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JPH0527388B2 - - Google Patents

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Publication number
JPH0527388B2
JPH0527388B2 JP11033884A JP11033884A JPH0527388B2 JP H0527388 B2 JPH0527388 B2 JP H0527388B2 JP 11033884 A JP11033884 A JP 11033884A JP 11033884 A JP11033884 A JP 11033884A JP H0527388 B2 JPH0527388 B2 JP H0527388B2
Authority
JP
Japan
Prior art keywords
arginine
medium
resistance
ahv
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 - Lifetime
Application number
JP11033884A
Other languages
Japanese (ja)
Other versions
JPS60251893A (en
Inventor
Takayasu Tsuchida
Yoshitaka Nishimoto
Hiroshi Sonoda
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 JP11033884A priority Critical patent/JPS60251893A/en
Publication of JPS60251893A publication Critical patent/JPS60251893A/en
Publication of JPH0527388B2 publication Critical patent/JPH0527388B2/ja
Granted legal-status Critical Current

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  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Description

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

〔産業上の利用分野〕 L−アルギニンは肝機能促進薬、アミノ酸輸液
及び総合アミノ酸製剤等の重要な成分である。本
発明はこのL−アルギニンを発酵法で製造する方
法を改良するものである。 〔従来技術〕 ブレビバクテリウム属及びコリネバクテリウム
属の微生物がL−アルギニン生産能を有するため
には、2−チアゾールアラニン(以下2−TAと
略す。)、アルギニンヒドロキサメート等への耐性
を付与せしめれば良いことがわかつている。更
に、前記の薬剤耐性に加えてサルフア剤、アルギ
ノール耐性又は8−アザグアニン等の薬剤に耐性
を付与すること、及びL−ヒスチジン、L−プロ
リン、L−スレオニン、L−トリプトフアン又は
L−リジン等のアミノ酸に対する要求性を付与す
ることによりL−アルギニンの生産能が向上する
ことは知られている。 〔発明が解説しようとする問題点〕 L−アルギニンの製造コストを低下させるため
に発酵収率を向上させることは重要な問題であ
る。 〔問題点を解決するための手段〕 本発明は上記問題点を解決するためになされた
ものであり、従来より知られているブレビバクテ
リウム属及びコリネバクテリウム属に属するL−
アルギニン生産能を有する微生物を改良して更に
発酵収率の向上した菌株を見いだすべく研究した
結果、α−アミノ−β−ヒドロキシ吉草酸(以下
AHVと略す。)に耐性を付与した菌株の中に、
従来のL−アルギニン生産菌よりも高収率でL−
アルギニンを生産する菌株が存在することを発見
した。 即ち、本発明は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、AHV耐性を有し、且
つL−アルギニン生産能を有する微生物を液体培
地中で培養し、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L−アルギニ
ンの製造法に関する。 本発明において用いられる微生物はブレビバク
テリウム属又はコリネバクテリウム属に属し、
AHV耐性を有し、かつL−アルギニン生産能を
有する変異株である。本発明の変異株を得るに
は、下記の野生株に、先にL−アルギニン生産能
を付与し、次いでAHV耐性を付与して良いし、
又先にAHV耐性を付与し、次いでL−アルギニ
ン生産能を付与しても良い。 本変異株の親株となる野性株は、ブレビバクテ
リウム属又はコリネバクテリウム属の特にコリネ
ホルムL−グルタミン酸生産性細菌として知られ
ているものであり、例えば、以下のものがある。
[Industrial Application Fields] L-arginine is an important component of liver function promoters, amino acid infusions, comprehensive amino acid preparations, and the like. The present invention improves the method for producing L-arginine by fermentation. [Prior Art] In order for microorganisms of the genus Brevibacterium and Corynebacterium to have the ability to produce L-arginine, they must have resistance to 2-thiazolealanine (hereinafter abbreviated as 2-TA), arginine hydroxamate, etc. I know that it would be better if I let them be granted. Furthermore, in addition to the above-mentioned drug resistance, it is possible to impart resistance to drugs such as sulfur drugs, arginol resistance, or 8-azaguanine, and to impart resistance to drugs such as L-histidine, L-proline, L-threonine, L-tryptophan, or L-lysine. It is known that the ability to produce L-arginine is improved by imparting requirements for amino acids. [Problems to be Explained by the Invention] It is an important problem to improve the fermentation yield in order to reduce the production cost of L-arginine. [Means for Solving the Problems] The present invention has been made to solve the above-mentioned problems, and is aimed at solving the problems described above.
As a result of research to improve microorganisms capable of producing arginine and find strains with even higher fermentation yields, we found that α-amino-β-hydroxyvaleric acid (hereinafter referred to as α-amino-β-hydroxyvaleric acid)
Abbreviated as AHV. ) among the strains that have conferred resistance to
L-arginine production with higher yield than conventional L-arginine producing bacteria
They discovered that there are strains of bacteria that produce arginine. That is, the present invention cultivates a microorganism belonging to the Brevibacterium genus or Corynebacterium genus and having AHV resistance and L-arginine production ability in a liquid medium, and L-arginine produced and accumulated in the medium. The present invention relates to a method for producing L-arginine, which comprises collecting L-arginine. The microorganism used in the present invention belongs to the genus Brevibacterium or Corynebacterium,
This is a mutant strain that is resistant to AHV and has the ability to produce L-arginine. To obtain the mutant strain of the present invention, the following wild strain may be first endowed with L-arginine production ability, and then AHV resistance may be imparted,
Alternatively, AHV resistance may be imparted first, and then L-arginine production ability may be imparted. The wild strain that serves as the parent strain of this mutant strain is a bacterium of the genus Brevibacterium or Corynebacterium that is particularly known as a coryneform L-glutamic acid-producing bacterium, and includes, for example, the following.

〔変異誘導法〕[Mutation induction method]

ブイヨン寒天スラント上に30℃で24時間生育さ
れたブレビバクテリウム・フラバム
AJ11169FERM−P4161(ATCC14067より誘導し
た2−TA耐性株)及びコリネバクテリウム・グ
ルメミクムAJ12092FERM−P7273(ATCC13032
より誘導した2−TA耐性株)の菌体をM/30リ
ン酸緩衝液に懸濁し菌体濃度108〜109/mlの菌体
懸濁液に500μg/mlのN−メチル−N′−ニトロ
−N−ニトロソグアニジンを加え30℃に20分間保
持した。ついで遠心分離して菌体を集め、1/30M
リン酸緩衝液で良く洗滌した後、下記組成の培地
に接種し、31.5℃で4〜10日間培養した。 培地組成(PH7.0)成 分 含量 グルコース 1.0g/dl 尿 素 0.2 〃 KH2PO4 0.1 〃 MgSO4・7H2O 0.1 〃 FeSO4・7H2O 0.002 〃 MnSO4・7H2O 0.002 〃 ビオチン 100μg/ サイアミン塩酸塩 100μg/ AHV 0.1g/dl 寒 天 2.0 〃 寒天培地に生育した菌株の中から、L−アルギ
ニン生産能の高い菌株としてブレビバクテリウ
ム・フラバムAJ12144FERM−P7642(2−TA耐
性、AHV耐性)及びコリネバクテリウム・グル
タミクムAJ12145FERM−P7643(2−TA耐性、
AHV耐性)を得た。 このようにして得られた変異株のAHV耐性度
を親株として比較した。 グルコース0.5g/dl、尿素0.15g/dl、硫安
0.15g/dl、KH2PO40.3g/dl、K2HPO40.1
g/dl、MgSO4・7H2O0.01g/dl、CaCl2
2H2O0.1mg/dl、ビオチン100μg/、サイアミ
ン塩酸塩100μg/、FeSO4・7H2O0.002g/
dl、MnSO4・7H2O0.002g/dlおよび表に示す
量のAHVを含み、PH7.0に調節した培地に、天然
培地(ペプトン1g/dl、酵母エキス1g/dl、
NaCl0.5g/dl、PH7.0)スラントで24時間培養し
た菌体を殺菌水に懸濁して接種し、24時間培養し
て生育度を濁度で測定した。
Brevibacterium flavum grown on broth agar slants at 30°C for 24 hours.
AJ11169FERM-P4161 (2-TA resistant strain derived from ATCC14067) and Corynebacterium grumemicum AJ12092FERM-P7273 (ATCC13032
2-TA resistant strain) was suspended in M/30 phosphate buffer, and 500 μg/ml of N-methyl-N' was added to the cell suspension with a cell concentration of 10 8 to 10 9 /ml. -Nitro-N-nitrosoguanidine was added and kept at 30°C for 20 minutes. Then, centrifuge to collect the bacterial cells, 1/30M
After thorough washing with phosphate buffer, the cells were inoculated into a medium with the following composition and cultured at 31.5°C for 4 to 10 days. Medium composition (PH7.0) Component content Glucose 1.0g/dl Urea 0.2 KH 2 PO 4 0.1 〃 MgSO 4・7H 2 O 0.1 〃 FeSO 4・7H 2 O 0.002 〃 MnSO 4・7H 2 O 0.002 〃 Biotin 100μg/thiamine hydrochloride 100μg/AHV 0.1g/dl Agar 2.0 Among the strains grown on agar medium, Brevibacterium flavum AJ12144FERM-P7642 (2-TA resistant, AHV resistant) and Corynebacterium glutamicum AJ12145FERM-P7643 (2-TA resistant,
AHV resistance) was obtained. The AHV resistance of the thus obtained mutant strain was compared with that of the parent strain. Glucose 0.5g/dl, urea 0.15g/dl, ammonium sulfate
0.15g/dl, KH 2 PO 4 0.3g/dl, K 2 HPO 4 0.1
g/dl, MgSO 4・7H 2 O0.01g/dl, CaCl 2
2H 2 O 0.1mg/dl, biotin 100μg/, thiamine hydrochloride 100μg/, FeSO 4・7H 2 O 0.002g/
Natural medium (peptone 1 g/dl, yeast extract 1 g /dl,
(NaCl 0.5 g/dl, PH 7.0) Bacterial cells cultured in a slant for 24 hours were suspended in sterilized water and inoculated, cultured for 24 hours, and the growth rate was measured by turbidity.

【表】【table】

〔作用〕[Effect]

このような変異株を培養する際に用いる培地
は、炭素源、窒素源、無機イオン、上記要求性を
満足させるべき物質及び必要に応じビタミン等そ
の他の有機微量栄養素を含有する通常の培地であ
る。 炭素源としてはグルコース、シユクロース等の
炭水化物、酢酸等の有機酸等が、窒素源としては
アンモニア水、アンモニアガス、アンモニウム塩
等が好適である。無機イオンとしてはカリイオ
ン、ナトリウムイオン、マグネシウムイオン、リ
ン酸イオンその他が必要に応じ適宜培地に添加さ
れる。 培養は好気的条件が望ましく、培養の間培地の
PHを4ないし8に温度を25℃ないし37℃に調節し
つつ行えばより好ましい結果が得られる。かくし
て1ないし7日間も培養すれば培地中に著量のL
−アルギニンが生成蓄積される。 培養液よりL−アルギニンを採取する方法は、
イオン交換樹脂による方法等通常の方法で採取で
きる。 以下実施例にて説明する。 実施例 グルコース10g/dl、(NH42SO47g/dl、
KH2PO40.1g/dl、MgSO47H2O0.04g/dl、
FeSO47H2O1mg/dl、MnSO4・4H2O1mg/dl、
サイアミン・HCl100μg/、ビオチン100μg/
、大豆蛋白酸加水分解液60mg/dl(全窒素とし
て)炭酸カルシウム5g/dl(別殺菌)を含む培
地をPH7.0に調節し、その20mlを500ml容肩付フラ
スコに入れ加熱殺菌した。これに第1表に示す菌
株を一白金耳接種し、31.5℃に保ちつつ4日間振
盪した。各菌株の培養液中には第2表に示す量の
L−アルギニンがそれぞれ生成蓄積していた。
The medium used for culturing such mutant strains is a normal medium containing a carbon source, a nitrogen source, inorganic ions, substances that should satisfy the above-mentioned requirements, and other organic micronutrients such as vitamins as necessary. . Preferred carbon sources include carbohydrates such as glucose and sucrose, organic acids such as acetic acid, and preferred nitrogen sources include aqueous ammonia, ammonia gas, and ammonium salts. As inorganic ions, potassium ions, sodium ions, magnesium ions, phosphate ions, and others are appropriately added to the medium as necessary. It is preferable to culture under aerobic conditions, and the culture medium should be
More favorable results can be obtained by controlling the pH to 4 to 8 and the temperature to 25 to 37°C. Thus, if the culture is continued for 1 to 7 days, a significant amount of L will be present in the medium.
- Arginine is produced and accumulated. The method for collecting L-arginine from the culture solution is as follows:
It can be collected using conventional methods such as using ion exchange resin. This will be explained below using examples. Example Glucose 10g/dl, (NH 4 ) 2 SO 4 7g/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,
Thiamine/HCl 100μg/, biotin 100μg/
A medium containing 60 mg/dl of soybean protein acid hydrolyzate (as total nitrogen) and 5 g/dl of calcium carbonate (separately sterilized) was adjusted to pH 7.0, and 20 ml of it was placed in a 500 ml shoulder flask and sterilized by heating. A loopful of the bacterial strains shown in Table 1 was inoculated into this, and the mixture was shaken for 4 days while being kept at 31.5°C. In the culture solution of each strain, L-arginine was produced and accumulated in the amounts shown in Table 2.

【表】 AJ12144を上記の方法で培養して培養液1を
得、これより遠心分離にて菌体他を除き、上清を
弱酸性イオン交換樹脂「アンバーライト」C−50
(NH4 +型)に通過させた。樹脂を水洗後、2N
NH4OHにてL−アルギニンを溶出し、ついで溶
出液を濃縮し、これよりL−アルギニンの粗結晶
24.0gを得た。
[Table] AJ12144 was cultured using the above method to obtain culture solution 1, which was centrifuged to remove bacterial cells and the supernatant was collected using weakly acidic ion exchange resin "Amberlite" C-50.
(NH 4 + form). After washing the resin with water, 2N
L-arginine was eluted with NH 4 OH, the eluate was concentrated, and crude crystals of L-arginine were obtained.
24.0g was obtained.

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
ム属に属しα−アミノ−β−ヒドロキシ吉草酸耐
性を有し、且つL−アルギニン生産能を有する微
生物を液体培地中で培養し、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
L−アルギニンの製造法。
1 A microorganism belonging to the genus Brevibacterium or Corynebacterium and having resistance to α-amino-β-hydroxyvaleric acid and capable of producing L-arginine was cultured in a liquid medium, and produced and accumulated in the medium. A method for producing L-arginine, which comprises collecting L-arginine.
JP11033884A 1984-05-30 1984-05-30 Preparation of l-arginine by fermentation method Granted JPS60251893A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11033884A JPS60251893A (en) 1984-05-30 1984-05-30 Preparation of l-arginine by fermentation method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11033884A JPS60251893A (en) 1984-05-30 1984-05-30 Preparation of l-arginine by fermentation method

Publications (2)

Publication Number Publication Date
JPS60251893A JPS60251893A (en) 1985-12-12
JPH0527388B2 true JPH0527388B2 (en) 1993-04-21

Family

ID=14533220

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11033884A Granted JPS60251893A (en) 1984-05-30 1984-05-30 Preparation of l-arginine by fermentation method

Country Status (1)

Country Link
JP (1) JPS60251893A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2578468B2 (en) * 1988-04-07 1997-02-05 協和醗酵工業株式会社 Method for producing L-arginine by fermentation

Also Published As

Publication number Publication date
JPS60251893A (en) 1985-12-12

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