JPS5832595B2 - L-Glutamine Seizouhou - Google Patents

L-Glutamine Seizouhou

Info

Publication number
JPS5832595B2
JPS5832595B2 JP14252775A JP14252775A JPS5832595B2 JP S5832595 B2 JPS5832595 B2 JP S5832595B2 JP 14252775 A JP14252775 A JP 14252775A JP 14252775 A JP14252775 A JP 14252775A JP S5832595 B2 JPS5832595 B2 JP S5832595B2
Authority
JP
Japan
Prior art keywords
temperature
glutamic acid
biotin
growth
culture
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
JP14252775A
Other languages
Japanese (ja)
Other versions
JPS5266687A (en
Inventor
義夫 広瀬
孝志 高木
春生 百瀬
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 JP14252775A priority Critical patent/JPS5832595B2/en
Publication of JPS5266687A publication Critical patent/JPS5266687A/en
Publication of JPS5832595B2 publication Critical patent/JPS5832595B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 この発明は、微生物を用いて、L−グルタミン酸を製造
する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing L-glutamic acid using microorganisms.

生育にビオチンを必要とする典型的なL−グルタミン酸
生産菌は、通常の培養温度、たとえば30℃では、その
L−グルタミン酸生産性が培地中のビオチン濃度にきわ
めて敏感であって、生育にとって制限量のビオチン濃度
のときはじめてL−グルタミン酸を生産できる。
Typical L-glutamic acid-producing bacteria, which require biotin for growth, have L-glutamic acid productivity that is extremely sensitive to the biotin concentration in the medium at normal culture temperatures, such as 30°C, and the amount of L-glutamic acid is the limiting amount for growth. L-glutamic acid can only be produced when the biotin concentration is .

あえて過剰のビオチンを含有する培地でL−グルタミン
酸を生産するためには、ペニシリンのような抗生物質、
「ツイン60」のような界面活性剤等高価な生理活性物
質を培養中に添加せねばならず、ビオチンを豊富に含有
する各種糖質原料を経済的に利用する場合の欠点の一つ
であった。
In order to produce L-glutamic acid in a medium containing an excess of biotin, antibiotics such as penicillin,
Expensive physiologically active substances such as surfactants such as ``Twin 60'' must be added during culture, which is one of the drawbacks when using various carbohydrate raw materials rich in biotin economically. Ta.

本発明者らは、従来知られているL−グルタミン酸生産
菌を親株として変異誘導した温度感受性を有する変異株
を好気的に培養すると、ビオチンの作用を抑制するため
の生理活性物質を添加することなく高い収率でL−グル
タミン酸を生産できることを知った。
The present inventors have demonstrated that when a temperature-sensitive mutant strain, which has been mutated from a conventionally known L-glutamic acid producing bacterium as a parent strain, is cultured aerobically, a physiologically active substance is added to suppress the action of biotin. I learned that it is possible to produce L-glutamic acid in high yield without any problems.

この発明は、これらの知見にもとずいて完成されるに至
ったものである。
This invention has been completed based on these findings.

更に詳細に説明する。This will be explained in more detail.

本発明の温度感受性変異株は、ブレビバクテリウム属の
L−グルタミン酸生産能を有する微生物を親株として変
異誘導されたものである。
The temperature-sensitive mutant strain of the present invention is a strain induced by mutation using a microorganism of the genus Brevibacterium having L-glutamic acid-producing ability as a parent strain.

変異誘導方法は、通常の方法でよく、変異処理された親
株から温度感受性変異株を選択する方法は、要は親株の
生育可能な高い温度で生育しえないような変異株であっ
て、かつ低温では親株と同様に生育しうるものを選択す
ればよい。
The mutation induction method may be a conventional method, and the method for selecting a temperature-sensitive mutant strain from a mutated parent strain is to select a mutant strain that cannot grow at the high temperature at which the parent strain can grow, and You can choose a strain that can grow in the same way as the parent strain at low temperatures.

かくして得られた温度感受性変異株は、例えば以下の菌
株がある。
The temperature-sensitive mutant strains thus obtained include, for example, the following strains.

これらの菌株は、ブレビバクテリウム・フラブムATC
C14067、ブレビバクテリウム・ラクトファーメン
タムATCC13869をそれぞれ親株として誘導した
ものである。
These strains are Brevibacterium flavum ATC
C14067 and Brevibacterium lactofermentum ATCC13869 were derived as parent strains, respectively.

ブレビバクテリウム・フラブムAJ3957FERM−
P 3307ブレビバクテリウム・ラクトファーメン
タムAJ 3955 FERM−P3305ブレビバク
テリウム・ラクトファーメンタムAJ3956 FER
M−P 330にれらの変異株の高温・低温両温度条件
下での生育の状況を親株と比較して第1表に示す。
Brevibacterium flavum AJ3957FERM-
P 3307 Brevibacterium lactofermentum AJ 3955 FERM-P3305 Brevibacterium lactofermentum AJ3956 FER
Table 1 shows the growth status of these mutant strains of M-P 330 under both high and low temperature conditions in comparison with the parent strain.

本発明の温度感受性変異株は、ビオチンを過剰に含有す
る培地を用いてL−グルタミン酸を生産する場合に特に
著しい効果を現わす。
The temperature-sensitive mutant strain of the present invention exhibits particularly remarkable effects when L-glutamic acid is produced using a medium containing excess biotin.

すなわち、ビオチンを過剰に含有する培地に従来のL−
グルタミン酸生産菌を培養する場合には、ペニシリン、
界面活性剤等のビオチンの作用を抑制するような薬剤を
培地に添加しなければならない。
That is, conventional L-
When culturing glutamic acid producing bacteria, penicillin,
A drug such as a surfactant that suppresses the action of biotin must be added to the medium.

しかるに、本発明の温度感受性変異株を用い、ビオチン
を過剰に含有する培地を用いてLグル タミン酸を生産する場合には、大変異株がある程度増殖
する1での間は、よく増殖出来るような低い温度で培養
し、所望の生育量に達した時点より増殖が抑制されるよ
うな高い温度に変換するのみで、ビオチンの作用を抑制
するような薬剤を添加することなく、高い収率でL−グ
ルタミン酸を得ることが出来る。
However, when producing L-glutamic acid using the temperature-sensitive mutant strain of the present invention in a medium containing excess biotin, the temperature must be low enough to allow good growth during the time period 1 when the large mutant strain grows to a certain extent. By simply culturing at a high temperature and changing the temperature to a high temperature that inhibits growth once the desired growth amount is reached, L- can be grown in high yield without adding any drugs that inhibit the action of biotin. Glutamic acid can be obtained.

これらの温度感受性変異株を培養する培地は、通常のL
−グルタミン酸生産によく知られている培地がいずれも
使用出来る。
The medium for culturing these temperature-sensitive mutants is the usual L
- Any well-known culture medium for glutamic acid production can be used.

炭素源としては、グルコース、シュークロース、酢酸、
エタノール等の通常のものが使用出来る。
Carbon sources include glucose, sucrose, acetic acid,
Ordinary substances such as ethanol can be used.

特にモラツセス、果汁等のビオチンを多量に含有するよ
うな天然原料を炭素源として使用する場合には、上述の
ように特に著しい効果が得られる。
In particular, when natural raw materials containing a large amount of biotin, such as molasses and fruit juice, are used as the carbon source, particularly remarkable effects can be obtained as described above.

培養条件についても従来のL−グルタミン酸生産菌にお
いて採用されていた条件と特にかわる点はないが、ビオ
チンを過剰に含有する培地を用いる場合には、先に述べ
たように、一定の生育量に達する迄は増殖に適した低い
温度で培養を行い、その後高い温度でL−グルタミン酸
を生成せしめると高い収率でL−グルタミン酸を得るこ
とができる。
The culture conditions are not particularly different from those used for conventional L-glutamic acid producing bacteria, but when using a medium containing excess biotin, as mentioned earlier, it is difficult to maintain a certain growth amount. L-glutamic acid can be obtained in a high yield by culturing at a low temperature suitable for growth until reaching this point, and then producing L-glutamic acid at a high temperature.

増殖に適した低い温度は、培養すべき変異株を各種温度
で培養して調べればよいが、通常29ないし35℃、望
ましくは30ないし34℃である。
The low temperature suitable for growth can be determined by culturing the mutant strain to be cultured at various temperatures, but it is usually 29 to 35°C, preferably 30 to 34°C.

L−グルタミン酸を生成せしめる高い温度とは、当該変
異株が殆んど増殖することが出来ず、しかしL−グルタ
ミン酸は旺盛に生産するような温度が良い。
The high temperature at which L-glutamic acid is produced is preferably a temperature at which the mutant strain can hardly proliferate, but L-glutamic acid is actively produced.

通常この温度は34ないし43℃であり、特に35°な
いし42℃が好ましい。
Usually this temperature is between 34° and 43°C, particularly preferably between 35° and 42°C.

低い温度から高い温度へ移行する際の生育量は、親株が
最も旺盛にL−グルタミン酸を生産するような生育量と
同じか、もしくはそれよりやへ低い値である。
The amount of growth when changing from a low temperature to a high temperature is the same as, or slightly lower than, the amount of growth at which the parent strain most actively produces L-glutamic acid.

一般に、高い温度に移行しても、直ちに生育が抑制され
ず、若干の生育を許すことが多いので、L−グルタミン
酸生産に望ましい条件を知るためには、予め温度移行時
の生育量と移行温度の至適値を調べておくとよい。
Generally, even when the temperature is shifted to a higher temperature, growth is not immediately suppressed and some growth is often allowed. Therefore, in order to know the desirable conditions for L-glutamic acid production, it is necessary to determine the amount of growth at the time of temperature shift and the temperature at which the temperature will shift. It is a good idea to investigate the optimal value of .

かくして、■ないし3日後には、培養液中に著量のL−
グルタミン酸が生成蓄積される。
Thus, after ■ to 3 days, a significant amount of L-
Glutamic acid is produced and accumulated.

培養液からのL−グルタミン酸の採取は公知の方法のい
づれでもよい。
L-glutamic acid may be collected from the culture solution by any known method.

実施例 1 グルコース3.6 g/dl 、 KH2PO40,1
g/dl、MgSO4’ 7H200,1g/dl、
FeSO4” 7H201m9/cll、 Mn SO
4・4 H201In97dl!、大豆分解濃縮液(全
窒素として)24■/di、ビオチン30μ9/11、
サイアミン塩酸塩100μg/13 、尿素(別に殺菌
) 0.797diの組成を有する培地を調製し、pH
を7.0に調整した後30wLlづつ500r/ll容
の振盪フラスコに入れ、115℃で10分加熱殺菌した
Example 1 Glucose 3.6 g/dl, KH2PO40.1
g/dl, MgSO4' 7H200, 1g/dl,
FeSO4” 7H201m9/cll, Mn SO
4.4 H201In97dl! , soybean decomposition concentrate (as total nitrogen) 24μ/di, biotin 30μ9/11,
Prepare a medium with the following composition: thiamine hydrochloride 100μg/13, urea (separately sterilized) 0.797di, and adjust the pH
After adjusting the temperature to 7.0, 30wLl each was placed in a 500r/l shaking flask and sterilized by heating at 115°C for 10 minutes.

この培地に第2表Aに示す菌株を接種し、まず第2表A
温度欄左に示す温度で第2表Aに示す時間振盪培養を行
ったところ、菌濃度(培養液26倍希釈液の562 n
mにおける吸光度)は第2表Aに示す通りであった。
This medium was inoculated with the bacterial strains shown in Table 2 A.
When shaking culture was performed at the temperature shown on the left side of the temperature column for the time shown in Table 2 A, the bacterial concentration (562 n of the 26-fold diluted culture solution)
The absorbance at m) was as shown in Table 2A.

この時点で第2表A温度の欄の右に示す温度に上昇させ
て更に培養をつゾけ、第2表Aに示す全培養時間後に最
終菌濃度およびL−グルタミン酸の蓄積量を測定したと
ころ、各々第2表Aに示す通りであった。
At this point, the temperature was raised to the temperature shown on the right in the temperature column of Table 2 A, and the culture was further incubated. After the total culture time shown in Table 2 A, the final bacterial concentration and the accumulated amount of L-glutamic acid were measured. , respectively as shown in Table 2A.

未来実施例 2 実施例1に述べた培地組成のうち、炭素源をグルコース
からケイン・モラツセスにかえた。
Future Example 2 In the medium composition described in Example 1, the carbon source was changed from glucose to Cane molasses.

3.6g/dlのグルコースに相当する量を添加すると
、培地中には200μ9/13の高濃度ビオチンが含ま
れる。
When an amount equivalent to 3.6 g/dl of glucose is added, the medium contains a high concentration of biotin of 200 μ9/13.

この培地(ただし尿素はAJ3955については初濃度
を0.4597dlとし、培養23時間目に更に0.4
5 g/dlをフィード、AJ3956については初め
から0.997di添加)を20m1づつ500mA容
の振盪フラスコに入れ殺菌後、第2表Hに示す菌株を接
種し、まず第2表B温度欄左に示す温度で第2表Bに示
す時間振盪培養を行ったところ、菌濃度は第2表Bに示
す通りであった。
This medium (however, for AJ3955, the initial concentration of urea was 0.4597 dl, and an additional 0.4 dl was added at the 23rd hour of culture).
5 g/dl (for AJ3956, 0.997 di added from the beginning) was put into 500 mA shaking flasks in 20 ml portions and sterilized, then inoculated with the strains shown in Table 2 H. When shaking culture was carried out at the temperature shown for the time shown in Table 2B, the bacterial concentrations were as shown in Table 2B.

この時点で第2表B温度の欄の右に示す温度に上昇させ
て更に培養をつゾけ、第2表Bに示す全培養時間後に最
終菌濃度およびL−グルタミン酸の蓄積量を測定したと
ころ、各々第2表Bに示す通りであった。
At this point, the temperature was raised to the temperature shown on the right side of the temperature column in Table 2 B, and the culture was further incubated. After the total culture time shown in Table 2 B, the final bacterial concentration and the accumulated amount of L-glutamic acid were measured. , as shown in Table 2B.

Claims (1)

【特許請求の範囲】[Claims] 1 ブレビバクテリウム属の、温度感受性を有し、グル
タミン酸生産能を有する変異株を好気的に培養し、培養
液中にL−グルタミン酸を生成蓄積せしめ、これを採取
することを特徴とするL−グルタミン酸の製造法。
1 L-glutamic acid is produced and accumulated in the culture solution by aerobically culturing a temperature-sensitive mutant strain of Brevibacterium that has the ability to produce glutamic acid, and the L-glutamic acid is collected. - A method for producing glutamic acid.
JP14252775A 1975-11-28 1975-11-28 L-Glutamine Seizouhou Expired JPS5832595B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14252775A JPS5832595B2 (en) 1975-11-28 1975-11-28 L-Glutamine Seizouhou

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14252775A JPS5832595B2 (en) 1975-11-28 1975-11-28 L-Glutamine Seizouhou

Publications (2)

Publication Number Publication Date
JPS5266687A JPS5266687A (en) 1977-06-02
JPS5832595B2 true JPS5832595B2 (en) 1983-07-14

Family

ID=15317420

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14252775A Expired JPS5832595B2 (en) 1975-11-28 1975-11-28 L-Glutamine Seizouhou

Country Status (1)

Country Link
JP (1) JPS5832595B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57102193A (en) * 1980-12-17 1982-06-25 Kyowa Hakko Kogyo Co Ltd Preparation of l-glutamic acid

Also Published As

Publication number Publication date
JPS5266687A (en) 1977-06-02

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