JPS62195293A - Production of l-isoleucine by fermentation method - Google Patents

Production of l-isoleucine by fermentation method

Info

Publication number
JPS62195293A
JPS62195293A JP3800686A JP3800686A JPS62195293A JP S62195293 A JPS62195293 A JP S62195293A JP 3800686 A JP3800686 A JP 3800686A JP 3800686 A JP3800686 A JP 3800686A JP S62195293 A JPS62195293 A JP S62195293A
Authority
JP
Japan
Prior art keywords
isoleucine
glutamic acid
culture
threoninehydroxamate
resistant
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.)
Granted
Application number
JP3800686A
Other languages
Japanese (ja)
Other versions
JPH0555113B2 (en
Inventor
Rei Furukawa
令 古川
Akio Ozaki
尾崎 明夫
Toshihide Nakanishi
中西 俊秀
Masahiro Sugimoto
杉本 正裕
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.)
KH Neochem Co Ltd
Original Assignee
Kyowa Hakko Kogyo Co Ltd
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 Kyowa Hakko Kogyo Co Ltd filed Critical Kyowa Hakko Kogyo Co Ltd
Priority to JP3800686A priority Critical patent/JPS62195293A/en
Publication of JPS62195293A publication Critical patent/JPS62195293A/en
Publication of JPH0555113B2 publication Critical patent/JPH0555113B2/ja
Granted legal-status Critical Current

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Abstract

PURPOSE:To obtain L-isoleucine in high yield inexpensively, by using a bacterium belonging to coryneform glutamic acid-forming mold, showing resistance to threoninehydroxamate, capable of producing L-isoleucine. CONSTITUTION:A strain having resistance to threoninehydroxamate can be obtained as a mold growing in an agar medium containing >=1g/l threoninehydroxamate by varying a coryneform glutamic acid-forming mold (a group of glutamic acid-forming mold belonging to the genus Corynebacterium, Brevibacterium, Microbacterium or Arthrobacter) by an ordinary variation means. Corynebacterium glutamicum H-4260 may be cited as the preferable example. It is cultivated in a medium containing a carbon source, a nitrogen source, an inorganic salt, etc., L-isoleucine is accumulated in a culture mixture and collected.

Description

【発明の詳細な説明】 産業上の利用分野 本発明はスレオニンハイドロキサメートに耐性を示し、
L−イソロイシン生産能を有するコリネ型グルタミン酸
生産菌に属する微生物を用いるL−イソロイシンの製造
法に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention exhibits resistance to threonine hydroxamate;
The present invention relates to a method for producing L-isoleucine using a microorganism belonging to coryneform glutamic acid-producing bacteria having the ability to produce L-isoleucine.

L−イソロイシンは、アミノ酸製剤として医薬品産業な
どの分野に利用される。
L-isoleucine is used in fields such as the pharmaceutical industry as an amino acid preparation.

従来の技術 従来、発酵法によるL−イソロイシンの製造法としては
、ミクロコツカス・グルタミクスに属し、スレオニン、
メチオニン、ホモセリンまたはロイシン要求性を有する
微生物を用いる方法(特公昭38−7091号公報)、
ブレビバクテリウム・フラバムに属し、α−アミノ−β
−ヒドロキシ吉草酸耐性およびアデニンまたはリジン要
求性を有する微生物を用いる方法(特公昭51−623
7号公報)、α−アミノ−β−ヒドロキシ吉草酸および
○−メチルスレオニン耐性を有する微生物を用いる方法
(特公昭51−21077号公報)、ブレビバクテリウ
ム属また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で、かつエチオニン、2−チ
アゾールアラニンおよびS−(2−アミノエチル)−L
−システィンのうち少なくとも1つに耐性を有する微生
物を用いる方法(特開昭50−101582号公報)、
コリネバクテリウム属に属し、イソロイシンアナログ耐
性で、かつメチオニンまたはリジン要求性を有する微生
物を用いる方法(特公昭54−32070号公報)、コ
リネバクテリウム属に属し、ビタミン−P耐性を有する
微生物を用いる方法(特開昭57−2687号公報)、
コリネバクテリウム属に属し、アルギニン要求性を有す
る微生物を用いる方法(特開昭59−106295号公
報)、コリネバクテリウム属に属し、フルオロピルビン
酸感受性を有する微生物を用いる方法(特開昭59−1
06294号公報)などが知られている。
Conventional technology Conventionally, as a method for producing L-isoleucine by a fermentation method, L-isoleucine belonging to Micrococcus glutamicus, threonine,
A method using microorganisms having auxotrophy for methionine, homoserine or leucine (Japanese Patent Publication No. 38-7091),
Belongs to Brevibacterium flavum, α-amino-β
- Method using microorganisms having hydroxyvaleric acid resistance and adenine or lysine auxotrophy (Japanese Patent Publication No. 51-623
7), a method using a microorganism resistant to α-amino-β-hydroxyvaleric acid and ○-methylthreonine (Japanese Patent Publication No. 51-21077), which belongs to the genus Brevibacterium or the genus Corynebacterium, Amino
β-hydroxyvaleric acid resistant and ethionine, 2-thiazolealanine and S-(2-aminoethyl)-L
- A method using a microorganism resistant to at least one of cysteine (Japanese Patent Application Laid-Open No. 101582/1982),
A method using a microorganism that belongs to the genus Corynebacterium and is resistant to isoleucine analogs and has a methionine or lysine auxotrophy (Japanese Patent Publication No. 1983-32070); A method that uses a microorganism that belongs to the genus Corynebacterium and has vitamin-P resistance Method (Japanese Unexamined Patent Publication No. 57-2687),
A method using a microorganism belonging to the genus Corynebacterium and having an arginine auxotrophy (JP-A-59-106295), a method using a microorganism belonging to the genus Corynebacterium and having fluoropyruvate sensitivity (JP-A-59-1989) 1
No. 06294) and the like are known.

発明が解決しようとする問題点 アミノ酸製剤として有用なL−イソロイシンを、より収
率よく安価に製造する方法が求められている。
Problems to be Solved by the Invention There is a need for a method for producing L-isoleucine, which is useful as an amino acid preparation, with higher yield and at lower cost.

問題点を解決するための手段 本発明者は、L−イソロイシンを収率よく安価に製造す
るためにより優れたL−イソロイシン生産菌の研究を行
った。その結果、スレオニンハイドロキサメートに耐性
を示し、L−イソロイシン生産能を有するコリネ型グル
タミン酸生産菌に属する微生物を用いると、収率よくL
−イソロイシンを得ることができることを見出し、本発
明を完成した。
Means for Solving the Problems The present inventor conducted research on better L-isoleucine producing bacteria in order to produce L-isoleucine with high yield and at low cost. As a result, when using a microorganism belonging to the coryneform glutamate-producing bacteria that is resistant to threonine hydroxamate and has the ability to produce L-isoleucine, L-isoleucine can be produced with good yield.
- It was discovered that isoleucine could be obtained, and the present invention was completed.

以下に本発明の詳細な説明する。The present invention will be explained in detail below.

本発明は、コリネ型グルタミン酸生産菌に属し、スレオ
ニンハイドロキサメートに耐性を示し、かつL−イソロ
イシン生産能を有する微生物を培地に培養し、培養物中
にL−イソロイシンを生成蓄積させ、該培養物よりL−
イソロイシンを採取することを特徴とする発酵法による
L−イソロイシンの製造法を提供する。
The present invention involves culturing a microorganism belonging to coryneform glutamate-producing bacteria, showing resistance to threonine hydroxamate, and having an ability to produce L-isoleucine in a medium, producing and accumulating L-isoleucine in the culture, and culturing the microorganism in a medium. L- than things
Provided is a method for producing L-isoleucine by a fermentation method characterized by collecting isoleucine.

本発明に使用する微生物の例としては、コリネ型グルタ
ミン酸生産菌に属し、スレオニンハイドロキサメートに
耐性を示し、かつL−イソロイシン生産能を有する微生
物であればいずれも用いることができる。スレオニンハ
イドロキサメートに耐性の菌株は、コリネ型グルタミン
酸生産菌を通常の変異手段により変異させ、スレオニン
ハイドロキサメートを1g/(2以上含有する寒天培地
上で生育してくる菌として得ることができる。好適な例
としては、コリネバクテリウム・グルタミクムH−42
60をあげることができる。
As an example of the microorganism used in the present invention, any microorganism that belongs to the coryneform glutamic acid-producing bacteria, exhibits resistance to threonine hydroxamate, and has the ability to produce L-isoleucine can be used. A strain resistant to threonine hydroxamate can be obtained by mutating a coryneform glutamate-producing bacterium by conventional mutation methods and growing on an agar medium containing 1 g/(2 or more) of threonine hydroxamate. A suitable example is Corynebacterium glutamicum H-42.
I can give you 60.

本明細書において、コリネ型グルタミン酸生産菌とは、
コリネバクテリウム属、ブレビバクテリウム属、ミクロ
バクテリウム属またはアースロバフタ−属に属する一群
のグルタミン酸生産菌をいう〔「発酵と工業」第40巻
、102.1982年参照〕。
As used herein, coryneform glutamate-producing bacteria are
A group of glutamic acid-producing bacteria belonging to the genus Corynebacterium, Brevibacterium, Microbacterium, or Arthrobacterium [see "Fermentation and Industry" Vol. 40, 102, 1982].

以下に、上記のスレオニンハイドロキサメート耐性株の
取得方法の具体例を示す。
A specific example of the method for obtaining the above-mentioned threonine hydroxamate-resistant strain is shown below.

コリネバクテリウム・グルタミン酸ムH−3501〔ア
ルギニン要求性、S−(2−アミノエチル)−L−シス
ティン耐性、リファンピシン耐性、フルオロピルビン酸
感受性、本菌株は昭和60年7月16日付で工業技術院
微生物工業技術研究所(以下微工研という)にFERM
  BP−848として寄託されている。〕を〕N−メ
チルーN′〜ニトローN−二トロソグアニジンNTG)
による変異処理(200x/ml、 30℃、30分間
)した後、以下に示す最少寒天培地に2g/βのスレオ
ニンハイドロキサメートを添加した培地で生育しつるよ
うな菌株を採取することにより行うことができる。得ら
れたスレオニンハイドロキサメート耐性株50株をL−
イソロイシンの生産試験(実施例の方法)にかけ、親株
よりL−イソロイシン生産性が著しくすぐれた菌株を選
んだ。そのうちの1株がコリネバクテリウム・グルタミ
クムH−4260(アルギニン要求性、5−(2−アミ
ノエチルiL−システィン耐性、リファンピシン耐性、
フルオロピルビン酸感受性、スレオニンハイドロキサメ
ート耐性〕である。
Corynebacterium glutamate H-3501 [arginine auxotrophic, S-(2-aminoethyl)-L-cysteine resistant, rifampicin resistant, fluoropyruvate sensitive, this strain was approved by the Agency of Industrial Science and Technology on July 16, 1985. FERM to the Microbial Technology Research Institute (hereinafter referred to as FERM)
It has been deposited as BP-848. ] N-methyl-N' ~ nitro N-nitrosoguanidine NTG)
After mutagenesis treatment (200x/ml, 30°C, 30 minutes), collect a strain that grows and vines on the following minimal agar medium supplemented with 2g/β threonine hydroxamate. I can do it. The obtained 50 threonine hydroxamate resistant strains were transformed into L-
A strain was selected which was subjected to an isoleucine production test (method in the example) and had significantly better L-isoleucine productivity than the parent strain. One of the strains was Corynebacterium glutamicum H-4260 (arginine auxotrophy, 5-(2-aminoethyl iL-cysteine resistant, rifampicin resistant,
Sensitive to fluoropyruvate, resistant to threonine hydroxamate].

本菌株は昭和61年2月13日付で微工研にFERM 
 BP−986として寄託されている。
This strain was FERMed to the Microtech Institute on February 13, 1986.
It has been deposited as BP-986.

培地組成ニゲルコース0.5%、(NH4)2S0゜0
.15%、K H2P O* 0.15%、K2HP0
゜0.05%、NaCJ!  0.01%、Mg5C)
s  ・7H200,05%、CaC#z’2HzO1
x/m15MnCl1z・4H207xr/ml、Fe
50<  1H2010g/m+、チアミン塩酸塩Q、
lB/ml、ビオチンQ、 03■/ml 、アルギニ
ン塩酸塩0.01%、寒天1.5%、pH7,2上記微
生物を炭素源、窒素源、無機塩類、生育因子などを含有
する合成培地または天然培地を用いて培養することによ
りL−イソロイシンを培養物中に蓄積させ、これを採取
することによりL−イソロイシンを製造することができ
る。
Medium composition Nigelcose 0.5%, (NH4)2S0゜0
.. 15%, K H2P O* 0.15%, K2HP0
゜0.05%, NaCJ! 0.01%, Mg5C)
s ・7H200,05%, CaC#z'2HzO1
x/m15MnCl1z・4H207xr/ml, Fe
50<1H2010g/m+, thiamine hydrochloride Q,
1B/ml, biotin Q, 03■/ml, arginine hydrochloride 0.01%, agar 1.5%, pH 7.2 The above microorganisms were placed in a synthetic medium containing carbon sources, nitrogen sources, inorganic salts, growth factors, etc. L-isoleucine can be produced by accumulating L-isoleucine in the culture by culturing in a natural medium and collecting it.

炭素源としては、グルコース、シュークロース、糖蜜、
デンプン加水分解物などの糖類、酢酸、プロピオン酸、
ギ酸、フマール酸、リンゴ酸などの有機酸類、メタノー
ル、エタノール、プロパツールなどのアルコール類、炭
化水素などが使用できる。
Carbon sources include glucose, sucrose, molasses,
Sugars such as starch hydrolysates, acetic acid, propionic acid,
Organic acids such as formic acid, fumaric acid, and malic acid, alcohols such as methanol, ethanol, and propatool, and hydrocarbons can be used.

窒素源としては硫酸アンモニウム、硝酸アンモニウム、
塩化アンモニウム、リン酸アンモニウム、尿素、アンモ
ニアなどが使用できる。また、栄養要求性を示す変異株
の場合には、栄養物質を純品として、または、それらを
含有する天然栄養物の形で添加することができる。
Nitrogen sources include ammonium sulfate, ammonium nitrate,
Ammonium chloride, ammonium phosphate, urea, ammonia, etc. can be used. Furthermore, in the case of mutant strains exhibiting auxotrophy, nutritional substances can be added as pure products or in the form of natural nutrients containing them.

培養は振盪培養あるいは深部通気攪拌培養などの好気的
条件下で行う。培養温度は通常24〜37℃、好ましく
は28〜32℃の範囲で、培地のpHは5〜9の範囲、
好ましくは中性付近に保持することが望ましい。培地の
pH調節は、炭酸カルシウム、無機又は有機の酸、アル
カリ溶液、尿素、炭酸カルシウム、アンモニアガスなど
によって行う。
Cultivation is performed under aerobic conditions such as shaking culture or deep aeration agitation culture. The culture temperature is usually in the range of 24 to 37°C, preferably 28 to 32°C, and the pH of the medium is in the range of 5 to 9.
It is desirable to maintain the temperature near neutrality. The pH of the medium is adjusted using calcium carbonate, an inorganic or organic acid, an alkaline solution, urea, calcium carbonate, ammonia gas, or the like.

培養期間は通常2〜7日間で培養物中にL−イソロイシ
ンが生成蓄積する。
The culture period is usually 2 to 7 days, and L-isoleucine is produced and accumulated in the culture.

培養終了後、培養液から菌体などの沈殿物を除去し、イ
オン交換処理法、濃縮法、吸着法、塩析法などを併用す
ることにより、培養液からL−イソロイシンを回収する
ことができる。
After culturing, L-isoleucine can be recovered from the culture solution by removing precipitates such as bacterial cells from the culture solution and using ion exchange treatment, concentration method, adsorption method, salting out method, etc. .

以下に実施例を示す。Examples are shown below.

実施例1 コリネバクテリウム・グルタミクムH−4260〔アル
ギニン要求性、5−(2−アミノエチル)−L−システ
ィン耐性、フルオロピルビン酸感受性、リファンピシン
耐性、スレオニンハイドロキサメート耐性〕 (FER
M  BP  986)を23m1の種培地(グルコー
ス5%、酵母エキス1%、ペプトン1%、尿素0.3%
、NaC10,25%、コーン・スチープ・リカー0.
5%、ビオチン50ttx/l、pH7,2)を含む3
00ml容三角フラスコに接種し、28℃で24時間、
21Orpmのロータリーシェーカー上で振とう培養し
た。
Example 1 Corynebacterium glutamicum H-4260 [arginine auxotrophy, 5-(2-aminoethyl)-L-cysteine resistance, fluoropyruvate sensitivity, rifampicin resistance, threonine hydroxamate resistance] (FER
M BP 986) in 23 ml of seed medium (glucose 5%, yeast extract 1%, peptone 1%, urea 0.3%).
, NaC 10.25%, Corn Steep Liquor 0.
5%, biotin 50ttx/l, pH 7,2)
Inoculated into a 00ml Erlenmeyer flask and incubated at 28°C for 24 hours.
Shaking culture was performed on a rotary shaker at 21 rpm.

この種培養液2mlを20m1の発酵培地を含む300
m1容三角フラスコに接種して72時間、種培養と同様
の方法で培養した。培養終了後の培養液中のL−イソロ
イシン蓄積量は、13.4g/#であった。対照とした
親株H−3501株〔アルギニン要求性、S−(2−ア
ミノエチル)−L−システィン耐性、フルオロピルビン
酸感受性、リファンピシン耐性〕を用いて同様に培養し
た結果、L〜インロイシンの蓄積量は、11.6g/f
fであった。
300ml of this seed culture containing 20ml of fermentation medium
It was inoculated into a 1 m Erlenmeyer flask and cultured for 72 hours in the same manner as the seed culture. The amount of L-isoleucine accumulated in the culture solution after completion of the culture was 13.4 g/#. As a result of culturing in the same manner using the parent strain H-3501 [arginine auxotrophic, S-(2-aminoethyl)-L-cysteine resistant, fluoropyruvate sensitive, rifampicin resistant] as a control, L-inleucine accumulation was observed. The amount is 11.6g/f
It was f.

発酵培地の組成は次のとおり。The composition of the fermentation medium is as follows.

廃ng<グルコース換3iE)70g/Cコーン・スチ
ープ・リカー5g/L塩化アンモニウム20g#、尿素
2g/j!、KH2PO12g/11Mg5O4−7H
200,5g/j2SFeSO4・7H200,01g
//、MnCj!2・4HzO0,01g#2、Cu5
O,・5H200,01g#、CaCff1z・2t(
to  O,OXg/l、ZnSO4・7H7H2O1
/n、N 1(1221mg/n、%リブデン酸アンモ
ン・4水塩1mg/I2、Co C(12・6HzO1
mg/f、パントテン酸カルシウム10mg/C二:+
チン酸1mg/#、ビオチン50■/1、アルギニン塩
酸塩0.5g/I2、p H7,4H−4260株を用
いて得たし一インロインン含有培養液200ffllを
遠心分離(3,00Orpm、10分)にかけ、菌体そ
の他の不純物を除いた。
Waste ng < glucose conversion 3iE) 70g/C corn steep liquor 5g/L ammonium chloride 20g#, urea 2g/j! , KH2PO12g/11Mg5O4-7H
200,5g/j2SFeSO4・7H200,01g
//, MnCj! 2.4HzO0.01g#2, Cu5
O,・5H200,01g#,CaCff1z・2t(
to O, OXg/l, ZnSO4・7H7H2O1
/n, N 1 (1221 mg/n, % Ammonium ribdate tetrahydrate 1 mg/I2, Co C (12.6 Hz O1
mg/f, calcium pantothenate 10 mg/C2:+
Tinic acid 1 mg/#, biotin 50 μ/1, arginine hydrochloride 0.5 g/I2, pH 7, 200 ffll of a culture solution containing linoin obtained using the 4H-4260 strain was centrifuged (3,00 rpm, 10 minutes). ) to remove bacterial cells and other impurities.

得られた上澄液を強酸性陽イオン交換樹脂ダイヤイオン
5KI(H”型)(三菱化成工業社製)のカラムに通し
、L−イソロイシンを吸着させ、水洗後、0.5規定の
アンモニア水で溶出してL−イソロイシン画分を集めた
。集めた画分を濃縮してpH6,02の等電点て晶出さ
せることにより、純度99%のし一イソロイシン1.4
gを得た。
The obtained supernatant liquid was passed through a column of strongly acidic cation exchange resin Diaion 5KI (H" type) (manufactured by Mitsubishi Chemical Industries, Ltd.) to adsorb L-isoleucine, and after washing with water, 0.5 N ammonia water was added. The L-isoleucine fraction was collected by elution.The collected fractions were concentrated and crystallized using an isoelectric point of pH 6.02 to obtain 99% pure L-isoleucine 1.4.
I got g.

発明の効果 本発明方法によれば、収率よくL−イソロイシンを得る
ことができる。
Effects of the Invention According to the method of the present invention, L-isoleucine can be obtained in good yield.

Claims (1)

【特許請求の範囲】[Claims] コリネ型グルタミン酸生産菌に属し、スレオニンハイド
ロキサメートに耐性を示し、かつL−イソロイシン生産
能を有する微生物を培地に培養し、培養物中にL−イソ
ロイシンを生成蓄積させ、該培養物よりL−イソロイシ
ンを採取することを特徴とする発酵法によるL−イソロ
イシンの製造法。
A microorganism belonging to the coryneform glutamate-producing bacteria, showing resistance to threonine hydroxamate, and having the ability to produce L-isoleucine is cultured in a medium, L-isoleucine is produced and accumulated in the culture, and L-isoleucine is produced and accumulated in the culture. A method for producing L-isoleucine by a fermentation method, characterized by collecting isoleucine.
JP3800686A 1986-02-22 1986-02-22 Production of l-isoleucine by fermentation method Granted JPS62195293A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3800686A JPS62195293A (en) 1986-02-22 1986-02-22 Production of l-isoleucine by fermentation method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3800686A JPS62195293A (en) 1986-02-22 1986-02-22 Production of l-isoleucine by fermentation method

Publications (2)

Publication Number Publication Date
JPS62195293A true JPS62195293A (en) 1987-08-28
JPH0555113B2 JPH0555113B2 (en) 1993-08-16

Family

ID=12513485

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3800686A Granted JPS62195293A (en) 1986-02-22 1986-02-22 Production of l-isoleucine by fermentation method

Country Status (1)

Country Link
JP (1) JPS62195293A (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008044409A1 (en) 2006-10-10 2008-04-17 Ajinomoto Co., Inc. Method for production of l-amino acid
WO2008075483A1 (en) 2006-12-19 2008-06-26 Ajinomoto Co., Inc. Process for production of l-amino acid
WO2008102572A1 (en) 2007-02-20 2008-08-28 Ajinomoto Co., Inc. Method for production of l-amino acid or nucleic acid
WO2009082028A2 (en) 2007-12-21 2009-07-02 Ajinomoto Co., Inc. Process for producing (2s,3r,4s)-4-hydroxy-l-isoleucine
WO2009088049A1 (en) 2008-01-10 2009-07-16 Ajinomoto Co., Inc. Method for production of desired substance by fermentation process
WO2009093703A1 (en) 2008-01-23 2009-07-30 Ajinomoto Co., Inc. Method of producing l-amino acid
WO2011013707A1 (en) 2009-07-29 2011-02-03 味の素株式会社 Method for producing l-amino acid
WO2014185430A1 (en) 2013-05-13 2014-11-20 味の素株式会社 Method for manufacturing l-amino acid
WO2015005406A1 (en) 2013-07-09 2015-01-15 味の素株式会社 Method for manufacturing useful substance
WO2015050234A1 (en) 2013-10-02 2015-04-09 味の素株式会社 Ammonia control apparatus and ammonia control method
WO2015060391A1 (en) 2013-10-23 2015-04-30 味の素株式会社 Method for producing target substance
EP3385389A1 (en) 2017-04-03 2018-10-10 Ajinomoto Co., Inc. Method for producing l-amino acid from fructose

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008044409A1 (en) 2006-10-10 2008-04-17 Ajinomoto Co., Inc. Method for production of l-amino acid
WO2008075483A1 (en) 2006-12-19 2008-06-26 Ajinomoto Co., Inc. Process for production of l-amino acid
WO2008102572A1 (en) 2007-02-20 2008-08-28 Ajinomoto Co., Inc. Method for production of l-amino acid or nucleic acid
WO2009082028A2 (en) 2007-12-21 2009-07-02 Ajinomoto Co., Inc. Process for producing (2s,3r,4s)-4-hydroxy-l-isoleucine
EP2749652A2 (en) 2008-01-10 2014-07-02 Ajinomoto Co., Inc. A method for producing a target substance by fermentation
WO2009088049A1 (en) 2008-01-10 2009-07-16 Ajinomoto Co., Inc. Method for production of desired substance by fermentation process
WO2009093703A1 (en) 2008-01-23 2009-07-30 Ajinomoto Co., Inc. Method of producing l-amino acid
WO2011013707A1 (en) 2009-07-29 2011-02-03 味の素株式会社 Method for producing l-amino acid
WO2014185430A1 (en) 2013-05-13 2014-11-20 味の素株式会社 Method for manufacturing l-amino acid
WO2015005406A1 (en) 2013-07-09 2015-01-15 味の素株式会社 Method for manufacturing useful substance
EP3521433A1 (en) 2013-07-09 2019-08-07 Ajinomoto Co., Inc. Process for producing l-glutamic acid
WO2015050234A1 (en) 2013-10-02 2015-04-09 味の素株式会社 Ammonia control apparatus and ammonia control method
WO2015060391A1 (en) 2013-10-23 2015-04-30 味の素株式会社 Method for producing target substance
EP3385389A1 (en) 2017-04-03 2018-10-10 Ajinomoto Co., Inc. Method for producing l-amino acid from fructose

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