JPS6234397B2 - - Google Patents
Info
- Publication number
- JPS6234397B2 JPS6234397B2 JP14819479A JP14819479A JPS6234397B2 JP S6234397 B2 JPS6234397 B2 JP S6234397B2 JP 14819479 A JP14819479 A JP 14819479A JP 14819479 A JP14819479 A JP 14819479A JP S6234397 B2 JPS6234397 B2 JP S6234397B2
- Authority
- JP
- Japan
- Prior art keywords
- leucine
- thienylalanine
- resistant
- producing
- strain
- 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
Links
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Description
本発明は、発酵法によるL―ロイシンの製造法
に関する。
従来、L―ロイシンの発酵法による製造法とし
ては、ブレビバクテリウム属、セラチア属、サル
モネラ属、コリネバクテリウム属等の微生物を使
用する方法が知られている。
これに対し、本発明者らは、エシエリヒア属の
微生物から突然変異によつてβ―2―チエニルア
ラニン耐性株を育種することにより、著量のL―
ロイシンを生産する能力を有する菌株を得た。
発明の方法において用いられる微生物として
は、具体的には、以下のものがある。
エシエリヒア・コリ AJ 11478
(β―2―チエニルアラニン耐性、β―ヒドロ
キシロイシン耐性)
(FERM―P 5274)
エシエリヒア・コリ AJ 11479
(β―2―チエニルアラニン耐性)
(FERM―P 5275)
これらの菌株は、エシエリヒア・コリK―12
(ATCC 10798)から変異誘導したものであり、
何れもβ―2―チエニルアラニンに耐性を有する
菌株である。
これらの菌株の、β―2―チエニルアラニンに
対する耐性度を第1表に示す。これらの結果は、
下記組成の培地に各薬剤を表に示した濃度になる
ように溶解し、各菌株を接種したのち、31℃で24
時間培養を行い、菌の生育を調べたものである。
培地組成:グルコース0.5g/dl、
(NH4)2SO40.1g/dl、KH2PO40.846g/dl、ク
エン酸ナトリウム0.05g/dl、KOH 0.226g/
dl、MgSO4・4H2O0.04g/dl、FeSO4・7H2O1
mg/dl、MnSO4・4H2O1mg/dl、チアミン・塩
酸塩1mg/mlを含む。
The present invention relates to a method for producing L-leucine using a fermentation method. Conventionally, methods using microorganisms such as Brevibacterium, Serratia, Salmonella, and Corynebacterium are known as methods for producing L-leucine by fermentation. In contrast, the present inventors have developed a β-2-thienylalanine-resistant strain from a microorganism belonging to the genus Escherichia through mutation, thereby producing a significant amount of L-
A strain capable of producing leucine was obtained. Specifically, the microorganisms used in the method of the invention include the following. Escherichia coli AJ 11478 (β-2-thienylalanine resistant, β-hydroxyleucine resistant) (FERM-P 5274) Escherichia coli AJ 11479 (β-2-thienylalanine resistant) (FERM-P 5275) These strains , Esierhia Cori K-12
(ATCC 10798),
All of these strains are resistant to β-2-thienylalanine. Table 1 shows the degree of resistance of these strains to β-2-thienylalanine. These results are
Each drug was dissolved in a medium with the following composition to the concentration shown in the table, and after inoculating each bacterial strain, it was incubated at 31°C for 24 hours.
The growth of the bacteria was investigated by culturing over time. Medium composition: glucose 0.5g/dl,
(NH 4 ) 2 SO 4 0.1g/dl, KH 2 PO 4 0.846g/dl, sodium citrate 0.05g/dl, KOH 0.226g/dl
dl, MgSO 4・4H 2 O0.04g/dl, FeSO 4・7H 2 O1
Contains mg/dl, MnSO 4 4H 2 O 1mg/dl, thiamine hydrochloride 1mg/ml.
【表】
本発明でいう薬剤耐性とは、上記培養条件下に
おいて、薬剤が存在するときの比生育度が親株で
あるエシエリヒア・コリ―K―12よりも大である
場合をいう。又比生育度は、薬剤が無添加のとき
の菌の生育量(接種菌量を差し引いた量)を100
とした。生育は570nmの吸光度で測定した。
L―ロイシン生産のための培養培地は特に制限
せず、炭素源、窒素源、無機塩及び必要ならば有
機微量栄養素を含有する通常の培地が用いられ
る。炭素源として含水炭素(グルコース、シユク
ロース、フラクトース、ラクトース及びこれらを
含有するデンプンやセルロース等の加水分解物、
糖蜜、ホエイ等)、有機酸(酢酸、クエン酸等)、
アルコール(グリセリン、エタノール)が使用で
きる。窒素源としては、アンモニウム塩(硫酸ア
ンモニウム、硝酸アンモニウム、リン酸アンモニ
ウム、塩化アンモニウム等)、アンモニアガス、
アンモニア水等が使用できる。無機塩としてはリ
ン酸塩、マグネシウム塩、カルシウム塩、鉄塩、
マンガン塩、微量金属塩等を必要に応じて使用す
る。有機微量栄養素としては、栄養要求性のある
場合には、該当するアミノ酸、ビタミン、脂肪酸
類、有機塩基物質等を適当量添加し、必要に応じ
てさらに生育促進物質としてアミノ酸、ビタミン
及びこれらを含有する大豆加水分解物、酵母エキ
ス、ペプトン、カザミノ酸等を使用する。
培養条件は通常の方法でよく、PH5ないし9、
温度20℃ないし45℃、好気条件下に20ないし96時
間培養すればよい。培養中にPHが下るときには、
炭酸カルシウムを別殺菌して加えるか又はアンモ
ニア水、アンモニアガス等のアルカリで中和す
る。
L―ロイシンの培養液からの採取は常法により
行なうことができる。
実施例 1
グルコース5g/dl、(NH4)2SO42.5g/dl、
KH2PO40.2g/dl、MgSO4・7H2O0.1g/dl、酵
母エキス0.05g/dl、サイアミン塩酸塩1000γ/
、FeSO4・7H2O1mg/dl、MnSO4・4H2O1mg/
dl、炭酸カルシウム2.5g/dlの組成をもち、PH
7.0の水溶液培地を500mlフラスコに20ml分注し、
これに各菌株を1白金耳植えつけ、31℃で72時間
培養した。発酵終了時におけるL―ロイシンの蓄
積量は第2表の如くであつた。[Table] Drug resistance as used in the present invention refers to a case where the specific growth rate in the presence of a drug is higher than that of the parent strain Escherichia coli K-12 under the above culture conditions. In addition, the specific growth rate is the amount of bacterial growth (minus the amount of inoculated bacteria) when no chemicals are added.
And so. Growth was measured by absorbance at 570 nm. The culture medium for producing L-leucine is not particularly limited, and a conventional medium containing a carbon source, a nitrogen source, an inorganic salt, and, if necessary, an organic micronutrient is used. Hydrous carbon (glucose, sucrose, fructose, lactose, and hydrolysates containing these such as starch and cellulose) as a carbon source;
molasses, whey, etc.), organic acids (acetic acid, citric acid, etc.),
Alcohol (glycerin, ethanol) can be used. Nitrogen sources include ammonium salts (ammonium sulfate, ammonium nitrate, ammonium phosphate, ammonium chloride, etc.), ammonia gas,
Ammonia water etc. can be used. Inorganic salts include phosphates, magnesium salts, calcium salts, iron salts,
Use manganese salt, trace metal salt, etc. as necessary. As organic micronutrients, if there is a nutritional requirement, appropriate amounts of corresponding amino acids, vitamins, fatty acids, organic basic substances, etc. are added, and if necessary, amino acids, vitamins, and these are added as growth-promoting substances. Soybean hydrolyzate, yeast extract, peptone, casamino acids, etc. are used. Culture conditions may be the usual methods, pH 5 to 9;
It may be cultured at a temperature of 20°C to 45°C under aerobic conditions for 20 to 96 hours. When the pH drops during culture,
Calcium carbonate is sterilized separately and added, or neutralized with alkali such as aqueous ammonia or ammonia gas. L-leucine can be collected from the culture solution by a conventional method. Example 1 Glucose 5 g/dl, (NH 4 ) 2 SO 4 2.5 g/dl,
KH 2 PO 4 0.2g/dl, MgSO 4・7H 2 O 0.1g/dl, yeast extract 0.05g/dl, thiamine hydrochloride 1000γ/
, FeSO 4・7H 2 O1mg/dl, MnSO 4・4H 2 O1mg/dl
dl, calcium carbonate 2.5g/dl, PH
Dispense 20ml of 7.0 aqueous medium into a 500ml flask,
One platinum loop of each strain was inoculated into this, and cultured at 31°C for 72 hours. The amount of L-leucine accumulated at the end of fermentation was as shown in Table 2.
Claims (1)
ラニンに耐性を有する微生物を、液体培地中に好
気的に培養して培養液中にL―ロイシンを生成蓄
積せしめ、これを採取することを特徴とするL―
ロイシンの製造法。1 A microorganism that belongs to the genus Escherichia and is resistant to β-2-thienylalanine is aerobically cultured in a liquid medium to produce and accumulate L-leucine in the culture solution, which is then collected. L-
Method for producing leucine.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14819479A JPS5672695A (en) | 1979-11-15 | 1979-11-15 | Preparation of l-leucine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14819479A JPS5672695A (en) | 1979-11-15 | 1979-11-15 | Preparation of l-leucine |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5672695A JPS5672695A (en) | 1981-06-16 |
JPS6234397B2 true JPS6234397B2 (en) | 1987-07-27 |
Family
ID=15447351
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14819479A Granted JPS5672695A (en) | 1979-11-15 | 1979-11-15 | Preparation of l-leucine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5672695A (en) |
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WO2007136133A1 (en) | 2006-05-23 | 2007-11-29 | Ajinomoto Co., Inc. | A method for producing an l-amino acid using a bacterium of the enterobacteriaceae family |
WO2008102861A1 (en) | 2007-02-22 | 2008-08-28 | Ajinomoto Co., Inc. | Method of producing l-amino acid |
WO2009031565A1 (en) | 2007-09-04 | 2009-03-12 | Ajinomoto Co., Inc. | Amino acid-producing microorganism and method of producing amino acid |
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Families Citing this family (2)
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-
1979
- 1979-11-15 JP JP14819479A patent/JPS5672695A/en active Granted
Cited By (37)
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Also Published As
Publication number | Publication date |
---|---|
JPS5672695A (en) | 1981-06-16 |
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