JPS5813151B2 - Production method of L-norleucine by fermentation method - Google Patents
Production method of L-norleucine by fermentation methodInfo
- Publication number
- JPS5813151B2 JPS5813151B2 JP4051076A JP4051076A JPS5813151B2 JP S5813151 B2 JPS5813151 B2 JP S5813151B2 JP 4051076 A JP4051076 A JP 4051076A JP 4051076 A JP4051076 A JP 4051076A JP S5813151 B2 JPS5813151 B2 JP S5813151B2
- Authority
- JP
- Japan
- Prior art keywords
- norleucine
- isoleucine
- valine
- production method
- serratia
- 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
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- Preparation Of Compounds By Using Micro-Organisms (AREA)
Description
【発明の詳細な説明】
本発明は発酵法によるL−ノルロイシンの製法に関する
。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing L-norleucine by fermentation.
ノルロイシンはメチオニンの代謝拮抗体としてよく知ら
れたアミノ酸であり〔ジュネテイツクス、58,473
〜492(1968)参照〕、またイソロイシン、パリ
ン、ロイシンなどの分岐鎖アミノ酸のアナログとしても
有用なアミノ酸である〔バイオテクノロジー・バイオエ
ンジニアリング、7,245〜268(1965)参照
〕。Norleucine is an amino acid well known as an antimetabolite of methionine [Genetics, 58,473
-492 (1968)], and is also useful as an analog of branched chain amino acids such as isoleucine, parine, and leucine [see Biotechnology and Bioengineering, 7, 245-268 (1965)].
本発明者らは先に、セラチア・マルセツセンスのイソロ
イシン、バリン要求性でかつロイシンによる代謝調節機
構が解除された変異株がノルバリンからL−ノルロイシ
ンを生成蓄積する能力を有していることを報告した〔昭
和49年度日本発酵工学会大会講演要旨集、71〜72
頁参照〕。The present inventors previously reported that a mutant strain of Serratia marsetuscens that is auxotrophic for isoleucine and valine and in which the metabolic regulation mechanism by leucine has been released has the ability to generate and accumulate L-norleucine from norvaline. [Collection of lecture abstracts from the 1971 Japan Fermentation Engineering Society Conference, 71-72
See page].
しかしながら、該菌株は培地中にメチオニンを添加しな
ければ全く生育せず、ノルバリンからL−ノルロイシン
を生成蓄積させることはできなかった。However, this strain did not grow at all unless methionine was added to the medium, and was unable to produce and accumulate L-norleucine from norvaline.
そこで本発明者らは、培地中にメチオニンおよびノルバ
リンを添加しなくてもL−ノルロイシンを生成蓄積せし
めうる微生物を広く検索した結果、セラチア属に属し、
イソロイシン、バリン要求性(部分要求性も含む、以下
同じ)でかつロイシンによる代謝調節機構およびメチオ
ニンによる代謝調節機構が解除されている変異株が、メ
チオニンおよびノルバリンの両者を含まない培地におい
てもL−ノルロイシンを生成蓄積せしめうる能力を有し
ていることを見い出し、本発明を完成するに至った。Therefore, the present inventors conducted a wide search for microorganisms that can produce and accumulate L-norleucine without adding methionine and norvaline to the culture medium, and found that they belong to the genus Serratia.
A mutant strain that is auxotrophic for isoleucine and valine (including partial auxotrophy, the same shall apply hereinafter) and in which the metabolic regulation mechanism by leucine and the metabolic regulation mechanism by methionine is abolished exhibits L- even in a medium that does not contain both methionine and norvaline. They discovered that they have the ability to produce and accumulate norleucine, leading to the completion of the present invention.
本発明において用いられる微生物の例としては、例えば
セラチア・マルセツセンス〔バージーのマニュアル・オ
ブ・デターミネイティブ・バクテリオロジー、第8版、
362頁参照〕イソロイシン、バリン要求性かつロイシ
ンによる代謝調節機構およびメチオニンによる代謝調節
機構が解除された変異株が挙げられる。Examples of microorganisms used in the present invention include, for example, Serratia marsetuscens [Bergie's Manual of Determinative Bacteriology, 8th edition,
[See page 362] Mutant strains that require isoleucine and valine and have a metabolic regulation mechanism by leucine and a metabolic regulation mechanism by methionine are mentioned.
かゝる変異株の取得は、例えば次の如くして行なうこと
ができる。Such mutant strains can be obtained, for example, as follows.
まず通常の変異誘導操作、例えは紫外線照射あるいは変
異誘起剤(例えばN−メチル−N′−ニトロ−N−ニト
ロソグアニジン、エチルメタンスルホネート等)処理に
より原株に変異を誘起せしめ、これをロイシン代謝拮抗
体、例えばα−アミノ酪酸および4−アザロイシンを各
々約10mg/ml添加した平板培地(例えばデービス
基礎培地)に2〜3日間培養し、生じた大コロニーを分
離することにより、ロイシンによる代謝調節機構が解除
された変異株を取得することができる。First, mutations are induced in the original strain by conventional mutation induction operations, such as ultraviolet irradiation or treatment with mutagenic agents (e.g., N-methyl-N'-nitro-N-nitrosoguanidine, ethyl methanesulfonate, etc.), and this induces leucine metabolism. Metabolic regulation by leucine can be investigated by culturing for 2 to 3 days in a plate medium (e.g., Davis basal medium) supplemented with antagonists such as α-aminobutyric acid and 4-azaleucine at approximately 10 mg/ml each, and isolating the resulting large colonies. It is possible to obtain mutant strains in which the mechanism has been released.
次にこの変異株に前記と同様に変異を誘起せしめ、これ
をイソロイシンおよびバリンを各々約2μg/ml添加
した平板培地(例えばデービス基礎培地)に1〜2日間
培養し、生じた小〜中コロニーを分離し、この菌株の要
求性をレプリカ法により確認することにより、イソロイ
シン、バリン要求性でかつロイシンによる代謝調節機構
が解除された変異株を取得することができる。Next, mutations were induced in this mutant strain in the same manner as described above, and this was cultured for 1 to 2 days on a plate medium (e.g., Davis basal medium) supplemented with approximately 2 μg/ml of each of isoleucine and valine, resulting in small to medium colonies. By isolating this strain and confirming the auxotrophy of this strain by the replica method, it is possible to obtain a mutant strain that is auxotrophic for isoleucine and valine and in which the metabolic regulation mechanism by leucine has been abolished.
次にこの変異株に前記と同様に変異を誘起せしめ、これ
を要求アミノ酸少量とメチオニン代謝拮抗体(例えばノ
ルロイシン、メチオニンハイドロキサメート、α−メチ
ルメチオニンなど)を約10mg/ml添加した平板培
地(例えばデービス基礎培地)に2〜3日間培養し、生
じた大コロニーを分離することにより、イソロイシン、
バリン要求性でかつロイシンによる代謝機構およびメチ
オニンによる代謝調節機構が解除されたL−ノルロイシ
ン生産菌を取得することができる。Next, mutations were induced in this mutant strain in the same manner as described above, and the mutant strain was cultured in a plate medium supplemented with a small amount of the required amino acid and approximately 10 mg/ml of a methionine antimetabolite antibody (e.g., norleucine, methionine hydroxamate, α-methylmethionine, etc.). For example, isoleucine,
It is possible to obtain an L-norleucine-producing bacterium that requires valine and has a leucine-based metabolic mechanism and a methionine-based metabolic control mechanism released.
このようにして得られたL−ノルロイシン生産菌の具体
例としては、例えばセラチア・マルセツセンスNLV−
11(微工研菌寄第3498号)(イソロイシン、バリ
ン要求性でかつα−アミノ酪酸、4−アザロイシンおよ
びノルロイシン耐性な変異株)、セラチア・マルセツセ
ンスNLG−21(微工研菌寄第3499号)(イソロ
イシン、バリン要求性でかつα−アミノ酪酸、4−アザ
ロイシンおよぴノルロイシンに耐性な変異株)などが挙
げられる。Specific examples of L-norleucine-producing bacteria obtained in this way include Serratia marsetuscens NLV-
11 (FER No. 3498) (isoleucine and valine auxotrophic mutant strain and resistant to α-aminobutyric acid, 4-azaleucine and norleucine), Serratia marsetuscens NLG-21 (FER No. 3499) ) (a mutant strain that requires isoleucine and valine and is resistant to α-aminobutyric acid, 4-azaleucine, and norleucine).
尚、本発明に係るL−ノルロイシン生産菌の誘導法は特
に制限されるものではなく、例えばまずロイシンによる
代謝調節機構が解除された変異株を取得し、次にこの変
異株にメチオニンによる代謝調節機構が解除された性質
を付与し、最後にこの変異株にイソロイシン、バリン要
求性を付与することによってもL−ノルロイシン生産菌
を取得することができる。The method for inducing L-norleucine-producing bacteria according to the present invention is not particularly limited. For example, first, a mutant strain in which the metabolic regulation mechanism by leucine has been released is obtained, and then this mutant strain is subjected to metabolic regulation by methionine. An L-norleucine-producing bacterium can also be obtained by imparting a property in which the mechanism is released and finally imparting isoleucine and valine auxotrophy to this mutant strain.
また、形質導入の可能な菌株においては、上記3つの性
質のいずれかを持つ変異株を各々別個に取得し、それら
の性質を互いに形質導入することによってもL−ノルロ
イシン生産菌を取得することができる。In addition, among strains that can be transduced, L-norleucine producing bacteria can also be obtained by separately obtaining mutant strains having any of the above three properties and transducing these properties with each other. can.
かくして得られた微生物のL−ノルロイシン生産用培地
としては、炭素源としてブドウ糖、でん粉加水分解物の
如き糖類、フマール酸、クエン酸の如き有機酸類、グリ
セロールの如きアルコール類等を2〜15%、窒素源と
して酢酸アスモニウムの如き有機アンモニウム塩、硫酸
アンモニウム、塩化アンモニウムの如き無機アンモニウ
ム塩、尿素等を0.5〜3%、有機栄養物としてコーン
スチープリカー、ペプトン、酵母エキス等を0〜2%、
さらにイソロイシン、バリンなどの要求アミノ酸を少量
含む培地が好適に用いられる。The thus obtained microbial L-norleucine production medium contains 2 to 15% of sugars such as glucose and starch hydrolyzate, organic acids such as fumaric acid and citric acid, and alcohols such as glycerol as carbon sources; 0.5 to 3% of organic ammonium salts such as asmonium acetate, inorganic ammonium salts such as ammonium sulfate and ammonium chloride, urea, etc. as nitrogen sources; 0 to 2% of corn steep liquor, peptone, yeast extract, etc. as organic nutrients;
Furthermore, a medium containing a small amount of required amino acids such as isoleucine and valine is preferably used.
これらの他にリン酸カリウム、硫酸マグネシウム等を少
量加え、また培地のpHを6〜9に保つために炭酸カル
シウムあるいは必要によりアンモニアを添加してもよい
。In addition to these, a small amount of potassium phosphate, magnesium sulfate, etc. may be added, and calcium carbonate or ammonia may be added if necessary to maintain the pH of the medium at 6 to 9.
さらにこのような培地にL−ノルロイシンの生合成系の
前駆物質、例えはノルバリンまたはα−ケト吉草酸を1
〜3%含有させれぱL−ノルロイシンの生成蓄積量を顕
著に高めることができる。Furthermore, a precursor for the biosynthetic system of L-norleucine, such as norvaline or α-ketovaleric acid, is added to such a medium.
If it is contained in an amount of up to 3%, the amount of L-norleucine produced and accumulated can be significantly increased.
本発明によれは、これらの培地に前記のL−ノルロイシ
ン生産菌を接種し、好気的条件下、例えば強振とうする
如き酸素供給の良好な条件下、25〜37℃にて1〜4
日間培養することにより培地中にL−ノルロイシンを生
成蓄積せしめることができる。According to the present invention, these mediums are inoculated with the L-norleucine-producing bacteria and incubated at 25-37° C. for 1 to 4 hours under aerobic conditions, for example, under conditions with good oxygen supply such as vigorous shaking.
By culturing for days, L-norleucine can be produced and accumulated in the medium.
生成したL−ノルロイシンの採取は、例えばイオン交換
樹脂を用いる通常の分離精製法により容易に行なうこと
ができる。The produced L-norleucine can be easily collected by a conventional separation and purification method using, for example, an ion exchange resin.
以下、実施例を挙げて本発明を具体的に説明するが、実
施例中L−ノルロイシンの定性は第3級アミルアルコー
ル:酢酸:水(20:1:20)の上層を用いるペーパ
ークロマトグラム上のニンヒドリン反応により、またそ
の定量は該反応による発色部分を切抜き抽出し、比色法
により行なった。Hereinafter, the present invention will be specifically explained with reference to Examples. The ninhydrin reaction was carried out, and its quantification was carried out by cutting out and extracting the colored portion resulting from the reaction, and using a colorimetric method.
実施例 1
ブドウ糖2%、デキストリン10%、尿素1%、DL−
ノルバリン2%、第2リン酸カリウム0.1%、硫酸マ
グネシウム7水和物0.05%、コーンスチープリカー
0.7%、L−イソロイシン0.5〜/ml、L−バリ
ン1.0mg/mlおよび炭酸カルシウム3%を含む培
地(pH7.0)15mlを50ml容振とうコルベン
に注入し、加圧滅菌する。Example 1 2% glucose, 10% dextrin, 1% urea, DL-
Norvaline 2%, dibasic potassium phosphate 0.1%, magnesium sulfate heptahydrate 0.05%, corn steep liquor 0.7%, L-isoleucine 0.5~/ml, L-valine 1.0mg/ ml and 15 ml of a medium (pH 7.0) containing 3% calcium carbonate are poured into a 50 ml shaking Kolben and autoclaved.
但し、ブドウ糖およびデキストリンは別滅菌後添加する
。However, glucose and dextrin are added after separate sterilization.
これにセラチア・マルセツセンスNLV−11(微工研
菌寄3498号)(イソロイシン、バリン要求性でかつ
α−アミノ酪酸、4−アザロイシンおよひノルロイシン
に耐性な変異株)を1白金耳植菌し、30℃、140回
転/分、振幅8cmの条件で72時間振とう培養する。One platinum loop of Serratia marsetuscens NLV-11 (Feikoken Bibori No. 3498) (a mutant strain that requires isoleucine and valine and is resistant to α-aminobutyric acid, 4-azaleucine, and norleucine) was inoculated into this. , shake culture for 72 hours at 30° C., 140 revolutions/min, and an amplitude of 8 cm.
培養液中に生成したL−ノルロイシンの量は4.5mg
/mlであった。The amount of L-norleucine produced in the culture solution was 4.5 mg.
/ml.
培養液1lを集め、熱処理後ロ過する。Collect 1 liter of culture solution and filter after heat treatment.
ロ液を強酸性イオン交換樹脂アンバーライト1R−12
0カラムに導通する。The filtrate is strongly acidic ion exchange resin Amberlite 1R-12.
0 column.
このカラムを水洗後、0.15Mアンモニア水で溶出す
る。After washing this column with water, it is eluted with 0.15M aqueous ammonia.
溶出したL−ノルロイシン区分を減圧下に濃縮し、メタ
ノールを加え、析出する結晶をロ取することによりL−
ノルロイシン2.5gを得る。The eluted L-norleucine fraction was concentrated under reduced pressure, methanol was added, and the precipitated crystals were collected by filtration to obtain L-
Obtain 2.5 g of norleucine.
実施例 2
実施例1と同様の培地を用い、セラチア・マルセツセン
スNLG−21(微工研菌寄第3499号)(イソロイ
シン、バリン要求性でかつα−アミノ酪酸、4−アザロ
イシン8よびノルロイシンに耐性な変異株)を実施例1
と同様に培養した。Example 2 Using the same medium as in Example 1, Serratia marsetuscens NLG-21 (FEI No. 3499) (isoleucine and valine auxotrophic and resistant to α-aminobutyric acid, 4-azaleucine 8 and norleucine) was grown. Example 1
It was cultured in the same way.
培養液中に生成したL−ノルロイシンの量は25mg/
mlであった。The amount of L-norleucine produced in the culture solution was 25 mg/
It was ml.
実施例 3
実施例1の培地からDL−ノルバリンを除いた培地を用
い、セラチア・マルセツセンスNLG−21(微工研菌
寄第3499号)を実施例1と同様に培養した。Example 3 Serratia marsetuscens NLG-21 (Feikoken Bacterial Serial No. 3499) was cultured in the same manner as in Example 1 using the medium from Example 1 except that DL-norvaline was removed.
培養液中に生成したL−ノルロイシンの量は0.8mg
/mlであった。The amount of L-norleucine produced in the culture solution is 0.8 mg
/ml.
Claims (1)
かつロイシンによる代謝調節機構およびメチオニンによ
る代謝調節機構が解除されているL−ノルロイシン生産
菌株を培地に培養して培地中にL−ノルロイシンを生産
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−ノルロイシンの製法。 2 菌体がセラチア属に属し、イソロイシン、バリン要
求性でかつロイシン代謝拮抗体およびメチオニン代謝拮
抗体に耐性なL−ノルロイシン生産菌である特許請求の
範囲第1項記載の製法。 3 菌株がセラチア属に属し、イソロイシン、バリン要
求性でかつα−アミノ酪酸、4−アザロイシンおよびノ
ルロイシンに耐性なL−ノルロイシン生産菌である特許
請求の範囲第1項記載の製法。 4 菌株がイソロイシン、バリン要求性でかつロイシン
による代謝調節機構およびメチオニンによる代謝調節機
構が解除されているL−ノルロイシン生産能を有するセ
ラチア・マルセツセンスである特許請求の範囲第1項記
載の製法。 5 菌株がイソロイシン、バリン袈求性でかつロイシン
代謝拮抗体およびメチオニン代謝拮抗体に耐性なL−ノ
ルロイシン生産能を有するセラチア・マルセツセンスで
ある特許請求の範囲第1項記載の製法。 6 菌株がイソロイシン、バリン要求性かつα−アミノ
酪酸、4−アザロイシンおよびノルロイシンに耐性なL
−ノルロイシン生産能を有するセラチア・マルセツセン
スである特許請求の範囲第1項記載の製法。 7 培養を好気的条件下、pH5〜9、温度25〜37
℃で行なう特許請求の範囲第1項、第2項、第3項、第
4項、第5項または第6項記載の製法。 8 培養をL−ノルロイシン生合成系の前駆物質を含む
培地中、好気的条件下、pH5〜9、温度25〜37℃
で行なう特許請求の範囲第1項、第2項、第3項、第4
項、第5項または第6項記載の製法。 9 L−ノルロイシン生合成系の前駆物質がノルバリン
またはα−ケト吉草酸である特許請求の範囲第8項記載
の製法。[Scope of Claims] 1 An L-norleucine-producing strain belonging to the genus Serratia that is auxotrophic for isoleucine and valine and in which the metabolic regulation mechanism by leucine and the metabolic regulation mechanism by methionine have been released is cultured in a medium, and L-norleucine is produced in the medium. - A method for producing L-norleucine by a fermentation method, which is characterized by producing and accumulating norleucine and collecting it. 2. The production method according to claim 1, wherein the bacterial cells belong to the genus Serratia and are L-norleucine-producing bacteria that require isoleucine and valine and are resistant to leucine antimetabolites and methionine antimetabolites. 3. The production method according to claim 1, wherein the bacterial strain belongs to the genus Serratia and is an L-norleucine producing bacteria that is auxotrophic for isoleucine and valine and resistant to α-aminobutyric acid, 4-azaleucine and norleucine. 4. The production method according to claim 1, wherein the strain is Serratia marsetuscens, which is isoleucine and valine auxotrophic and has an ability to produce L-norleucine in which the leucine-based metabolic control mechanism and the methionine-based metabolic control mechanism have been released. 5. The production method according to claim 1, wherein the bacterial strain is Serratia marsetuscens, which is isoleucine and valine fertile and has an ability to produce L-norleucine, which is resistant to leucine antimetabolite antibodies and methionine antimetabolite antibodies. 6 L strain whose strain is isoleucine, valine auxotrophic and resistant to α-aminobutyric acid, 4-azaleucine and norleucine
- The production method according to claim 1, which is Serratia marsetuscens having the ability to produce norleucine. 7 Culture under aerobic conditions, pH 5-9, temperature 25-37.
The manufacturing method according to claim 1, 2, 3, 4, 5 or 6, which is carried out at ℃. 8 Culture in a medium containing a precursor for the L-norleucine biosynthetic system under aerobic conditions at pH 5-9 and temperature 25-37°C.
Claims 1, 2, 3, and 4
5. The manufacturing method according to item 5 or 6. 9. The production method according to claim 8, wherein the precursor of the L-norleucine biosynthesis system is norvaline or α-ketovaleric acid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4051076A JPS5813151B2 (en) | 1976-04-10 | 1976-04-10 | Production method of L-norleucine by fermentation method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4051076A JPS5813151B2 (en) | 1976-04-10 | 1976-04-10 | Production method of L-norleucine by fermentation method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS52125693A JPS52125693A (en) | 1977-10-21 |
| JPS5813151B2 true JPS5813151B2 (en) | 1983-03-11 |
Family
ID=12582531
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4051076A Expired JPS5813151B2 (en) | 1976-04-10 | 1976-04-10 | Production method of L-norleucine by fermentation method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5813151B2 (en) |
-
1976
- 1976-04-10 JP JP4051076A patent/JPS5813151B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS52125693A (en) | 1977-10-21 |
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