used. To coat these promoters on the surface of a conductive support,
The support is placed in an aqueous solution of bromocou for a predetermined period of time, e.g.
After soaking for ~3 minutes to adsorb the promoter to the surface,
Just wash with water.

金属酸化物半導体からなる電極はそのまま使用するのが
好ましいが、上記メディエータ−を被覆して使用しても
差支えない。
Although it is preferable to use the electrode made of a metal oxide semiconductor as it is, it may be used after being coated with the above-mentioned mediator.

対極としては、上記半導体電極、導電性支持体電極、こ
れらの電極にメディエータ−やプロモーターを被覆した
電極のいずれを使用してもよく、特に制限はない。
As the counter electrode, any of the above semiconductor electrodes, conductive support electrodes, and electrodes in which these electrodes are coated with a mediator or promoter may be used, and there are no particular limitations.

本発明においては、作用極、対極の両者を培養液中に設
置してもよいし、また対極での逆反応を防止するため、
作用極を培養液を満した培養槽中に設置し、対極を、イ
オン交換膜等で培養液から隔離された室中に設置しても
よい。基準極は培養液と塩橋で接続して用いる。
In the present invention, both the working electrode and the counter electrode may be placed in the culture medium, and in order to prevent a reverse reaction at the counter electrode,
The working electrode may be placed in a culture tank filled with a culture solution, and the counter electrode may be placed in a chamber separated from the culture solution by an ion exchange membrane or the like. The reference electrode is used by connecting it to the culture solution with a salt bridge.

陽極にかける電位は、培養する微生物のもつ呼吸系電子
伝達体すなわちチトクロムを酸化するのに十分な電位で
あり、かつ水の分解を起さない程度の電位が望ましい。
The potential applied to the anode is preferably a potential sufficient to oxidize the respiratory electron carrier, ie, cytochrome, of the microorganism to be cultured, and a potential that does not cause water decomposition.

すなわち、チトクロムの酸化還元電位より責の電位であ
り、水の電解における酸素過電圧より卑の電位であるこ
とが望ましい。
That is, it is desirable that the potential be more negative than the oxidation-reduction potential of cytochrome, and more base than the oxygen overvoltage in water electrolysis.

〔発明の効果〕〔Effect of the invention〕

本発明方法によれば、有用物質の生産量を低下させるこ
となく、酸素の供給量を少なくすることができ、有用物
質の生産コストを低減することができる。
According to the method of the present invention, the amount of oxygen supplied can be reduced without reducing the production amount of useful substances, and the production cost of useful substances can be reduced.

〔実施例〕〔Example〕

以下実施例により本発明方法を更に詳細に説明する。 The method of the present invention will be explained in more detail with reference to Examples below.

実施例1 ブレビバクテリウム・ラクトフェルメンタム培養による
グルタミン酸の生産 グルコース100 g / A 、KH2PO,l g
 / 1、JS[]、  l g / 1、大豆酸加水
分解物(総窒素として)480mg/j2およびビオチ
ン300 r7Bを含む培地300mf!をB容ガラス
製培養槽A、B、Cそれぞれに入れ、この培地にブレビ
バクテリウム・ラクトフェルメンタム(Breviba
cteriumlactofermentum) (A
 T CC13869)の種培養液を5%接種し、温度
31.5℃で30時間、通気皿押培養を行った。培養8
時間口にツイーン(Tween) 60を0.2%添加
した。通気量はAllvvm (voluma ver
sus m1nute )、B : 0.2vvm 。
Example 1 Production of glutamic acid by Brevibacterium lactofermentum culture Glucose 100 g/A, KH2PO, l g
/ 1, JS[], l g / 1, 300 mf of medium containing soy acid hydrolyzate (as total nitrogen) 480 mg/j2 and biotin 300 r7B! Brevibacterium lactofermentum (Breviba
cterium lactofermentum) (A
A 5% seed culture of TCC13869) was inoculated and cultured in an aerated dish at a temperature of 31.5°C for 30 hours. Culture 8
0.2% Tween 60 was added at the beginning of the test. The ventilation volume is Allvvm (voluma ver.
sus m1nute), B: 0.2vvm.

C:0.2vνmとし、pHはアンモニアガスを用いて
7.5に調節した。攪拌は100 Qrρmで行った。
C: 0.2vνm, and the pH was adjusted to 7.5 using ammonia gas. Stirring was performed at 100 Qrρm.

培養tfA、Bには電極を設置しなかった。培養槽Cの
内壁には、水平帯状(巾約12C:m)に酸化インジウ
ムを蒸着させ、その一部よりリード線を引き出し、また
対極として白金片を用いた。白金片は培養液中に設置し
た。培養開始後、培養液と塩橋で連絡された水素標準電
極に対して+300mVの電位を酸化インジウム電極に
印加した。培養終了後、培養生産物を分析したところ、
第1表に示す結果が得られた。
No electrodes were placed in cultures tfA and B. Indium oxide was deposited on the inner wall of the culture tank C in the form of a horizontal strip (width: approximately 12 C:m), a lead wire was drawn out from a part of the strip, and a platinum piece was used as a counter electrode. The platinum piece was placed in the culture solution. After the start of the culture, a potential of +300 mV was applied to the indium oxide electrode with respect to the hydrogen standard electrode, which was connected to the culture solution via a salt bridge. After the culture was completed, the culture products were analyzed.
The results shown in Table 1 were obtained.

通気量をAの175 にしたBでは、酸素の供給不足の
ために総有機酸の生産量が増加し、目的のグルタミン酸
の生産量は約73%に低下している。
In B, where the aeration rate was 175 times that of A, the production of total organic acids increased due to the insufficient supply of oxygen, and the production of the target glutamic acid decreased to about 73%.

これに対して培養液中に陽極を設置し電位を印加したC
では、通気量をAの115 にしているにもかかわらず
、総有機酸の生産量は増加せず、すなわち酸素の供給不
足を生じることなく、目的のグルタミン酸の生産量は、
Aとほぼ同等であることがわかる。
On the other hand, C
In this case, even though the aeration rate is set to A of 115, the production of total organic acids does not increase, that is, there is no shortage of oxygen supply, and the desired production of glutamic acid is:
It can be seen that it is almost the same as A.

実施例2 サブ力ロミセス・セレビジアエ(パン酵母)による菌体
生産 グルコース50 g / 12 、 KH2PO45g
 / It 、 MgSOsIg/A’およびコーンス
チープリ力−10g/βを含む培地(pt(6,0)3
00−を、実施例1で使用したものと同様のガラス製培
養槽A、B、Cそれぞれに入れ、この培地にサブ力ロミ
セス・セレビジアx (Saccharomyces 
cerevisiae)  (F E RM  P−2
897)(AJ  14457)の種培養液を10%接
種し、温度30℃で24時間通気攪拌培養を行った。通
気量はA : 2.Ovvm 、 B :Q、 5vv
m 、 C: 0.5vvm とし、pHはl N −
NaOHを用いて6.0に調節した。攪拌は600rp
m で行った。Cの酸化インジウム電極には実施例1と
同様に水累標準電極に対して+300mVの電位を印加
した。培養生産物の分析結果を第2表に示す。
Example 2 Bacterial cell production of glucose by Romyces cerevisiae (baker's yeast) 50 g/12, KH2PO 45 g
/It, medium containing MgSOsIg/A' and Cornsteepley force-10 g/β (pt(6,0)3
00- was placed in glass culture tanks A, B, and C similar to those used in Example 1, and Saccharomyces cerevisiae x (Saccharomyces cerevisiae) was added to this medium.
cerevisiae) (F E RM P-2
897) (AJ 14457) was inoculated at 10%, and cultured with aeration and stirring at a temperature of 30°C for 24 hours. The ventilation amount is A: 2. Ovvm, B:Q, 5vv
m, C: 0.5vvm, pH is lN-
Adjusted to 6.0 using NaOH. Stirring is 600 rpm
I went with m. As in Example 1, a potential of +300 mV with respect to the water standard electrode was applied to the indium oxide electrode of C. The analysis results of the culture products are shown in Table 2.

通気量をAのAにしたBでは、酸素の供給不足のためエ
タノールの生産量が増加し、目的の菌体生産量は約50
%に低下している。これに対して、培養液中に陽極を設
置し、電位を印加したCては通気量をAの2にしている
にもかかわらず、エタノールの生産は認められず、すな
わち酸素の供給不足を生じることはなく、目的の菌体の
生産量は、Δとほぼ同等であることがわかる。
In case B, where the aeration rate is set to A, the amount of ethanol produced increases due to the lack of oxygen supply, and the desired amount of bacterial cell production is approximately 50.
%. On the other hand, in case C, in which an anode was installed in the culture medium and a potential was applied, no ethanol production was observed, even though the aeration rate was set to 2 in A, resulting in a lack of oxygen supply. It can be seen that the production amount of the target bacterial cells is almost the same as Δ.

実施例3 メディエータ−被覆電極を用いた糸状菌培養によるプロ
テアーゼの生産 ユニオンカーバイド社製パイロリティック・グラファイ
ト(直径5mm、長さ12cm)を導電性支持体として
用い、これにポリ−4−ビニルピリジンのメタノール溶
液を塗布し乾燥した。これを10−2 モル/lの濃度
のフェリシアン化カリp性溶液(pH1,5)に室温で
約10分間浸漬した後、よく水洗し、メディエータ−を
被覆したq %を作成した。11容ガラス製小型培養槽
A、B、Cを用意し、培養槽Cの内壁面に接するように
、上記電極20本を縦に配置し、各゛電極を結線した。
Example 3 Production of protease by filamentous fungus culture using mediator-coated electrodes Pyrolitic graphite manufactured by Union Carbide (diameter 5 mm, length 12 cm) was used as a conductive support, and poly-4-vinylpyridine was applied to it. A methanol solution was applied and dried. This was immersed in a potassium ferricyanide solution (pH 1.5) with a concentration of 10-2 mol/l for about 10 minutes at room temperature, and then thoroughly washed with water to prepare a q% coated mediator. Small 11-volume glass culture tanks A, B, and C were prepared, and the 20 electrodes described above were arranged vertically so as to be in contact with the inner wall surface of culture tank C, and each electrode was connected.

また対極は、実施例1と同様に白金片を用い、培養液中
に設置した。
Further, as the counter electrode, a platinum piece was used as in Example 1, and it was placed in the culture solution.

試験管に入れた種培養寒天斜面培地(グルコース1.0
%、ペプトン0.2%、麦芽エキス0.1%、酵母エキ
ス0.1%、寒天1.5%、pH7,0)上にアスペル
ギルス・フエニシス(ATCCI 4332)を接種し
、27℃で10日間培養した。胞子を採取し、0.1M
リン酸緩衝液(p)16.8)に、胞子数が約107個
/mlとなるように懸濁した。
Seed culture agar slant medium (glucose 1.0
%, peptone 0.2%, malt extract 0.1%, yeast extract 0.1%, agar 1.5%, pH 7.0) was inoculated with Aspergillus feinisis (ATCCI 4332) and incubated at 27°C for 10 days. Cultured. Collect spores and add 0.1M
The spores were suspended in phosphate buffer (p) 16.8) so that the number of spores was approximately 107/ml.

この懸濁液30−を、前記各培養槽に入れた主培地(ア
ジプロン(大豆抽出蛋白)1.5%、食添用レシチン3
.0%、KH2PO40,5%、pH6,6) 300
−に接種し、27℃で、pHを調節することなく、4日
間通気攪拌培養を行った。Cには水素標準電極に対して
+300mVの電位を印加した。通気量はA:1.Ov
vm SB:0.1vvm SC:0.1vvmとし、
攪拌は、700rpmで行った。培養液を遠心分離して
得られた上清について、常法に従いプロテアーゼ活性を
測定した。結果を第3表に示す。
This suspension 30- was added to the main medium (adipron (soybean extract protein) 1.5%, lecithin for food additive 3) in each of the culture tanks.
.. 0%, KH2PO40.5%, pH6.6) 300
- and cultured with aeration at 27°C for 4 days without adjusting the pH. A potential of +300 mV was applied to C with respect to a hydrogen standard electrode. The ventilation amount is A:1. Ov
vm SB: 0.1vvm SC: 0.1vvm,
Stirring was performed at 700 rpm. The protease activity of the supernatant obtained by centrifuging the culture solution was measured according to a conventional method. The results are shown in Table 3.

第3表 IUは1分間にチロシン1μgを生成する活性通気量を
Aの1/10にしたBでは、プロテアーゼの生産量が約
175 に低下するのに対し、培養液中に陽極を配置し
、これに電位を印加したCでは、通気量をAの1710
にして“も、Aよりもプロテアーゼの生産量が高いこと
がわかる。
Table 3 IU shows that in B, where the active aeration rate to produce 1 μg of tyrosine per minute is 1/10 that of A, the production amount of protease decreases to about 175, whereas the anode is placed in the culture medium, In C, where a potential is applied to this, the ventilation amount is 1710 that of A.
It can be seen that the production amount of protease is higher than that of A.

実施例4 プロモーター被覆電極を用いた放線菌培養による抗菌性
物質の生産 直径4 mmφ、長さ12cmの金電極表面をアルミナ
で研磨した後、1ミリモル/Ilの濃度のビス(4−ピ
リジン)ジスルフィド溶液に2分間浸漬し、次いてよく
水洗して、プロモーター被覆電極を作成した。実施例3
と同様に、11容ガラス製小型培養槽3基を用意し、そ
のうちの1基に同様に電極を配置した。
Example 4 Production of antibacterial substances by culturing actinomycetes using promoter-coated electrodes After polishing the surface of a gold electrode with a diameter of 4 mmφ and a length of 12 cm with alumina, bis(4-pyridine) disulfide at a concentration of 1 mmol/Il was applied. A promoter-coated electrode was prepared by immersing it in the solution for 2 minutes and then thoroughly rinsing with water. Example 3
Similarly, three small 11-volume glass culture tanks were prepared, and electrodes were placed in one of them in the same manner.

500ml!容坂ロフラスコに下記組成の培地(A)3
0rr11を入れ、これにストレプトミセス・グリセロ
インカルタナス819C(FERM  P4O10)を
1白金耳接種し、30℃で24時間、120回/分、7
 cmの振幅で振とう培養(種培養)を行った。この培
養液30mj!を、前記各培養槽に人・ れた下記組成
の培地(B)300mj!に接種し、pitを調節する
ことなく、30℃で50時間通気攪拌培養を行った。C
には、水素標準電極に対して+300mVの電位を印加
した。通気量はA : 0.5vvm 、 B:0.0
5vvm 、 C:0.05vvm とし、攪拌は70
0rpmで行った。
500ml! Culture medium (A) 3 with the following composition in Yosaka Lof flask
0rr11, inoculated with 1 platinum loop of Streptomyces glyceroincartanus 819C (FERM P4O10), and incubated at 30°C for 24 hours, 120 times/min, 7
Shaking culture (seed culture) was performed at an amplitude of cm. This culture solution is 30mj! 300mj of culture medium (B) with the following composition was added to each culture tank. and cultured with aeration at 30° C. for 50 hours without adjusting the pit. C
A potential of +300 mV was applied to the hydrogen standard electrode. The ventilation amount is A: 0.5vvm, B: 0.0
5vvm, C: 0.05vvm, stirring at 70
This was done at 0 rpm.

培養液を遠心分離し、得られた上清についてエシェリヒ
ア・コリ M P −2に対する抗菌活性を測定した。
The culture solution was centrifuged, and the resulting supernatant was measured for antibacterial activity against Escherichia coli MP-2.

結果を第4表に示す。The results are shown in Table 4.

第4表 通気量をへの1710にしたBでは、抗菌活性が20%
以下に低下するのに対し、通気量をへの1710にして
も、培養液中に陽極を設置し、これに電位を印加したC
では、Aとほぼ同等の抗菌活性を示すことがわかる。
Table 4 B, which has an air flow rate of 1710, has an antibacterial activity of 20%.
However, even if the aeration rate is set to 1710, an anode is installed in the culture solution and a potential is applied to it.
It can be seen that this shows almost the same antibacterial activity as A.

抗菌活性の測定法: バクト・アンチバイオテックメディアム3(ディフコ社
製品) 1.75%、寒天1.0%より成る培地(M3
培地)を120℃、15分間加熱殺菌した後20−ずつ
シャーレに分注し、放冷してプレート培地を調製する。
Measuring method for antibacterial activity: A medium consisting of 1.75% Bacto Antibiotic Medium 3 (Difco product) and 1.0% agar (M3
After heat sterilizing the culture medium at 120° C. for 15 minutes, it is dispensed into 20-mL petri dishes and left to cool to prepare a plate culture medium.

一方ペプトン0.5%、肉エキス0.5%、Naα 0
.3%、寒天0.8%より成る培地を120℃15分加
熱殺菌する。その後42℃の恒温槽に保ち培地の温度が
42℃になったら、あらかじめ37℃で17時間培養し
たエシェリヒア・コリMP−2を11Tll!に5 X
 10”個の細胞が存在する様に培地中に加える。ピペ
ットによって2mlを採取しあらかじめ作製して置いた
M3 培地表面上に加え、すばやく均一にひろげ固化さ
せる。
On the other hand, peptone 0.5%, meat extract 0.5%, Naα 0
.. A medium consisting of 3% agar and 0.8% agar is heat sterilized at 120°C for 15 minutes. After that, it was kept in a constant temperature bath at 42°C, and when the temperature of the culture medium reached 42°C, 11 Tll of Escherichia coli MP-2, which had been previously cultured at 37°C for 17 hours, was added. 5 X
Add to the medium so that 10" cells are present. Take 2 ml with a pipette and add it to the surface of the M3 medium prepared in advance, and spread quickly and uniformly to solidify.

被験液を希釈して、その溶液0.06m1!をペーノく
−・ディスク(東洋濾紙)にしみ込ませる。このペーパ
ー・ディスクを前記作製プレート上に置き37℃で17
時間培養し、被験液によってできる阻止円の大きさを測
定する。即ち、ペー、<−・ディスクの一端からエシェ
リヒア・コリMP−2生育阻止端までの距離(關)を1
mlの被験液の抗菌活性としてU/−で表示する。
Dilute the test solution and make 0.06ml of the solution! Soak it into a Penoku disc (Toyo filter paper). This paper disk was placed on the preparation plate and heated at 37°C for 17 days.
Incubate for a time and measure the size of the inhibition circle created by the test solution. That is, P,<-・The distance from one end of the disk to the end of Escherichia coli MP-2 growth inhibition
The antibacterial activity of ml of test solution is expressed as U/-.

Claims (4)

【特許請求の範囲】[Claims] (1)好気性微生物の培養方法において、培養液中に設
置した陽極に微生物の呼吸系成分を酸化しうる電位をか
けて培養することを特徴とする好気性微生物の培養方法
(1) A method for culturing aerobic microorganisms, which comprises culturing by applying a potential capable of oxidizing respiratory system components of microorganisms to an anode placed in a culture solution.
(2)陽極が、酸化金属半導体からなる特許請求の範囲
第(1)項記載の方法。
(2) The method according to claim (1), wherein the anode is made of a metal oxide semiconductor.
(3)陽極が、メディエーターを被覆した電極である特
許請求の範囲第(1)項記載の方法。
(3) The method according to claim (1), wherein the anode is an electrode coated with a mediator.
(4)陽極が、プロモーターを被覆した電極である特許
請求の範囲第(1)項記載の方法。
(4) The method according to claim (1), wherein the anode is an electrode coated with a promoter.
JP60198866A 1985-09-09 1985-09-09 Cultivation of aerobic microorganism Pending JPS6258986A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60198866A JPS6258986A (en) 1985-09-09 1985-09-09 Cultivation of aerobic microorganism

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60198866A JPS6258986A (en) 1985-09-09 1985-09-09 Cultivation of aerobic microorganism

Publications (1)

Publication Number Publication Date
JPS6258986A true JPS6258986A (en) 1987-03-14

Family

ID=16398225

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60198866A Pending JPS6258986A (en) 1985-09-09 1985-09-09 Cultivation of aerobic microorganism

Country Status (1)

Country Link
JP (1) JPS6258986A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03124593A (en) * 1989-09-29 1991-05-28 Hitachi Chem Co Ltd Panel assembly type water supply tank

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5739772A (en) * 1980-05-30 1982-03-05 Ppg Industries Inc Electric stimulation of microorganism reaction
JPS60149378A (en) * 1984-01-12 1985-08-06 Shigeo Kono Method for fermentation by charging of high-voltage static potential

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5739772A (en) * 1980-05-30 1982-03-05 Ppg Industries Inc Electric stimulation of microorganism reaction
JPS60149378A (en) * 1984-01-12 1985-08-06 Shigeo Kono Method for fermentation by charging of high-voltage static potential

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03124593A (en) * 1989-09-29 1991-05-28 Hitachi Chem Co Ltd Panel assembly type water supply tank

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