JPS61282092A - Production of l-lysine by fermentation method - Google Patents

Production of l-lysine by fermentation method

Info

Publication number
JPS61282092A
JPS61282092A JP60125499A JP12549985A JPS61282092A JP S61282092 A JPS61282092 A JP S61282092A JP 60125499 A JP60125499 A JP 60125499A JP 12549985 A JP12549985 A JP 12549985A JP S61282092 A JPS61282092 A JP S61282092A
Authority
JP
Japan
Prior art keywords
lysine
superoxide
strain
superoxide dismutase
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.)
Granted
Application number
JP60125499A
Other languages
Japanese (ja)
Other versions
JPH0411196B2 (en
Inventor
Yasuhiko Yoshihara
吉原 康彦
Yoshio Kawahara
河原 義雄
Shigeo Ikeda
茂穂 池田
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 JP60125499A priority Critical patent/JPS61282092A/en
Priority to FR8608398A priority patent/FR2583061B1/en
Publication of JPS61282092A publication Critical patent/JPS61282092A/en
Priority to US07/469,687 priority patent/US5179010A/en
Publication of JPH0411196B2 publication Critical patent/JPH0411196B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/0004Oxidoreductases (1.)
    • C12N9/0089Oxidoreductases (1.) acting on superoxide as acceptor (1.15)
    • 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
    • C12P13/08Lysine; Diaminopimelic acid; Threonine; Valine

Landscapes

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

Abstract

PURPOSE:To produce L-lysine by the fermentation method at a low cost, by using a microorganism, having enhanced superoxide dismutase activity, belonging to the genus Brevibacterium or Corynebacterium and capable of producing L-lysine. CONSTITUTION:A microorganism, belonging to the genus Brevibacterium or Corynebacterium and having the ability to produce L-lysine is subjected to variation treatment. A strain having resistance to superoxide dismutase production increaser, superoxide dismutase induction inhibitor, superoxide radical reaction accelerator or an oxidizing agent feeding an enzyme forming the superoxide is selected from the resultant variant strain. The resultant variant strain has enhanced superoxide dismutase activity and can be cultivated to collect L-lysine from the culture fluid readily at a low cost.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は発酵法によるL −リジンの製造法に関する。[Detailed description of the invention] (Industrial application field) The present invention relates to a method for producing L-lysine using a fermentation method.

さらに詳しくは、強化されたスーツや一オキシドジスム
ターゼ活性を有する!レピパクテリウム属又はコリネバ
クテリウム属のL−リジン生産菌を用いる発酵法による
I、−IJジンを製造する方法に関する。
More specifically, it has an enhanced suit and monooxide dismutase activity! The present invention relates to a method for producing I, -IJ gin by a fermentation method using L-lysine producing bacteria of the genus Lepipacterium or Corynebacterium.

(従来の技術) 従来、発酵法によるL−リジンの製造法として1s−(
2−7ミノエチル)−L−システィン(以下AECと記
す)耐性菌を使用する方法(%公昭42−55213号
)、AEC耐性でかつL−ロイシン、L−ホモセリン、
L−プロリン、L−アルギ=7、あ、いゆL−ア、=□
よ、δrLa−hY。
(Prior art) Conventionally, as a method for producing L-lysine by a fermentation method, 1s-(
2-7minoethyl)-L-cysteine (hereinafter referred to as AEC) resistant bacteria (% Publication No. 42-55213), AEC-resistant and L-leucine, L-homoserine,
L-Proline, L-Argi = 7, A, IYL-A, =□
Yo, δrLa-hY.

変異株を使用する方法(%開昭49−36888号、特
開昭49−80289号、特公昭51−21078号)
、AEC耐性でかつβ−ヒドロキシルロイシン(以下H
L!:記t)等のロイシンアナログ耐性変異株を用いる
方法(特公昭53−1833)、α−クロロカグロラク
タム(以下CCLと記す)耐性変異株を用いる方法(特
公昭53−43591)、γ−メチルリジン(以下ML
と記す)耐性変異株を用いる方法(特公昭56−192
35) 、フルオロピルビン酸(以下FPと記す)感受
性変異株を使用する方法(特開昭55−9783号)、
ピルビン酸キナーゼ活性が低下した変異株を使用する方
法(特開昭58−170487号)などが知られている
Method using mutant strains (% 1987-36888, JP 49-80289, JP 51-21078)
, AEC resistant and β-hydroxyleucine (hereinafter H
L! : A method using a leucine analog resistant mutant strain such as t) (Japanese Patent Publication No. 53-1833), a method using a mutant strain resistant to α-chlorocaglolactam (hereinafter referred to as CCL) (Japanese Patent Publication No. 53-43591), γ- Methylysine (hereinafter referred to as ML)
) method using resistant mutant strains (Special Publication No. 56-192)
35), a method using a fluoropyruvate (hereinafter referred to as FP) sensitive mutant strain (Japanese Unexamined Patent Publication No. 55-9783),
A method using a mutant strain with reduced pyruvate kinase activity (Japanese Unexamined Patent Publication No. 170487/1987) is known.

(本発明が解決しようとする問題点) 本発明が解決しようとする問題点は、更に安価に発酵法
によfi L −リジンを製造する方法を確立すること
にある。
(Problems to be Solved by the Present Invention) The problems to be solved by the present invention are to establish a method for producing fi L-lysine by a fermentation method at a lower cost.

(問題点を解決するための手段) 本発明者らは上述の問題点を解決するためにL−リジン
生産菌の菌株改良によって発酵収率を高めるべく種々検
討し九結果、L−リジン生産菌のス−74−オキシドシ
スムターゼ活性tiめることによってこの菌のL −I
Jレシン産能を大巾に高めうろことを見出し、これに基
いて本発明を完成するに至っ九。
(Means for Solving the Problems) In order to solve the above-mentioned problems, the present inventors conducted various studies to increase the fermentation yield by improving the strain of L-lysine-producing bacteria, and as a result, found that The L-I of this bacterium was reduced by decreasing the su-74-oxidocysmutase activity of
They discovered that the production capacity of J-resin could be greatly increased, and based on this, they completed the present invention.

すなわち本発明は、ブレビバクテリウム属を念はコリネ
バクテリウム属に属し、強化されたスーパーオキシドジ
スムターゼ活性を有シ、かつL−リジン生産能を有する
変異株を培養して培養液中にL−リジンを生成、蓄積せ
しめ、これを採取することを特徴とする発酵法によるL
−リジンの製造方法に関するものである。
That is, the present invention involves culturing a mutant strain of the Brevibacterium genus, specifically the Corynebacterium genus, having enhanced superoxide dismutase activity and L-lysine producing ability, and injecting L-lysine into the culture solution. L produced by a fermentation method characterized by producing and accumulating lysine and collecting it.
- It relates to a method for producing lysine.

本発明に使用する微生物は、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L−リジン生産能を有す
るものを変異処理し、得られた変異株のうちからスーノ
ヤーオキシド増産剤、スーパ−オキシドジスムターゼ誘
導抑制剤、スーパーオキシドラジカル反応促進剤または
スーパーオキシ本発明で誘導する変異株の親株としては
ブレビパフチリウム属又はコリネバクテリウム属に属す
る微生物であれば種、菌株を問わずどのような菌株でも
良いが、以下に示すような、いわゆるコリネフォームの
L−グルタミン酸生産菌として知られるものが好適であ
る。
The microorganisms used in the present invention belong to the genus Brevibacterium or Corynebacterium and have the ability to produce L-lysine. Dismutase induction inhibitors, superoxide radical reaction promoters, or superoxy As the parent strain of the mutant strain induced by the present invention, any microorganism belonging to the genus Brevipaftillium or Corynebacterium, regardless of its species or strain, can be used. Although any bacterial strain may be used, the so-called coryneform L-glutamic acid producing bacteria shown below are suitable.

グレピパクテリウム・デパリカタム     ATCC
14020ブレビバクテリウム・フラブム      
 ATCC14067!レビバクテリウム・ラクト7ア
ーメンタム ATCC13869グレピパクテリウム・
ロゼラム       ATCC13825コリネバク
テリウム・アセトアシドフィラム ATCC13870
コリネバクテリウム・リリウム       ATCC
15990菌株としては、これら野生株の他に、リジン
生産に有利な性質、例えばAEC耐性、CCL耐性、■
、耐性、ホモセリン要求性、アラニン要求性、フルオロ
ピルビン酸感受性、スレオニン感受性、メチオニン感受
性などの性質を有する変異株を使用することもできる。
Grepipacterium deparicatum ATCC
14020 Brevibacterium flavum
ATCC14067! Levibacterium lacto 7 amentum ATCC13869 Grepipacterium
Roserum ATCC13825 Corynebacterium acetoacidophyllum ATCC13870
Corynebacterium Lilium ATCC
In addition to these wild strains, the 15990 strain has properties that are advantageous for lysine production, such as AEC resistance, CCL resistance,
Mutant strains having properties such as resistance, homoserine auxotrophy, alanine auxotrophy, fluoropyruvate sensitivity, threonine sensitivity, methionine sensitivity, etc. can also be used.

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
、リジン生産に有利な性質を有する菌株を用いて、本発
明の変異株を得るには、紫外線照射、X線照射、変異誘
起剤処理等の一般に微生物を変異誘導する通常の方法を
用いればよい。変異誘起剤処理の例としては、250μ
97111のN−二トローN′−メチルーN−二トロソ
グアニジンによって30℃で20分間処理する方法があ
る。
In order to obtain the mutant strain of the present invention using a strain belonging to the Brevibacterium genus or Corynebacterium genus and having properties advantageous for lysine production, microorganisms such as ultraviolet irradiation, X-ray irradiation, mutagenic agent treatment, etc. are generally used. Any conventional method for inducing mutations may be used. An example of mutagen treatment is 250μ
There is a method of treating with N-nitro N'-methyl-N-nitrosoguanidine of 97111 at 30° C. for 20 minutes.

本発明においてはこのようにして得られた変異株カラス
−ツク−オキシド増産剤、スー/4− # *シトシス
ムメーゼ誘導抑制剤、スーパ−オキシドラジカル反応促
進剤、またはスー・平−オキシドを形成する酸素を供給
する醸化剤に対する耐性株を選別取得する。
In the present invention, the thus obtained mutant Karasu-Tsuku-oxide production enhancer, Su/4-#*cytosis induction inhibitor, superoxide radical reaction accelerator, or oxygen forming Su/4- Select and obtain strains that are resistant to the brewing agent that supplies them.

これらの薬剤はいずれもスーツ4−オキシド(02−)
と不飽和脂肪酸の反応による過酸化脂質の形成をしやす
くするものである。すなわち、これらO薬剤耐性株は細
胞活性が低下しやすい環境下で増殖する細胞活性の強い
菌株である筈であシ、本発明者らはこのような菌株がL
−I7ジン生産用の菌株として極めてすぐれていること
を見出したのである。
Both of these drugs are suit 4-oxide (02-)
This facilitates the formation of lipid peroxides through the reaction of unsaturated fatty acids with unsaturated fatty acids. In other words, these O drug-resistant strains are supposed to be strains with strong cell activity that proliferate in an environment where cell activity is likely to decrease.
-I7 It was discovered that this strain is extremely excellent as a strain for producing gin.

スーツ!−オキシド増産剤とは生体内においてスーパー
オキシドを増す作用を有するものであシ、例えばメチル
ビオロゲン、ニトロ7ラントイン、ビタミンに1、モル
フイン、ストレプトニグリン、アドリアマイシン、マイ
トマイシンC,ダウノマイシン、ブレオマイシン、β−
ラノ母コン、eia−グラチナム([I)ジアミノジク
ロライドの如きものである。
suit! - Oxide production enhancers are those that have the effect of increasing superoxide in the living body, such as methyl viologen, nitro7lantoin, vitamin 1, morphine, streptonigrin, adriamycin, mitomycin C, daunomycin, bleomycin, β-
It is a compound such as lanocontainer, eia-gratinum ([I) diaminodichloride.

スーパーオキシドジスムターゼ誘導抑制剤とはスー・ぐ
−オキシドを過酸化水素に変える酵素であるスーパーオ
キシドジスムターゼの生体内における誘導生成を抑制す
るもので、例としてはピーーロマイシンを挙げることが
できる。
A superoxide dismutase induction inhibitor is an agent that inhibits the induction of superoxide dismutase, an enzyme that converts sour oxide into hydrogen peroxide, in vivo, and pelomycin can be mentioned as an example.

スーツや−オキシドラジカル反応促進剤とは、スー・母
−オキシドが不飽和脂肪酸と反応して過酸化脂質を生成
する反応を促進するものであシ、例としてフェニルヒド
ラノンを挙げることができる。
The suit or oxide radical reaction accelerator is one that promotes the reaction in which a soot mother oxide reacts with an unsaturated fatty acid to produce lipid peroxide, and phenylhydranone can be mentioned as an example.

酸化剤は生体内でスーパーオキシドを形成する酸素を供
給するものであシ、例えば過酸化ベンゾイル、過硫酸ア
ンモニウムの如きものである。
The oxidizing agent is one that supplies oxygen that forms superoxide in vivo, such as benzoyl peroxide and ammonium persulfate.

これらの薬剤に対する耐性株の取得は通常の薬剤耐性株
取得方法に準じて行なえばよく、例えば前記薬剤のいず
れかを親株が生育しないような濃度で含有する寒天培地
に変異株を撒いて培養し、生育し九コロニーを採取すれ
ばよい。培地中の薬剤の濃度は薬剤の種類によって異な
)、例えばメチルピオロrンの場合には1.5μシ’a
t程H、ビューロマイシンの場合には0.5μ117a
t 徨度、フェニルヒドラジンの場合には20μシ旬程
度、過酸化ベンゾイルの場合には20μ79/rd程度
が適当である。その他の薬剤を用い゛る場合には予め培
養試験を行なフて適切な濃度を定めればよいことはいう
までもない。
Obtaining strains resistant to these drugs can be carried out in accordance with the usual method for obtaining drug-resistant strains, for example, by spreading and culturing the mutant strain on an agar medium containing one of the above drugs at a concentration that does not allow the growth of the parent strain. , all you need to do is to grow and collect nine colonies. (The concentration of the drug in the medium varies depending on the type of drug), for example, in the case of methylpiolone, the concentration of drug is 1.5μ a
t H, in case of buromycin 0.5μ117a
In the case of phenylhydrazine, a suitable degree of t-tolerance is about 20μ, and in the case of benzoyl peroxide, it is about 20μ79/rd. Needless to say, when using other drugs, a culture test may be conducted in advance to determine the appropriate concentration.

また、グレピパクテリウム属またはコリネパクテリクム
属に属する野生株を変異処理し、得られた変異株の中か
らスーツ臂−オキシド増産剤、スー/4−オキクドソス
ムメーゼ鰐導抑制剤、スーツ4’−オキシドラジカル反
応促進剤ま九はスー・臂−オキシドを形成する酸素を供
給する酸化剤に耐性を有する株を選別し九後にこれらの
耐性株にリジン化してもリジン生産能を大巾に高めた菌
株を取得できる。
In addition, wild strains belonging to the genus Grepipacterium or Corynepactericum were subjected to mutation treatment, and from among the obtained mutant strains, a suit arm oxide production enhancer, a crocodile induction inhibitor for suo/4-oxydososummase, etc. The 4'-oxide radical reaction accelerator is used to select strains that are resistant to oxidizing agents that supply oxygen to form soot-oxides. You can obtain strains with greatly increased

本発明に使用しうる微生物の例としては、スーツ々−オ
キシド増産剤については、メチルピオロr中シトジスム
ターゼ誘導抑制剤については、ピ。
Examples of microorganisms that can be used in the present invention include: methyl pyrolytic acid, methylpyrolytic acid, methylpyrolytic acid, cytodismutase induction inhibitor, and cytodismutase induction inhibitor.

−ロマイシンに耐性を有するコリネバクテリウ・ム・ア
セトグルタミカムAJ 12,2′23 (FERM−
直こまた、スーツや−オキシドラジカル反応促進剤につ
いては、てスー・々−オキシドを形成する酸素を供給す
る酸化剤については、過酸化ベンゾイルに耐性を有すこ
のよ5な微生物を用いてL−リジンを生成蓄゛積させる
にはL −Uジン発酵に用いられる常法を用いて行なえ
ばよい。
- Corynebacterium acetoglutamicum AJ 12,2'23 (FERM-
In addition, for suits and -oxide radical reaction accelerators, for oxidizing agents that supply oxygen to form tetanus-oxide, we can use these five microorganisms that are resistant to benzoyl peroxide. - Lysine can be produced and accumulated using a conventional method used for L-U gin fermentation.

すなわち、使用する培地としては、通常の炭素源、窒素
源、無機イオンその他の栄養素の含有する通常の培地を
用いる。炭素源としては、例えばサトウキビ、甜菜から
の糖汁あるいは廃糖蜜、澱粉加水分解物等の糖質原料等
ま九は酢酸等の有機酸等を用いればよい。
That is, the medium to be used is a conventional medium containing a conventional carbon source, nitrogen source, inorganic ions, and other nutrients. As the carbon source, for example, sugar juice from sugar cane or sugar beet, or carbohydrate raw materials such as blackstrap molasses or starch hydrolyzate, or organic acids such as acetic acid may be used.

優素源も通常のL−IJジン発酵に用いられるアンモニ
ウム塩、アンモニア水、尿素等を用いればよく、その他
リン酸イオン、マグネシウムイオン等の有機イオン及び
サイアミン等のビタミンを必要に応じて適宜使用する。
Ammonium salts, aqueous ammonia, urea, etc. used in normal L-IJ gin fermentation may be used as the element source, and organic ions such as phosphate ions, magnesium ions, and vitamins such as thiamine may be used as necessary. do.

栄養要求性株のような特定の物質を生育に必要とする菌
株を用いるときにはこれらの物質そのものを培地に加え
るか、これらを含む蛋白加水分解物、ペプトン、コーン
ステーf+)カー、肉工Φス、酵母エキスなどを加えた
培地を用いればよい。
When using bacterial strains that require specific substances for growth, such as auxotrophic strains, these substances themselves must be added to the culture medium, or protein hydrolysates containing these substances, peptone, cornstarch, meat processing A medium to which yeast extract or the like may be added may be used.

培養条件についても、温度30〜40℃、PH6〜8の
範囲内で好気的条件で実施する等常法によりて実施すれ
ばよい。また、発酵液からL −I7ゾンを取得する方
法も常法に従って行なえばよいことはいうまでもない。
Regarding the culture conditions, the culture may be carried out by a conventional method, such as under aerobic conditions at a temperature of 30 to 40°C and a pH of 6 to 8. Furthermore, it goes without saying that L-I7zone can be obtained from the fermentation broth by any conventional method.

本発明はL−グルタミン酸生産菌にそのスーツ4’−オ
キシドジスムターゼ活性を強化することによってL−リ
ジン生産能を高めるという全く新規な知見に係るもので
あシ、本発明の方法によってL−リジンを簡便な手段で
安価に取得できる。
The present invention relates to the completely new finding that L-lysine production ability is increased by enhancing the suit 4'-oxide dismutase activity of L-glutamic acid producing bacteria. It can be obtained easily and inexpensively.

次に、本発明の方法に使用する微生物の取得例を示す。Next, an example of obtaining microorganisms used in the method of the present invention will be shown.

親株として下記に示す微生物を使用した。The microorganism shown below was used as a parent strain.

!レビパクテリウム・ラクトフェルメンタムAJ 39
90 、FERM−P 3387 (AECr、MLr
、kt*−)!レピパクテリウム・フラバムF’AEC
1−30。
! Levipacterium lactofermentum AJ 39
90, FERM-P 3387 (AECr, MLr
,kt*-)! Lepipacterium flavum F'AEC
1-30.

FgRM−P 282 (kEC’ )コリネバクテリ
ウム・アセトグルタミカム AJ3792 、  FE
RM−P 2650 (AEC’ 、 β−HI、r)
これらの菌株をブイヨンスラントで24時間培養し、得
られた各菌株をいずれも250μl/rutのN−二ト
ローN/ −メチル−N−ニトロソクアニジンによって
30℃で20分間処理して変異株を得九〇 イーストエキス1 it/m sペグトンIF/dg、
食塩0、5117dlおよび寒天217dlよシなる培
地に、メチルビオロゲン1.5μg〜、ピューロマイク
70.5μg7mt、  フェニルヒドラノン20μ7
77rd、過酸化ベンゾイル10μb包を添加し、いず
れもpH7,0に調整後120Cで15分間殺菌して寒
天培地を調製し念。
FgRM-P 282 (kEC') Corynebacterium acetoglutamicum AJ3792, FE
RM-P 2650 (AEC', β-HI, r)
These strains were cultured in bouillon slant for 24 hours, and each strain was treated with 250 μl/rut of N-nitro-N/-methyl-N-nitrosoquanidine at 30°C for 20 minutes to isolate mutant strains. Toku90 Yeast Extract 1 it/m s Pegton IF/dg,
In a medium consisting of 0.5117 dl of sodium chloride and 217 dl of agar, 1.5 μg ~ of methyl viologen, 70.5 μg of Puromic, 7 mt, and 20 μ7 of phenylhydranone.
77rd and a 10 μb packet of benzoyl peroxide were added, and after adjusting the pH to 7.0, sterilization was carried out at 120C for 15 minutes to prepare an agar medium.

前記変異株をこの寒天培地に撒いて31.5℃で48時
間培養し、生成したコロニーを採取して各薬剤耐性株を
取得し、表1に記載された各AJ番号を付与し友。
The mutant strain was spread on this agar medium and cultured at 31.5°C for 48 hours, and the resulting colonies were collected to obtain each drug-resistant strain, which was assigned each AJ number listed in Table 1.

このようにして得られた各薬剤耐性株および親株につい
て各薬剤の濃度を変えて生育試験を行なっ之結果を次に
示す。
Growth tests were conducted on each of the drug-resistant strains and the parent strain thus obtained, with varying concentrations of each drug.The results are shown below.

試験方法としては、いずれの菌株もブイヨンスラントで
24時間培養し、イーストエキスl 1ldl−ベグト
ン117m 1食塩0.5I殉および寒天211/di
を含有するpH7,0の培地を直径8tMのシャーレに
入れて調製し几寒天プレート上に菌数がグレート当シ1
05〜10個になるように撒い友。そして、その上に第
1表に示す濃度の各薬剤を含有するペーノ量−ディスク
をおいて16〜48時間培養後、形成される生育阻止円
の存在の有無によりて生育度を求めた。各薬剤耐性株お
よびその親株について得られた結果を81表に示す。な
お、表中井、+は菌の生育度を表わし、−は生育が観察
されなかりたものを表わしている。
As a test method, all strains were cultured for 24 hours in bouillon slant, yeast extract 1 1 ldl-Begton 117 ml 1 common salt 0.5 I and agar 211/di.
A medium containing pH 7.0 was prepared by placing it in a Petri dish with a diameter of 8 tM, and the number of bacteria was 1.
Sprinkle so that there are 05 to 10 pieces. Then, a peno disk containing each drug at the concentration shown in Table 1 was placed thereon and cultured for 16 to 48 hours, and the degree of growth was determined based on the presence or absence of a growth inhibition circle formed. Table 81 shows the results obtained for each drug-resistant strain and its parent strain. In addition, + indicates the degree of growth of the bacteria, and - indicates that no growth was observed.

第  1  表 前述の各薬剤耐性株およびその親株のスー・量−オキシ
ドシスムターゼ活性を測定し九結果を第2表に示す。
Table 1 The oxidocysmutase activity of each of the above-mentioned drug-resistant strains and their parent strains was measured and the results are shown in Table 2.

測定は次のようにして行なりた。まず、各菌株の培養液
20ゴを10.00 Orpmで10分間遠心して沈殿
物を集め、PH7の0.1Mリン酸緩衝液で2回洗浄し
た。洗浄した沈殿物に前記リン酸緩衝液を2014加え
て懸濁し、超音波処理t−5分間行なりてから10.0
0 Orpmで10分間遠心し、得られた上清液を試料
とした。
The measurements were carried out as follows. First, 20 cultures of each strain were centrifuged at 10.00 Orpm for 10 minutes to collect precipitates, which were washed twice with 0.1M phosphate buffer, pH 7. The washed precipitate was suspended by adding 2014 ml of the phosphate buffer solution, and subjected to ultrasonication for 5 minutes, and then 10.0
The mixture was centrifuged at 0 Orpm for 10 minutes, and the resulting supernatant was used as a sample.

試験管にpH10,2の0.05M炭酸ナトリウム緩衝
液2.4 al t−とシ、3mMキサンチン、3mM
EDT人、0.15%5%クシアルブミンよび0゜75
2?IMニトログルーテトラゾリウムを各々0.1d添
加し次。これに前記試料0.1 mを加えて25℃で1
0分間放置し、後述するキサンチンオキシダーゼ溶液0
.1dを加えすばやく攪拌して25Cでインキ−ベート
した。20分後に6mMC託旬0.IMlを添加して反
応を停止させ、560 nmにおける吸光度を測定した
。一方、試料のかわ9に蒸溜水を用いて同様の操作を行
ない、得られ九吸光度をブランクとした。
In a test tube, add 0.05M sodium carbonate buffer at pH 10.2, 2.4 alt, 3mM xanthine, 3mM
EDT human, 0.15% 5% oxyalbumin and 0°75
2? Next, 0.1 d each of IM nitroglutetrazolium was added. Add 0.1 m of the above sample to this and heat at 25°C for 1
Leave to stand for 0 minutes, and add xanthine oxidase solution 0 to be described later.
.. 1d was added, stirred quickly, and incubated at 25C. After 20 minutes, 6mMC 0. The reaction was stopped by adding IMl and the absorbance was measured at 560 nm. On the other hand, the same operation was carried out using distilled water as the sample glue 9, and the obtained absorbance 9 was used as a blank.

活性単位は、このような測定条件でキサンチンオキシダ
ーゼ灰石を1/2阻害するスーツクーオキシドジスムタ
ーゼ活性を1単位とした。
One unit of activity was defined as the activity of suction oxide dismutase that inhibits xanthine oxidase by half under these measurement conditions.

なお、前記キサンチンオキシダーゼ溶液は、ブランク試
験における吸光度が0.23前後になるようにキサンチ
ンオキシダーゼを2M(NH4)2804で希釈し友も
のであシ、キサンチンオキシダーゼ濃度は約2.lX1
0  Mでありた。
The xanthine oxidase solution was prepared by diluting xanthine oxidase with 2M (NH4) 2804 so that the absorbance in the blank test was around 0.23, and the xanthine oxidase concentration was about 2. lX1
It was 0M.

第  2  表 以下、実施例を示す。Table 2 Examples are shown below.

実施例1 グルコース3619/lEj、塩化アンモニウム20r
r9/kl、KH2PO41w/kl、Mg5O4・7
 aq O,4m9/M 。
Example 1 Glucose 3619/lEj, ammonium chloride 20r
r9/kl, KH2PO41w/kl, Mg5O4・7
aq O, 4m9/M.

F@5O44aq 10 tsl/ml、MnSO44
aq 8 fi177kl、大豆蛋白酸加水分解物(窒
素として)1Mg/rttl 、サイアミン塩酸塩0.
1μシnおよびピオチン0.3μ/17fnlを含有す
る培地を調製し、その30dづつを5004容の振盪フ
ラスコに入れて115℃で10分間を接種し、往復振盪
機によシ31.5℃で培養を行っ次。48時間で発酵を
終了し発酵液中に蓄積したL −IJジンを測定し次。
F@5O44aq 10 tsl/ml, MnSO44
aq 8 fi177kl, soybean protein acid hydrolyzate (as nitrogen) 1Mg/rttl, thiamine hydrochloride 0.
Prepare a medium containing 1μ sin and 0.3μ/17fnl piotin, put 30d each into a 5004 volume shaking flask, inoculate at 115°C for 10 minutes, and transfer to a reciprocating shaker at 31.5°C. Next, culture. Fermentation was completed in 48 hours, and L-IJ gin accumulated in the fermentation liquid was measured.

その結果、第3表に示すようにいずれの薬剤耐性株も良
好なL −IJジン(塩酸塩換算)を蓄積していた。
As a result, as shown in Table 3, all drug-resistant strains accumulated good L-IJ gin (in terms of hydrochloride).

第  3  表 実施例2 廃蔗糖蜜を糖として80〃旬、正2PO414旬、Mg
SO4・7aq 1 m9/ml、大豆加水分解物を窒
素換算で14旬および硫酸アンモニウム500μg7r
tttの組成を有する培地を調製しくp)(7,0)、
その20ゴづつを500d振盪フラスコに分注して加熱
殺菌し、あらかじめ別殺菌した炭酸カルシウムを1.9
加えた。この培地に下記の菌株を接種し、往復振盪機に
よ、931.5℃で培養を行つ次。
Table 3 Example 2 Using waste cane molasses as sugar, 80 yen, regular 2PO 414 yen, Mg
SO4.7aq 1 m9/ml, soybean hydrolyzate 14 times in terms of nitrogen and ammonium sulfate 500μg7r
Prepare a medium having the composition of ttt p) (7,0),
Dispense 20 grams of each into 500 d shake flasks and heat sterilize them.
added. The following bacterial strains were inoculated into this medium and cultured at 931.5°C using a reciprocating shaker.

72時間で発酵を終了し、発酵液中に蓄積し九L−リジ
ンを測定し比。その結果、第4表に示すようにいずれの
薬剤耐性株もL −IJレシン塩酸塩換算)を良好に蓄
積し念。
Fermentation was completed in 72 hours, and the nine L-lysine accumulated in the fermentation liquid was measured and compared. As a result, as shown in Table 4, all drug-resistant strains successfully accumulated L-IJ (resin hydrochloride equivalent).

第  4  表Table 4

Claims (1)

【特許請求の範囲】 1、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、強化されたスーパーオキシドジスムターゼ活性
を有し、かつL−リジン生産能を有する変異株を培養し
て培養液中にL−リジンを生成、蓄積せしめ、これを採
取することを特徴とする発酵法によるL−リジンの製造
方法。 2、変異株がスーパーオキシド増産剤、スーパーオキシ
ドジスムターゼ誘導抑制剤、スーパーオキシドラジカル
反応促進剤、またはスーパーオキシドを形成する酸素を
供給する酸化剤に耐性を有するものである特許請求の範
囲第1項記載の製造方法。
[Scope of Claims] 1. A mutant strain belonging to the genus Brevibacterium or Corynebacterium that has enhanced superoxide dismutase activity and L-lysine production ability is cultured, and L-lysine is added to the culture solution. - A method for producing L-lysine by a fermentation method, which comprises producing, accumulating, and collecting lysine. 2. Claim 1, wherein the mutant strain is resistant to superoxide production agents, superoxide dismutase induction inhibitors, superoxide radical reaction promoters, or oxidizing agents that supply oxygen to form superoxide. Manufacturing method described.
JP60125499A 1985-06-10 1985-06-10 Production of l-lysine by fermentation method Granted JPS61282092A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP60125499A JPS61282092A (en) 1985-06-10 1985-06-10 Production of l-lysine by fermentation method
FR8608398A FR2583061B1 (en) 1985-06-10 1986-06-10 PROCESS FOR PRODUCING L-LYSINE BY FERMENTATION
US07/469,687 US5179010A (en) 1985-06-10 1990-01-26 Fermentation process for producing L-lysine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60125499A JPS61282092A (en) 1985-06-10 1985-06-10 Production of l-lysine by fermentation method

Publications (2)

Publication Number Publication Date
JPS61282092A true JPS61282092A (en) 1986-12-12
JPH0411196B2 JPH0411196B2 (en) 1992-02-27

Family

ID=14911619

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60125499A Granted JPS61282092A (en) 1985-06-10 1985-06-10 Production of l-lysine by fermentation method

Country Status (2)

Country Link
JP (1) JPS61282092A (en)
FR (1) FR2583061B1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002089253A (en) * 2000-09-11 2002-03-27 Ibiden Co Ltd Holding seal material of catalytic converter for exhaust emission control

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2103617B (en) * 1981-08-10 1986-05-21 Kyowa Hakko Kogyo Kk Production of l-lysine by fermentation and new micro-organisms obtained by protoplast fusion

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002089253A (en) * 2000-09-11 2002-03-27 Ibiden Co Ltd Holding seal material of catalytic converter for exhaust emission control

Also Published As

Publication number Publication date
JPH0411196B2 (en) 1992-02-27
FR2583061B1 (en) 1989-07-28
FR2583061A1 (en) 1986-12-12

Similar Documents

Publication Publication Date Title
JP3151073B2 (en) Production of amino acids by fermentation
JPH0529436B2 (en)
JPS5832596B2 (en) Method for producing L-glutamic acid by fermentation method
JPS5810075B2 (en) New mutant strain
JP3717970B2 (en) Method for producing L-isoleucine by fermentation
JPS6257315B2 (en)
JP2876739B2 (en) Production method of L-lysine by fermentation method
JPS6224073B2 (en)
JPS61282092A (en) Production of l-lysine by fermentation method
JP2600750B2 (en) Method for producing L-threonine by fermentation
JPS6224074B2 (en)
US5179010A (en) Fermentation process for producing L-lysine
Kisumi et al. Construction of an L-Arginine-producing mutant in Serratia marcescens: use of the wide substrate specificity of acetylornithinase
JPS6312292A (en) Production of l-lysine
JPH02234686A (en) Production of l-lysine by fermentation method
JP2995816B2 (en) Production method of L-lysine by fermentation method
JPH0347838B2 (en)
JP2876743B2 (en) Method for producing L-threonine by fermentation
JPH0314436B2 (en)
JPS62253391A (en) Production of l-tryptophan by fermentation
US3616230A (en) Method for production of l-asparaginase
JP2817189B2 (en) Method for producing L-threonine by fermentation
JPH0369518B2 (en)
JPS61128897A (en) Production of l-phenylalanine by fermentation method
JPS5816691A (en) Preparation of l-lysine

Legal Events

Date Code Title Description
EXPY Cancellation because of completion of term