JPS6224075B2 - - Google Patents

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Publication number
JPS6224075B2
JPS6224075B2 JP54053421A JP5342179A JPS6224075B2 JP S6224075 B2 JPS6224075 B2 JP S6224075B2 JP 54053421 A JP54053421 A JP 54053421A JP 5342179 A JP5342179 A JP 5342179A JP S6224075 B2 JPS6224075 B2 JP S6224075B2
Authority
JP
Japan
Prior art keywords
arginine
argininol
strain
brevibacterium
corynebacterium
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
JP54053421A
Other languages
Japanese (ja)
Other versions
JPS55148093A (en
Inventor
Kunihiko Akashi
Yayoi Nakamura
Takayasu Tsuchida
Hiroi Yoshii
Shigeo Ikeda
Masaru Okutsu
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 JP5342179A priority Critical patent/JPS55148093A/en
Publication of JPS55148093A publication Critical patent/JPS55148093A/en
Publication of JPS6224075B2 publication Critical patent/JPS6224075B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は微生物を用いて発酵によりL−アルギ
ニンを生産する方法に関する。 本発明者等はさきにブレビバクテリウム・フラ
バム及びコリネバクテリウム・アセトアシドフイ
ラムの変異株がL−アルギニンを生産蓄積するこ
とを認め、L−アルギニンの製造法を確立した。
(フランス特許7105791、イギリス特許公告
1278917)本発明者等は更にL−アルギニン生産
性の高い変異株を採取するため種々の研究を行な
つた結果、ブレビバクテリウム属又はコリネバク
テリウム属に属しアルギニノール耐性を有する変
異株が著量のL−アルギニンを培地中に生成蓄積
することを見出し本発明を完成した。 本発明の変異株の親株はブレビバクテリウム・
デイバリカタムATCC14020、ブレビバクテリウ
ム・フラバムATCC14067、ブレビバクテリウ
ム・ラクトフアーメンタムATCC13869、ブレビ
バクテリウム・ロゼウムATCC13825、コリネバ
クテリウム・アセトアシドフイラム
ATCC13870、コリネバクテリウム・リリウム
ATCC15990等である。 本発明の変異株を採取するには例えば上記親株
をN−メチル−N′−ニトロ−N−ニトロソグア
ニジン250μg/mlで30℃で30分処理し、アルギ
ニノール耐性株を採取してこれをスクリーニング
しアルギニン生産菌を採取した。 かくしてアルギニン生産能のすぐれた変異株を
採取したが、その親株及び親株より誘導したアル
ギニノール耐性株の例を下記する。 親株ブレビバクテリウム・フラバムAJ3277
(S.Dr) (ブレビバクテリウム・フラバムATCC14067
より誘導した) 耐性株 AJ11336 FERM−P 4939(S.Dr
アルギニノールr) 親株コリネバクテリウム・アセトアシドフイラ
ムAJ3278(S.Dr) (コリネバクテリウム・アセトアシドフイラム
ATCC13870より誘導した) 耐性株 AJ11340 FERM−P 4943(S.Dr)+
アルギニノールr) 親株ブレビバクテリウム・フラバムAJ 11193
(2TAr+S.Gr+His-) (ブレビバクテリウム・フラバムATCC14067
より誘導した) 耐性株 AJ11345 FERM−P 4948(2TAr
S.Gr+His-+アルギニノールr) S.Dr:サルフアダイアジン耐性、2TAr:2−
チアゾールアラニン耐性、SGr:サルフアグアニ
ジン耐性、His-:ヒスチジン要求性を示す。 下記の組成の培地にアルギニノールを添加し、
その4mlを小型試験管に分注し殺菌後上記各菌株
を接種して31℃で48時間振盪培養した。吸光度を
測定して生育度を算出し各菌株の耐性度を調べ
た。 培地組成: グルコース 2% 尿素 0.3〃 硫酸アンモニウム 1.0〃 KH2PO4 0.1〃 MgSO4・7H2O 0.04〃 Fe及びMnイオン 各2ppm ビオチン 100μg/ サイアミン塩酸塩 200μg/ PH7.0
The present invention relates to a method for producing L-arginine by fermentation using microorganisms. The present inventors previously recognized that mutant strains of Brevibacterium flavum and Corynebacterium acetoacidophyllum produce and accumulate L-arginine, and established a method for producing L-arginine.
(French patent 7105791, British patent publication
1278917) The present inventors further conducted various studies to collect mutant strains with high L-arginine production, and as a result, a significant number of mutant strains belonging to the genus Brevibacterium or Corynebacterium and having resistance to argininol were found. The inventors completed the present invention by discovering that L-arginine is produced and accumulated in the culture medium. The parent strain of the mutant strain of the present invention is Brevibacterium
Devaricatum ATCC14020, Brevibacterium flavum ATCC14067, Brevibacterium lactofamentum ATCC13869, Brevibacterium roseum ATCC13825, Corynebacterium acetoacidophyllum
ATCC13870, Corynebacterium rillium
ATCC15990 etc. To collect the mutant strain of the present invention, for example, the above parent strain is treated with 250 μg/ml of N-methyl-N'-nitro-N-nitrosoguanidine at 30°C for 30 minutes, and an argininol-resistant strain is collected and screened. Arginine producing bacteria were collected. A mutant strain with excellent arginine-producing ability was thus collected, and examples of its parent strain and argininol-resistant strains derived from the parent strain are described below. Parent strain Brevibacterium flavum AJ3277
(SD r ) (Brevibacterium flavum ATCC14067
) Resistant strain AJ11336 FERM-P 4939 (SD r +
Argininol r ) Parent strain Corynebacterium acetoacidophyllum AJ3278 (SD r ) (Corynebacterium acetoacidophyllum
(derived from ATCC13870) Resistant strain AJ11340 FERM-P 4943 (SD r ) +
Argininol r ) Parent strain Brevibacterium flavum AJ 11193
(2TA r +S.G r +His - ) (Brevibacterium flavum ATCC14067
) Resistant strain AJ11345 FERM-P 4948 (2TA r +
SG r +His - + argininol r ) SD r : sulfadiazine resistance, 2TA r : 2-
Thiazolealanine resistance, SG r : sulfaguanidine resistance, His - : histidine requirement. Add argininol to a medium with the following composition,
4 ml of the mixture was dispensed into small test tubes, sterilized, inoculated with each of the above bacterial strains, and cultured with shaking at 31°C for 48 hours. The degree of growth was calculated by measuring the absorbance and the degree of resistance of each strain was investigated. Medium composition: Glucose 2% Urea 0.3〃 Ammonium sulfate 1.0〃 KH 2 PO 4 0.1〃 MgSO 4・7H 2 O 0.04〃 Fe and Mn ions 2ppm each Biotin 100μg / Thiamine hydrochloride 200μg / PH7.0

【表】【table】

【表】 これらの微生物を用いてL−アルギニンを生産
させるには、炭素源、窒素源、無機塩類更に必要
により生育促進因子を含有する通常の栄養培地を
用いて常法により行なう。用いられる炭素源とし
てはグルコース、シユークロース、及びこれを含
有する糖蜜、デンプン加水分解液などの糖類、酢
酸、プロピオン酸などの有機酸、エタノール、プ
ロパノールなどのアルコール類、炭化水素などが
使用できる。窒素源としてはアンモニウム塩、ア
ンモニアガス、尿素、アンモニアその他が使用で
きる。 本発酵の条件は通気培養がよく、発酵温度は24
〜37℃、発酵日数は通常2〜7日である。発酵開
始時及び培養中のPHは5.0〜9.0がよく、PHの調整
には無機或いは有機の酸性又はアルカリ性物質、
更に尿素、炭酸カルシウム、アンモニアガスなど
を使用することができる。発酵液からのL−アル
ギニンの採取は通常イオン交換樹脂法その他の公
知の方法を組合わせて行なわれる。 以下実施例により本発明を具体的に説明する。 実施例 1 グルコース10g/dl、硫酸アンモニウム6g/
dl、KH2PO40.1g/dl、MgSO4・7H2O0.04g/
dl、FeSO4・7H2O1mg/dl、MnSO4・4H2O1mg/
dl、ビオチン50μg/、サイアミン塩酸塩20μ
g/、大豆蛋白酸分解液(総窒素2.4%)1
ml/dl、炭酸カルシウム5g/dl(別殺菌添加)
を含みPH7.0に調節した培地を調製し、その20ml
を500ml肩付フラスコに分注した。殺菌後あらか
じめブイヨンスラント上で生育させた。ブレビバ
クテリウム・フラバムAJ11336(SDr+アルギニ
ノールr)を接種し、31℃にて72時間振盪培養し
た。アルギニンの生成蓄積量は下記の如くであつ
た。 親株 AJ3277 1.80g/dl 耐性株 AJ11336 2.50 〃 さらに培養終了液から遠心分離により菌体およ
びカルシウム塩を除去して得た上清液1を弱酸
性イオン交換樹脂アンバーライトC−50(NH4 +
型)に通過させ、L−アルギニンを吸着させた。
水洗後2Nアンモニア水でL−アルギニンを溶出
し溶出液を濃縮した。濃縮液を冷却しL−アルギ
ニンの結晶16.2gを得た。 実施例 2 グルコース10g/dl、硫酸アンモニウム6g/
dl、KH2PO40.1g/dl、MgSO4・7H2O0.04g/
dl、FeSO4・7H2O1mg/dl、MnSO4・4H2O1mg/
dl、ビオチン50μg/、サイアミン塩酸塩20μ
g/、大豆蛋白分解液(総窒素2.4%)1mg/
dl、炭酸カルシウム5g/dl(別殺菌添加)を含
みPH7.0に調節した培地を調製し、その20mlを500
ml肩付フラスコに分注した。殺菌後あらかじめブ
イヨンスラント上で生育させたブレビバクテリウ
ム・フラバムAJ11345(SGr+2TAr+His-+アル
ギニノールr)を接種し31℃にて72時間振盪培養
した。アルギニンの生成蓄積量は下記の如くであ
つた。 親株 AJ11193 3.3g/dl 耐性株 AJ11345 3.7 〃 培養終了液を実施例1と同様に処理してL−ア
ルギニンの結晶21.5gを得た。 実施例 3 グルコース10g/dl、硫酸アンモニウム6g/
dl、KH2PO40.1g/dl、MgSO4・7H2O0.04g/
dl、FeSO4・7H2O1mg/dl、MnSO4・4H2O1mg/
dl、ビオチン50μg/、サイアミン塩酸塩20μ
g/、大豆蛋白分解液(総窒素2.4%)1mg/
dl、炭酸カルシウム5g/dl(別殺菌添加)、PH7.0
に調節した培地を調製し、その20mlを500ml肩付
フラスコに分注した。殺菌後あらかじめブイヨン
スラント上で生育させたコリネバクテリウム・ア
セトアシドフイラムAJ11340(S.Dr+アルギニノ
ールr)を接種し31℃にて72時間振盪培養した。
アルギニンの生成蓄積量は下記の如くであつた。 親株 AJ3278 1.70g/dl 耐性株 AJ11340 1.95 〃 培養終了液を実施例1と同様に処理してL−ア
ルギニンの結晶12.7gを得た。
[Table] Production of L-arginine using these microorganisms is carried out by a conventional method using a conventional nutrient medium containing a carbon source, a nitrogen source, inorganic salts, and, if necessary, growth promoting factors. Examples of carbon sources that can be used include glucose, sucrose, molasses containing the same, sugars such as starch hydrolyzate, organic acids such as acetic acid and propionic acid, alcohols such as ethanol and propanol, and hydrocarbons. Ammonium salts, ammonia gas, urea, ammonia, and others can be used as nitrogen sources. The main fermentation conditions are aeration culture, and the fermentation temperature is 24℃.
~37°C, and the number of fermentation days is usually 2 to 7 days. The pH at the start of fermentation and during cultivation is preferably 5.0 to 9.0. To adjust the pH, use inorganic or organic acidic or alkaline substances,
Furthermore, urea, calcium carbonate, ammonia gas, etc. can be used. L-arginine is usually collected from the fermentation broth by a combination of ion exchange resin method and other known methods. The present invention will be specifically explained below using Examples. Example 1 Glucose 10g/dl, ammonium sulfate 6g/dl
dl, KH 2 PO 4 0.1g/dl, MgSO 4・7H 2 O0.04g/
dl, FeSO 4・7H 2 O1mg/dl, MnSO 4・4H 2 O1mg/
dl, biotin 50μg/, thiamine hydrochloride 20μ
g/, soybean protein acid decomposition solution (total nitrogen 2.4%) 1
ml/dl, calcium carbonate 5g/dl (separate sterilization added)
Prepare a medium containing PH7.0 and add 20ml of it.
was dispensed into a 500ml flask with a shoulder. After sterilization, they were grown on a bouillon slant. Brevibacterium flavum AJ11336 (SD r + argininol r ) was inoculated and cultured with shaking at 31°C for 72 hours. The amount of arginine produced and accumulated was as follows. Parent strain AJ3277 1.80 g/dl Resistant strain AJ11336 2.50 Furthermore, the supernatant liquid 1 obtained by removing bacterial cells and calcium salts from the cultured liquid by centrifugation was added to a weakly acidic ion exchange resin Amberlite C-50 (NH 4 +
type) to adsorb L-arginine.
After washing with water, L-arginine was eluted with 2N ammonia water and the eluate was concentrated. The concentrated solution was cooled to obtain 16.2 g of L-arginine crystals. Example 2 Glucose 10g/dl, ammonium sulfate 6g/dl
dl, KH 2 PO 4 0.1g/dl, MgSO 4・7H 2 O0.04g/
dl, FeSO 4・7H 2 O1mg/dl, MnSO 4・4H 2 O1mg/
dl, biotin 50μg/, thiamine hydrochloride 20μ
g/, soy protein decomposition solution (total nitrogen 2.4%) 1 mg/
dl, prepare a medium containing 5 g/dl of calcium carbonate (separately added for sterilization) and adjust the pH to 7.0, and add 20 ml of it to 500 ml.
Dispense into ml shoulder flasks. After sterilization, Brevibacterium flavum AJ11345 (SG r + 2TA r + His - + Argininol r ), which had been grown in advance on a bouillon slant, was inoculated and cultured with shaking at 31°C for 72 hours. The amount of arginine produced and accumulated was as follows. Parent strain AJ11193 3.3 g/dl Resistant strain AJ11345 3.7 The cultured solution was treated in the same manner as in Example 1 to obtain 21.5 g of L-arginine crystals. Example 3 Glucose 10g/dl, ammonium sulfate 6g/dl
dl, KH 2 PO 4 0.1g/dl, MgSO 4・7H 2 O0.04g/
dl, FeSO 4・7H 2 O1mg/dl, MnSO 4・4H 2 O1mg/
dl, biotin 50μg/, thiamine hydrochloride 20μ
g/, soy protein decomposition solution (total nitrogen 2.4%) 1 mg/
dl, calcium carbonate 5g/dl (separate sterilization added), PH7.0
A culture medium adjusted to the following conditions was prepared, and 20 ml of the medium was dispensed into a 500 ml shoulder flask. After sterilization, Corynebacterium acetoacidophyllum AJ11340 (SD r + Argininol r ), which had been grown in advance on a bouillon slant, was inoculated and cultured with shaking at 31°C for 72 hours.
The amount of arginine produced and accumulated was as follows. Parent strain AJ3278 1.70 g/dl Resistant strain AJ11340 1.95 The cultured solution was treated in the same manner as in Example 1 to obtain 12.7 g of L-arginine crystals.

Claims (1)

【特許請求の範囲】[Claims] 1 ブレビバクテリウム属又はコリネバクテリウ
ム属のアルギニノールに耐性を有し、かつL−ア
ルギニン生産能を有する微生物を培地に培養し、
培地中に生成蓄積したL−アルギニンを採取する
ことを特徴とする微生物によるL−アルギニンの
製造法。
1. Cultivating a microorganism of the genus Brevibacterium or Corynebacterium that is resistant to argininol and has L-arginine production ability,
A method for producing L-arginine using a microorganism, which comprises collecting L-arginine produced and accumulated in a culture medium.
JP5342179A 1979-05-02 1979-05-02 Preparation of l-arginine Granted JPS55148093A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5342179A JPS55148093A (en) 1979-05-02 1979-05-02 Preparation of l-arginine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5342179A JPS55148093A (en) 1979-05-02 1979-05-02 Preparation of l-arginine

Publications (2)

Publication Number Publication Date
JPS55148093A JPS55148093A (en) 1980-11-18
JPS6224075B2 true JPS6224075B2 (en) 1987-05-26

Family

ID=12942369

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5342179A Granted JPS55148093A (en) 1979-05-02 1979-05-02 Preparation of l-arginine

Country Status (1)

Country Link
JP (1) JPS55148093A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014185430A1 (en) 2013-05-13 2014-11-20 味の素株式会社 Method for manufacturing l-amino acid

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0728749B2 (en) * 1986-09-22 1995-04-05 協和醗酵工業株式会社 Method for producing L-arginine
JP5247120B2 (en) * 2007-11-02 2013-07-24 雪印メグミルク株式会社 Method for producing L-ornithine-containing material

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5137348A (en) * 1974-09-24 1976-03-29 Japan Electronic Control Syst

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5137348A (en) * 1974-09-24 1976-03-29 Japan Electronic Control Syst

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014185430A1 (en) 2013-05-13 2014-11-20 味の素株式会社 Method for manufacturing l-amino acid

Also Published As

Publication number Publication date
JPS55148093A (en) 1980-11-18

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