[go: up one dir, main page]

JPH0349690A - Preparation of l-glutamic acid - Google Patents

Preparation of l-glutamic acid

Info

Publication number
JPH0349690A
JPH0349690A JP1186282A JP18628289A JPH0349690A JP H0349690 A JPH0349690 A JP H0349690A JP 1186282 A JP1186282 A JP 1186282A JP 18628289 A JP18628289 A JP 18628289A JP H0349690 A JPH0349690 A JP H0349690A
Authority
JP
Japan
Prior art keywords
glutamic acid
brevibacterium
microorganism
prepare
approximately
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
JP1186282A
Other languages
Japanese (ja)
Other versions
JP2817228B2 (en
Inventor
Takayasu Tsuchida
隆康 土田
Mitsuyoshi Seki
光義 関
Haruo Uchibori
内堀 治夫
Nobuki Kawashima
川島 伸樹
Hitoshi Ei
仁 江井
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 JP1186282A priority Critical patent/JP2817228B2/en
Priority to AU58745/90A priority patent/AU628598B2/en
Priority to KR1019900010782A priority patent/KR970009156B1/en
Priority to BR909003459A priority patent/BR9003459A/en
Priority to PE1990172305A priority patent/PE33790A1/en
Priority to MYPI90001193A priority patent/MY105945A/en
Priority to FR9009249A priority patent/FR2649993B1/en
Publication of JPH0349690A publication Critical patent/JPH0349690A/en
Priority to US07/830,530 priority patent/US5272067A/en
Application granted granted Critical
Publication of JP2817228B2 publication Critical patent/JP2817228B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P13/00Preparation of nitrogen-containing organic compounds
    • C12P13/04Alpha- or beta- amino acids
    • C12P13/14Glutamic acid; Glutamine

Landscapes

  • Organic Chemistry (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Zoology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Microbiology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Biotechnology (AREA)
  • Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Abstract

PURPOSE:To contrive to inexpensively prepare the subject compound in an improved yield by culturing a microorganism which belongs to the genus Brevibacterium, etc., resistant against prumycin (derivative) and having an activity to produce L-glutamic acid. CONSTITUTION:Brevibacterium lactofermentum stain ATCC 13869 is subjected to a mutation treatment with approximately 2000 mug/ml of nitrosoguanidine, etc., at approximately 0 deg.C for approximately 20min to prepare a prumycin- resistant Brevibacterium or Corynebacterium microorganism such as Brevibacterium lactofermentum strain AJ 12475. The microorganism is aerobically cultured in a medium containing waste syrup, urea, etc., and, if necessary, biotin action-suppressing substance such as penicillin at 24-37 deg.C at a pH of 6-9. The culture product is purified with an ion exchange resin, etc., to prepare L-glutamic acid.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 L−グルタミン酸は調味料及びアミノ酸輸液原料等の重
要なアミノ酸であり、本発明はこのLーグルタミン酸を
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又はコリネバクテリウム属の野性
株又は、グルタミン酸アナログ耐性株、ケトマロン酸及
びフルオロ酢酸等の呼吸阻害剤耐性株、エスクレチン耐
性株等を使用する方法が知られている。
[Detailed Description of the Invention] [Industrial Application Field] L-glutamic acid is an important amino acid for seasonings and raw materials for amino acid infusions, and the present invention improves the method for producing this L-glutamic acid by fermentation. It is. [Prior Art] Methods using wild strains of the genus Brevibacterium or Corynebacterium, strains resistant to glutamic acid analogs, strains resistant to respiratory inhibitors such as ketomalonic acid and fluoroacetic acid, strains resistant to esculetin, etc. are known.

(発明が解決しようとする問題点〕 L−グルタミン酸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にある。
(Problems to be Solved by the Invention) An object of the present invention is to improve the fermentation yield in order to reduce the manufacturing cost of L-glutamic acid.

〔問題点を解決するための手段〕[Means for solving problems]

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L−グルタミン酸の生産菌として知゛られ
るブレビバクテリウム属またはコリネバクテリウム属に
属する微生物に、プルマイシン又はその誘導体に耐性を
有する変異株を育種すると、L−グルタミン酸の収率が
向上する事を見出した。プルマイシンは、バチルス属細
菌が産生,する抗生物質として知られている。
The present invention was made to solve the above-mentioned problems, and it has been made to make microorganisms belonging to the genus Brevibacterium or Corynebacterium, which are conventionally known as L-glutamic acid producing bacteria, resistant to purmycin or derivatives thereof. It has been found that the yield of L-glutamic acid is improved by breeding a mutant strain having the following. Purmycin is known as an antibiotic produced by bacteria of the genus Bacillus.

本発明に使用するブレビバクテリウム属またはコリネバ
クテリウム属のプルマイシン、およびその誘導体に耐性
を有する菌株は、例えば以下の菌株がある。
Examples of strains of the genus Brevibacterium or Corynebacterium that are resistant to purmycin and derivatives thereof used in the present invention include the following strains.

うY AJ  1247B  (FERM− これらの菌株は、それぞれブレビバクテリウム・ラクト
フェルメンタム^TCC 13869、ブレビバクテリ
ウム・フラバムATCC 14067およびコリネバク
テリウム・グルタミクムATCC 13032を親株と
して変異誘導したものである。
Y AJ 1247B (FERM- These strains are mutated from Brevibacterium lactofermentum^TCC 13869, Brevibacterium flavum ATCC 14067, and Corynebacterium glutamicum ATCC 13032, respectively, using parent strains.

上記変異株の変異誘導方法としては、紫外線照射、放射
線照射変異誘導起剤処理等の通常の方法が用いられ、例
えば2000μg/n+j!のニトロソグアニジンでO
℃20分間処理する方法等がある.上記例示の菌株の各
薬剤耐性に関する実験結果を第1表に示す. これらの菌株を用いてL−グルタミン酸を生産するには
次のような方法が用いられる.培地としては、甘蔗、甜
菜からの糖汁あるいは廃I!密、澱粉質原料加水分解物
質等のI!質原料、酢酸、エチルアルコール、パラフィ
ン等の非糖質原料を含有する液体培地を用い、培養を行
う。窒素源としては通常のL−グルタミン酸発酵に用い
られるアンモニウム塩、アンモニア水、尿素の他CSL
,蛋白質分解アミノ酸等が用いられる.その他、リン酸
塩、マグネシウム塩等の無機塩、サイアミン、ビオチン
等の微量栄養素等が適宜使用される。ま地に添加される
.培養は好気的条件下で行うのがよく、培養温度は24
〜37℃培養中pHは6〜9に制御するのがよ<pHの
調整には無機あるいは有機の酸性あるいはアルカリ性物
質、さらには尿素炭酸カルシウム、アンモニアガス等を
使用することが出来る。発酵液からのL−グルタξン酸
の採取はイオン交換樹脂法、その他の公知の方法を組合
せることにより行われる。
As a method for inducing mutations in the above-mentioned mutant strain, conventional methods such as ultraviolet irradiation, radiation irradiation, and treatment with mutagenic agents are used. For example, 2000 μg/n+j! O with nitrosoguanidine
There are methods such as processing at ℃ for 20 minutes. Table 1 shows the experimental results regarding the drug resistance of the above-mentioned exemplified bacterial strains. The following method is used to produce L-glutamic acid using these strains. As a medium, sugar juice from cane, sugar beet or waste I! Dense, starchy raw material hydrolyzed substances, etc. I! Culture is performed using a liquid medium containing non-carbohydrate raw materials such as raw materials, acetic acid, ethyl alcohol, and paraffin. Nitrogen sources include ammonium salts, aqueous ammonia, urea, and CSL used in normal L-glutamic acid fermentation.
, proteolytic amino acids, etc. are used. In addition, inorganic salts such as phosphates and magnesium salts, micronutrients such as thiamine and biotin, etc. are used as appropriate. It is added to the soil. Cultivation is best carried out under aerobic conditions, with a culture temperature of 24°C.
During cultivation at ~37°C, the pH should be controlled at 6-9.To adjust the pH, inorganic or organic acidic or alkaline substances, as well as urea calcium carbonate, ammonia gas, etc. can be used. Collection of L-glutamic acid from the fermentation liquor is carried out by a combination of the ion exchange resin method and other known methods.

第1表の各菌株の生育度は次のようにして検定した.グ
ルコース0.5g/a、尿素0.15g/設、硫安0.
 1 5 g / a, KHzPO*0. 3 g 
/ +I4−κ2肝04Q,Ig/dl,  MgSO
,・711!0  0.01g/d1、CaC 1 z
 ・2Hg0  0.’ 1 rrg/ a、サイアよ
ン塩酸塩10r/dl、ビオチン3 r / dl ,
 NazB407 ’ 10ftg00.44trz/
a、FeC l t ・6H20  4. 8 5 m
g/ ilJ、CLISO4 ・5Hi0 1.9 5
mg/ dl、(NI44) tMQ1ozm ・41
1200. 1 8 5+ngldl、ZnSO4 ・
7H20  4 4 nv/dI,MnCl14Ht0
  0.3611W/d1および表ニ示tffi〕プル
マイシンを含みpH7.0に調整した培地に、天然培地
(ペプトン1g/dI、酵母エキスIg/〃、NaCj
!  0.5g/dJ、pl1 7. 0 >スラント
で24時間培養した菌を無菌水で懸濁して接種し、24
時間培養して生育値を懸濁で測定した。
The growth rate of each strain in Table 1 was tested as follows. Glucose 0.5g/a, urea 0.15g/a, ammonium sulfate 0.
15 g/a, KHzPO*0. 3g
/ +I4-κ2 liver 04Q, Ig/dl, MgSO
,・711!0 0.01g/d1, CaC 1 z
・2Hg0 0. ' 1 rrg/a, Siayone Hydrochloride 10 r/dl, Biotin 3 r/dl,
NazB407' 10ftg00.44trz/
a, FeCl t ・6H20 4. 8 5 m
g/ilJ, CLISO4 ・5Hi0 1.9 5
mg/dl, (NI44) tMQ1ozm ・41
1200. 1 8 5+ngldl, ZnSO4 ・
7H20 4 4 nv/dI, MnCl14Ht0
0.3611W/d1 and the indicated tffi] A natural medium (peptone 1g/dI, yeast extract Ig/〃, NaCj) was added to a medium containing purmycin and adjusted to pH 7.0.
! 0.5g/dJ, pl1 7. 0 > Bacteria cultured in a slant for 24 hours were suspended in sterile water and inoculated.
After culturing for hours, growth values were measured in suspension.

4.実施例−1 グルコース1 0 g /dl, KHZPO4  0
. 1 g /J、MgSO4・7FlzO  o. 
1 g /dl,サイアミン塩酸塩20r/d1、大豆
分解濃縮液(T − Nとして)36mg/dl、硫安
2.0g/d1、FeSOn’7H20  1vw/d
l、MnSO4・4Hz0  1mg/d!およびビオ
チン3 r/1  (pH7.0)の組成を有する培地
を調整し、その20mjiづつを500ml容振盪フラ
スコに入れ115゜Cで10分間加熱殺菌した。この培
地にそれぞれの菌を接種し往復振盪培養機により31.
5℃で培養を行った。
4. Example-1 Glucose 10 g/dl, KHZPO4 0
.. 1 g/J, MgSO4.7FlzO o.
1 g/dl, thiamine hydrochloride 20r/d1, soybean decomposition concentrate (as T-N) 36mg/dl, ammonium sulfate 2.0g/d1, FeSOn'7H20 1vw/d
l, MnSO4・4Hz0 1mg/d! A medium having a composition of 3 r/1 and biotin 3 r/1 (pH 7.0) was prepared, and 20 mji of each was placed in a 500 ml shake flask and sterilized by heating at 115°C for 10 minutes. 31. Inoculate each bacteria into this medium and use a reciprocating shaking culture machine.
Culture was performed at 5°C.

なお、培養中は培養液をPH6.5〜8. 0に保つた
め、5g/d!の炭酸カルシウムを添加した.また24
時間目に2.5g/dlの硫安を添加し46時間で発酵
終了し、発酵液中に蓄積したし−グルタミン酸の対糖収
率を求めた。
During cultivation, the culture solution should be kept at pH 6.5-8. 5g/d to keep it at 0! of calcium carbonate was added. 24 again
2.5 g/dl of ammonium sulfate was added at 46 hours, and the fermentation was completed in 46 hours, and the yield of glutamic acid accumulated in the fermentation liquid relative to sugar was determined.

結果を第2表に示す。The results are shown in Table 2.

第 2 表 実施例−2 ビートモラセスを還元糖として100■/値、KH.P
O4  1■/dI(pH7.0)の組成を有する培地
を調整し、その30mlづつを50On!!容振盪フラ
スコに分注し、115℃で10分加熱殺菌した.この培
地にそれぞれの菌を接種し、往復振盪培養機により31
.5℃で培養を行った。なお培養中は培養液をpH6.
5〜8.0に保つため400■/〃の尿素水を適宜添加
した。菌接種後所定の生育に到達時にポリオキシソルビ
クンモノパル主ナイトを4■/+++j!の濃度になる
よう添加して30時間で発酵を終了し、発酵液中に蓄積
したL−グルタξン酸の対糖収率を求めた。
Table 2 Example-2 Beet molasses was used as reducing sugar at 100 μ/value, KH. P
Prepare a medium with a composition of O4 1■/dI (pH 7.0), and add 30 ml of it to 50 On! ! The mixture was dispensed into shaker flasks and sterilized by heating at 115°C for 10 minutes. Each bacteria was inoculated into this medium, and the culture medium was incubated with a reciprocating shaking culture machine for 31 days.
.. Culture was performed at 5°C. During cultivation, the culture solution should be kept at pH 6.
In order to maintain the temperature between 5 and 8.0, 400 μ/〃 of urea water was added as appropriate. When the specified growth is reached after inoculating the bacteria, add 4■/+++j of polyoxysorbicne monopal main night! The fermentation was completed in 30 hours, and the yield of L-glutanic acid accumulated in the fermentation liquid relative to sugar was determined.

結果を第3表に示す。The results are shown in Table 3.

第   3   表Table 3

Claims (1)

【特許請求の範囲】[Claims] ブレビバクテリウム属もしくはコリネバクテリウム属に
属し、プルマイシン、およびその誘導体に耐性を有し、
L−グルタミン酸生産能を有する微生物を培養し、培養
液中に生成蓄積したL−グルタミン酸を採取することを
特徴とするL−グルタミン酸の製造法。
It belongs to the genus Brevibacterium or Corynebacterium and is resistant to purmycin and its derivatives.
1. A method for producing L-glutamic acid, which comprises culturing a microorganism capable of producing L-glutamic acid and collecting L-glutamic acid produced and accumulated in the culture solution.
JP1186282A 1989-07-19 1989-07-19 Method for producing L-glutamic acid Expired - Lifetime JP2817228B2 (en)

Priority Applications (8)

Application Number Priority Date Filing Date Title
JP1186282A JP2817228B2 (en) 1989-07-19 1989-07-19 Method for producing L-glutamic acid
AU58745/90A AU628598B2 (en) 1989-07-19 1990-07-06 Process for producing l-glutamic acid
KR1019900010782A KR970009156B1 (en) 1989-07-19 1990-07-16 Method for preparing L-glutamic acid
PE1990172305A PE33790A1 (en) 1989-07-19 1990-07-17 PROCEDURE TO PRODUCE L-GLUTAMIC ACID
BR909003459A BR9003459A (en) 1989-07-19 1990-07-17 PROCESS FOR THE PRODUCTION OF L-GLUTAMIC ACID
MYPI90001193A MY105945A (en) 1989-07-19 1990-07-17 Process for producing l-glutamic acid.
FR9009249A FR2649993B1 (en) 1989-07-19 1990-07-19 PROCESS FOR THE MANUFACTURE OF L-GLUTAMIC ACID
US07/830,530 US5272067A (en) 1989-07-19 1992-02-04 Process for producing L-glutamic acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1186282A JP2817228B2 (en) 1989-07-19 1989-07-19 Method for producing L-glutamic acid

Publications (2)

Publication Number Publication Date
JPH0349690A true JPH0349690A (en) 1991-03-04
JP2817228B2 JP2817228B2 (en) 1998-10-30

Family

ID=16185579

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1186282A Expired - Lifetime JP2817228B2 (en) 1989-07-19 1989-07-19 Method for producing L-glutamic acid

Country Status (7)

Country Link
JP (1) JP2817228B2 (en)
KR (1) KR970009156B1 (en)
AU (1) AU628598B2 (en)
BR (1) BR9003459A (en)
FR (1) FR2649993B1 (en)
MY (1) MY105945A (en)
PE (1) PE33790A1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110923275B (en) * 2019-12-24 2024-01-12 内蒙古阜丰生物科技有限公司 Glutamic acid fermentation and extraction process

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3096252A (en) * 1960-04-23 1963-07-02 Ajinomoto Kk Process for producing l-glutamic acid

Also Published As

Publication number Publication date
PE33790A1 (en) 1991-01-16
AU5874590A (en) 1991-03-28
JP2817228B2 (en) 1998-10-30
AU628598B2 (en) 1992-09-17
KR970009156B1 (en) 1997-06-07
KR910003108A (en) 1991-02-26
MY105945A (en) 1995-02-28
FR2649993B1 (en) 1993-10-01
FR2649993A1 (en) 1991-01-25
BR9003459A (en) 1991-08-27

Similar Documents

Publication Publication Date Title
JP2817155B2 (en) Production method of L-arginine by fermentation method
JPS6236676B2 (en)
JPH02186994A (en) Production of l-amino acid by fermentation
JP3008565B2 (en) Method for producing L-glutamic acid by fermentation method
JPH06237779A (en) Production of l-glutamic acid by fermentation method
JPS6321479B2 (en)
JPS6115695A (en) Preparation of l-isoleucine by fermentation method
JP2876739B2 (en) Production method of L-lysine by fermentation method
JP3006929B2 (en) Production method of L-valine by fermentation method
JPS6224074B2 (en)
JP2578463B2 (en) Production method of L-lysine by fermentation method
JPH0665314B2 (en) Fermentation method for producing L-valine
JP2578474B2 (en) Method for producing L-glutamic acid
JPH0349690A (en) Preparation of l-glutamic acid
JPS6224075B2 (en)
JPH0561914B2 (en)
JP2995816B2 (en) Production method of L-lysine by fermentation method
JPH027635B2 (en)
JPH0594A (en) Production of anthranilic acid by fermentation
JPS6324896A (en) Production of l-glutamic acid by fermentation
JPH04166092A (en) Production of l-lysine by fermentation
JPH029795B2 (en)
JPH0211236B2 (en)
JPH055476B2 (en)
JPS60156399A (en) Preparation of 5'-xanthylic acid

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090821

Year of fee payment: 11

EXPY Cancellation because of completion of term