JPS61268175A - Cultivation of tryptophan synthetase-producing microbial strain - Google Patents

Cultivation of tryptophan synthetase-producing microbial strain

Info

Publication number
JPS61268175A
JPS61268175A JP60111207A JP11120785A JPS61268175A JP S61268175 A JPS61268175 A JP S61268175A JP 60111207 A JP60111207 A JP 60111207A JP 11120785 A JP11120785 A JP 11120785A JP S61268175 A JPS61268175 A JP S61268175A
Authority
JP
Japan
Prior art keywords
concentration
tryptophan
tryptophan synthetase
culture
synthetase
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.)
Pending
Application number
JP60111207A
Other languages
Japanese (ja)
Inventor
Norisue Takeshita
竹下 徳末
Koji Osumi
大隅 孝治
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.)
Nippon Steel Corp
Original Assignee
Sumitomo Metal Industries 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 Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP60111207A priority Critical patent/JPS61268175A/en
Publication of JPS61268175A publication Critical patent/JPS61268175A/en
Pending legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

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  • Enzymes And Modification Thereof (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Abstract

PURPOSE:To culture a tryptophan synthetase-producing strain having high activity, in high efficiency and yield, by culturing a mutant of Escherichia coli in a specific medium. CONSTITUTION:A mutant of Escherichia coil capable of producing tryptophan synthetase is inoculated in a medium containing glucose as a carbon source at a concentration of <=10%, ammonium sulfate as a nitrogen source at a concentration of <=5% and organic acids, etc., and cultured aerobically at 4-9pH and 20-50 deg.C to obtain tryptophan synthetase. L-tryptophan can be produced by reacting indole with L-seselin in the presence of the above tryptophan synthetase as a catalyst.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、エシェリヒア(Escherichia)属
に属するトリプトファン・シンセターゼ(E。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to tryptophan synthetase (E.) belonging to the genus Escherichia.

C,4,2,1,20:インドールとL−セリンよりL
−トリプトファン合成を触媒する酵素)生産菌の培養方
法に関する0 〔従来の技術〕 近年、L−)+3ブトフアンは輸液成分・精神安定剤等
の医薬品および医薬品原料以外に、飼料添加物としての
効果が認めらn、工業的規模による安価な生産が検討さ
ルている0 従来、L−1リブトフアンの製造は、主として化学合成
法および発酵法により行なわnてきた。化学合成法は高
温・高圧といった荷酷な条件が必要であり、また、長い
反応経路を有し、生成物がD体、L体のラセミ混合物で
あるために、必要とするL体を得るために光学分割を行
なわなけnばならなかった0発酵法では、微生物の物質
代謝を利用して糖類よりL−トリブトファ/を製造する
方法である0こnによって生成するトリプトファンはL
体のみであって光学分割する必要はないが、微生物の生
育に必要な種々の物質および代謝産物の混合物から目的
の生成物を分離するのに難点があり、さらに生菌体を用
いているために、雑菌に対する汚染に関する対策も必要
である。
C, 4, 2, 1, 20: L from indole and L-serine
-Enzyme that catalyzes tryptophan synthesis) 0 [Conventional technology] In recent years, L-)+3butophane has been used as a feed additive in addition to pharmaceuticals such as infusion components and tranquilizers and raw materials for pharmaceuticals. However, inexpensive production on an industrial scale is being considered. Conventionally, L-1 ribotophan has been produced mainly by chemical synthesis and fermentation methods. Chemical synthesis requires harsh conditions such as high temperature and high pressure, has a long reaction route, and the product is a racemic mixture of D and L forms, so it is difficult to obtain the required L form. In the 0-fermentation method, which required optical resolution to be carried out, the tryptophan produced by 0-con is a method of producing L-tributophane from sugars using the metabolism of microorganisms.
However, it is difficult to separate the desired product from a mixture of various substances and metabolites necessary for the growth of microorganisms, and since live microorganisms are used, it is not necessary to perform optical resolution. In addition, countermeasures against bacterial contamination are also necessary.

こnに対して、酵素法による合成ではトリプトファンの
代謝に関与する酵素を触媒として、常温常圧でインドー
ルおよびL−セリンよりL−トリプトファンを一段階の
反応によって得るために、製造に際してエネルギーおよ
びコストにおいて、前記方法により非常に有利である。
In contrast, in enzymatic synthesis, L-tryptophan is obtained from indole and L-serine in one step at room temperature and pressure using an enzyme involved in tryptophan metabolism as a catalyst, which requires less energy and cost during production. The method provides significant advantages.

この反応の触媒となる酵素として、トリプトファン・シ
ンセターゼがちシ、これはエシェリヒア(Escher
ichia )属に属する微生物によって生産さnるが
、こnらを遺伝的に改良した微生物では、一層効率よく
酵素を生産する。本酵素は、精製単離した状態、または
酵素を含む培養菌体、無細胞抽出液、固定化物などで使
用できる。
The enzyme that catalyzes this reaction is tryptophan synthetase, which is produced by Escherichia.
The enzyme is produced by microorganisms belonging to the genus Ichia), but microorganisms that have been genetically improved from these microorganisms produce the enzyme more efficiently. The present enzyme can be used in a purified and isolated state, or in the form of cultured bacterial cells, cell-free extracts, immobilized products, etc. containing the enzyme.

本酵素を工業的規模で使用するためには、安価な培地で
高い活性を有するトリプトファン・シンセターゼ生産菌
を高収量で効率よく培養することが必要である。本酵素
の性質は、マイルス(E−Mi les 、 Adr−
Enzymol、 l 42+ 127 +(1979
))等によって報告さfている。
In order to use this enzyme on an industrial scale, it is necessary to efficiently culture tryptophan synthetase-producing bacteria with high activity in an inexpensive medium with high yield. The properties of this enzyme are as described by E-Miles, Adr-
Enzymol, l 42+ 127 + (1979
)) etc. have been reported.

しかるに、このトリプトファン・シンセターゼ生産菌の
培養には、天然培地tたは合成培地が用いらnているが
、培養条件、特に培地組成に関する検討はほとんど報告
さnておらず、経験的に求めら几た組成のものが使用さ
nており、わずかに特開昭58−20186号公報にお
いて、培地中のグルコース濃度が1%以下に保たnるよ
うにグルコースを連続的tたは断続的に添加するように
した、トリプトファン・シンセターゼ生産菌の培養方法
が開示さnている。
However, although natural or synthetic media have been used to culture this tryptophan synthetase-producing bacterium, there have been few reports on culture conditions, especially on culture medium composition, and it has not been determined empirically. In Japanese Patent Application Laid-open No. 58-20186, glucose is added continuously or intermittently to keep the glucose concentration in the medium below 1%. A method for culturing tryptophan synthetase-producing bacteria is disclosed.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

上記特開昭58−20186号公報に開示さnている方
法では、グルコース濃度を1チ以下に保つために、グル
コース濃度の分析を迅速に行なう必要があるが、現在、
培地成分からグルコースのみを直接に定量する方法はな
く、グルコース濃度と相関関係にある溶存酸素濃度CD
O値)とI)Hの変化よりグルコース濃度の調節を行な
っている。この場合、グルコース濃度ゼロになったこと
がDo値等に現わnることより、14以下にするように
している0さらに詳しい分析を行なうとなると培養装置
に、グルコース分析用の装置が付属するため、初めに所
定量の糖濃度に仕込んだ場合と比較して、工業的規模の
培養の場合設備面で複雑になる。さらにま念、同公報で
は窒素源についての検討はなさnていない0 そこで、本発明の目的は、トリプトファン・シンセター
ゼを生産するエシェリヒア・コリ変異株の培養において
、培地中炭素源としてのグルコース濃度を10係以下、
窒素源としての硫酸アンモニウム濃度を5%以下とする
ことによって、培養途中でグルコース濃度測定、濃度調
節をすることなく、したがって培養操作が簡潔となシ、
しかも安価な培地で高い酵素活性を有し、菌体収量の良
いトリプトファン・シンセターゼ生産菌の培養方法を提
供することにある。
In the method disclosed in JP-A-58-20186, it is necessary to quickly analyze the glucose concentration in order to keep the glucose concentration below 1 g.
There is no method to directly quantify glucose alone from medium components, and dissolved oxygen concentration CD, which has a correlation with glucose concentration.
Glucose concentration is regulated by changes in O value) and I)H. In this case, since the Do value will show that the glucose concentration has become zero, it should be set to 14 or less.0 For more detailed analysis, a glucose analysis device is attached to the culture device. Therefore, compared to the case where the sugar concentration is initially set to a predetermined amount, the equipment required for culturing on an industrial scale becomes more complicated. Furthermore, this publication does not discuss nitrogen sources. Therefore, the purpose of the present invention is to increase the concentration of glucose as a carbon source in the medium by 10% in the culture of an Escherichia coli mutant strain that produces tryptophan synthetase Below,
By setting the concentration of ammonium sulfate as a nitrogen source to 5% or less, there is no need to measure or adjust the glucose concentration during the culture, which simplifies the culture operation.
Moreover, it is an object of the present invention to provide a method for culturing tryptophan synthetase-producing bacteria that has high enzyme activity and good bacterial cell yield using an inexpensive medium.

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

上記問題点を解決するために、本発明は、インドールと
L−セリンを反応させてL−トリプトファンを製造する
際に触媒として用いる酵素のトリプトファン・シンセタ
ーゼを生産するエシェリヒア・コリ(Escheric
hia−coli )変異株の培養において、培地中の
炭素源としてのグルコース濃度を10係以下、窒素源と
しての硫酸アンモニウム濃度を5係以下とするものであ
る。
In order to solve the above problems, the present invention aims at producing tryptophan synthetase, an enzyme used as a catalyst when producing L-tryptophan by reacting indole with L-serine.
hia-coli) mutant strain, the concentration of glucose as a carbon source in the medium is set to 10 parts or less, and the concentration of ammonium sulfate as a nitrogen source is set to 5 parts or less.

〔作用〕[Effect]

本発明者の知見によnば、トリプトファン・シンセター
ゼを生産するエシェリヒア・コリ変異株の培養において
、培地成分について検討した結果、グルコース濃度を1
0%以下、好ましくは0.5〜5%に、窒素源として硫
酸アンモニウム濃度を5係以下、好ましくは1.0〜5
チ以下とすることによって、高い酵素活性を有する菌体
が収量良く得らf’L、 Lかも培地が安価となること
が判った。また、グルコースおよび硫酸アンモニウムを
一度に仕込むだけでよく、培養中グルコース濃度を測定
する必要がないので培養設備および操作が簡素となるO 〔発明の具体例〕 以下、本発明をさらに詳説する0 まず、第1図を参照して、トリプトファン・シンセター
ゼ生産菌の培養からL−1リプトフアンの合成および分
離・精製までの工程についての概説をする0 (1)酵素生産菌の培養 培養容器中において、組成CC源、N源。
According to the present inventor's findings, as a result of examining the medium components in culturing an Escherichia coli mutant strain that produces tryptophan synthetase, it was found that the glucose concentration was reduced to 1.
0% or less, preferably 0.5 to 5%, and the concentration of ammonium sulfate as a nitrogen source to 5% or less, preferably 1.0 to 5%.
It has been found that by setting the concentration of f'L, L or less, a good yield of bacterial cells with high enzyme activity can be obtained, and the medium can be inexpensive. In addition, since it is only necessary to charge glucose and ammonium sulfate at once, and there is no need to measure the glucose concentration during culture, the culture equipment and operation are simple. [Specific Examples of the Invention] The present invention will be explained in more detail below. First, Referring to Figure 1, we will outline the steps from culturing tryptophan synthetase-producing bacteria to synthesis, isolation, and purification of L-1 liptophan. Source, N source.

ミネラル他)調整を行なった培地中に酵素生産菌を接種
し、温度調節およびpH調節を行いつつ無菌通気培養を
行う。
Enzyme-producing bacteria are inoculated into a medium that has been adjusted (minerals, etc.), and sterile aerated culture is performed while controlling temperature and pH.

(2)集菌 (1)によって得らnfc培養液よフ遠心分離(几とえ
ば110X103rpで20分)により菌体を集め、こ
nをトリプトファン・シンセターゼの酵素源とし、場合
によっては固定化処理等の菌体処理を行う0 (3)合成反応 次に(2)で得らnた酵素を触媒としてインドールとL
−セリンを反応させてL−)リブトファンの合成を行う
0 (4)分離・精製 (3)で得うf″したL−トリプトファンの分離・精製
を行う。
(2) Collect bacteria from the NFC culture solution obtained in step (1) by centrifugation (for example, 110 x 103 rp for 20 minutes), use this as an enzyme source for tryptophan synthetase, and in some cases immobilize it. (3) Synthesis reaction Next, using the enzyme obtained in (2) as a catalyst, indole and L
-React serine to synthesize L-)ributophane (4) Separate and purify the f'' L-tryptophan obtained in (3).

次に、本発明に係るシンセターゼ生産菌の培養方法に関
し詳述する0 本発明に用いるトリプトファン・シンセターゼ生産菌は
、公知のエシェリヒア・コリ(Escherichia
  coli ) W3110から誘導さf′Lfc変
異株であり、該生産菌の培養に当り、その培地に用いる
炭素源はグルコース等の糖類−グリセリン等の多価アル
コール類、クエン酸等の有機酸類、その細微生物が消化
可能な物質は利用でき、その適正濃度は添加物質によっ
て異なり、グルコースの場合、添加濃度は10%以下、
好ましくは0.5〜5憾が望ましい。ここで、培地中グ
ルコース濃度1〜2係における菌生育状態を基準にすn
ば5チまでは濃度増加とともに活性・菌体収量の増加が
認めらnるが、10%までは5憾と比較してそ几はど大
きく増加していない。
Next, the method for culturing the synthetase-producing bacteria according to the present invention will be described in detail.
This is an f'Lfc mutant strain derived from E.coli W3110, and when culturing the producing bacteria, the carbon sources used in the medium are sugars such as glucose, polyhydric alcohols such as glycerin, organic acids such as citric acid, etc. Substances that can be digested by microorganisms can be used, and the appropriate concentration varies depending on the added substance; in the case of glucose, the added concentration is 10% or less;
Preferably 0.5 to 5 is desirable. Here, the bacterial growth condition at glucose concentration 1 to 2 in the medium is used as a standard.
Up to 5%, an increase in activity and bacterial cell yield was observed as the concentration increased, but up to 10%, the concentration did not increase significantly compared to 5%.

さらに10憾を超えると、生育が非常に悪くなる0 窒素源としては、アンモニア、塩化アンモニウム、硫酸
アンモニウム、クエン酸アンモニウム、リン酸アンモニ
ウムなどの各種の有機・無機アンモニウム塩、または肉
エキス、酵母エキス、カゼイン加水分解物、コーン・ス
f−7’・リカーなどの天然有機窒素化合物が用いらn
る0こ几らの天然有機窒素化合物の多くは、窒素源だけ
でなく同時に炭素源としてもm−ることができる。この
場合も、その適正濃度は添加物質によって異なり、硫酸
アンモニウムの場合5チ以下、好ましくは1.0〜5.
0係が望ましい0硫酸アンモニウム濃度が5係を超えた
培地では生育が非常に悪くなる0 さらに、本発明におけるトリプトファン・シンセターゼ
生産菌の培養において、一層効率良く培養を行なうため
に、リン酸マグネシウム。
Furthermore, if the concentration exceeds 10, the growth becomes very poor.Nitrogen sources include various organic and inorganic ammonium salts such as ammonia, ammonium chloride, ammonium sulfate, ammonium citrate, and ammonium phosphate, or meat extract, yeast extract, Natural organic nitrogen compounds such as casein hydrolyzate and corn f-7' liquor are used.
Many natural organic nitrogen compounds can be used not only as a nitrogen source but also as a carbon source at the same time. In this case as well, the appropriate concentration varies depending on the additive substance, and in the case of ammonium sulfate, it is 5% or less, preferably 1.0 to 5%.
A ratio of 0 is desirable.0 Growth is very poor in a medium with an ammonium sulfate concentration of more than 5.Furthermore, in the cultivation of tryptophan synthetase producing bacteria in the present invention, magnesium phosphate is added in order to culture more efficiently.

リン酸カリウム、および鉄、亜鉛、マンガン等の金属イ
オンの無機物、さらにビタミン類、アミノ酸類あるいは
こnらを含む酵母エキス、カザミノ酸、ポリペプトン等
を添加しても良い0こnらの物質は本酵素生産菌の培養
時に、制限基質とならないように培地中に充分量添加し
ておく必要がある。
Potassium phosphate and inorganic substances such as metal ions such as iron, zinc, and manganese, as well as vitamins, amino acids, yeast extract containing these, casamino acids, polypeptone, etc. may be added. When culturing this enzyme-producing bacterium, it is necessary to add a sufficient amount to the medium so that it does not become a limiting substrate.

培養温度は、20〜50℃好ましくは30〜40℃であ
る0培地のpHは4〜9、好ましくは°7〜8であシ、
水酸化ナトリウム、水酸化カリウム等で培養中一定に保
つのが望ましい。培養は好気的に行ない、培養期間中培
地の溶存酸素濃度が酵素生産菌の生育の律速因子になら
ないように、通気および撹拌することが望ましい。
The culture temperature is 20-50°C, preferably 30-40°C. The pH of the medium is 4-9, preferably 7-8°C,
It is desirable to keep the concentration constant during culture using sodium hydroxide, potassium hydroxide, etc. The culture is preferably carried out aerobically, with aeration and stirring so that the dissolved oxygen concentration in the medium does not become a rate-limiting factor for the growth of the enzyme-producing bacteria during the culture period.

さらに、本酵素生産菌の培養において、L−トリプトフ
ァンまたはインドールを添加することが必要である。こ
のようにして得らn几酵素をインドールとL−セリンよ
りL−1リプトフアン合成の触媒として供する。この場
合、精製単離した状態、または酵素を含む培養菌体、無
細胞抽出液、固定化物などで使用できる。ま友、本酵素
を本出願人が先に出願した特願昭59−264228号
の酵素法によるL−1リプトフアンの製造性における酵
素として使用すると効率よ<L−)リブトファンが合成
できる。
Furthermore, it is necessary to add L-tryptophan or indole to the culture of this enzyme-producing microorganism. The n-enzyme thus obtained serves as a catalyst for the synthesis of L-1 liptophan from indole and L-serine. In this case, it can be used in a purified and isolated state, or in the form of cultured bacterial cells containing enzymes, cell-free extracts, immobilized products, etc. Friend, if this enzyme is used as an enzyme in the production of L-1 liptophan by the enzymatic method described in Japanese Patent Application No. 59-264228 previously filed by the present applicant, L-1 liptophan can be synthesized efficiently.

〔実施例〕〔Example〕

次に実施例にて本発明をさらに詳説し、比較例と共にそ
の効果を示す。
Next, the present invention will be further explained in detail in Examples, and its effects will be shown together with Comparative Examples.

(実施例1) トリプトファン・シンセターゼ生産菌であるエシェリヒ
ア・コリ(Escherichia colt) tr
pR−W3110t”第1表に示す培地で種培養を20
時間行ない、そのscr&を第2表に示す組成の培地1
00dに加えて本培養を30’Cで24時間行なった。
(Example 1) Escherichia coli (Escherichia colt) tr which is a tryptophan synthetase producing bacterium
pR-W3110t" Seed culture for 20 minutes in the medium shown in Table 1.
medium 1 with the composition shown in Table 2.
In addition to 00d, main culture was performed at 30'C for 24 hours.

(pH7,0) 第  2  表 (pH8,0) 培養後、菌体を遠心分離(10xl O3rpm20分
)シタ後、生理食塩水に懸濁し、トリプトファンシンセ
ターゼ活性を測定した0菌体濃度は610 nmにおけ
る吸光度より求めた。トリプトファン・シンセターゼ活
性は第3表に示す反応組成の反応液を用いて、37℃、
20分間反応し、単位乾燥菌体量および単位時間当9の
インドールの減少量で表わした。その結果を第4表に示
す。
(pH 7,0) Table 2 (pH 8,0) After culturing, the bacterial cells were centrifuged (10xl O3 rpm 20 minutes), suspended in physiological saline, and the tryptophan synthetase activity was measured.The 0 bacterial cell concentration was 610 nm. It was determined from the absorbance at . Tryptophan synthetase activity was measured at 37°C using a reaction solution with the reaction composition shown in Table 3.
The reaction was carried out for 20 minutes and expressed as the amount of dry bacterial cells and the amount of decrease in indole per unit time. The results are shown in Table 4.

第  3  表 (実施例2) 実施例1において、第2表中の硫酸アンモニウム濃度を
1.0係として同様の操作を行なったO結果を第5表に
示す。
Table 3 (Example 2) Table 5 shows the results obtained by performing the same operation as in Example 1 with the ammonium sulfate concentration in Table 2 set to 1.0.

第  5  表 (実施例3) 実施例1において、第2表中の硫酸アンモニウム濃度を
5.0係として同様の操作に行なった。
Table 5 (Example 3) The same operation as in Example 1 was performed except that the ammonium sulfate concentration in Table 2 was set to 5.0.

結果を第6表に示す。The results are shown in Table 6.

第  6  表 グルコース濃度 乾燥菌体量   菌活性(インドール
減少量)(@      (mg)   nmol沖9
m、9dr7cellO,554,48〜4 1.0        50.0          
932.0        51.6        
  965.0         4’7−1    
      101(比較例) 実施例1において、本培養の組成を第1表の組成(但し
pH8,0)で同様に行なった時の菌体量は73.4 
m&で酵素活性は58 nmol/mm ・4−dry
 cellであっり。
Table 6 Glucose concentration Dry bacterial mass Bacterial activity (indole reduction) (@ (mg) nmol Oki 9
m, 9dr7cellO, 554, 48-4 1.0 50.0
932.0 51.6
965.0 4'7-1
101 (Comparative Example) In Example 1, when the main culture was carried out in the same manner as shown in Table 1 (however, pH 8.0), the amount of bacterial cells was 73.4.
The enzyme activity in m& is 58 nmol/mm ・4-dry
It's easy to use cell.

〔発明の効果〕〔Effect of the invention〕

以上のように、本発明によnば、培養操作が簡潔となり
、また安価な培地成分で従来方法に比べ2〜3倍の高い
酵素活性を示し、しかも菌体収量の良いトリプトファン
・シンセターゼ生産菌の培養をできる。
As described above, according to the present invention, the culture operation is simple, and the tryptophan synthetase-producing bacteria exhibits enzyme activity 2 to 3 times higher than that of the conventional method using inexpensive medium components, and has good cell yield. can be cultured.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はトリプトファン・シンセターゼ生産菌の培養か
らL−トIJブトファンの合成および分離・精製までの
工程図である0 第1図
Figure 1 is a process diagram from culturing tryptophan synthetase-producing bacteria to synthesis, separation, and purification of L-toIJ butophane.0 Figure 1

Claims (1)

【特許請求の範囲】[Claims] (1)インドールとL−セリンを反応させてL−トリプ
トファンを製造する際に触媒として用いる酵素のトリプ
トファン・シンセターゼを生産するエシエリヒア・コリ
(Escherichia−coli)変異株の培養に
おいて、培地中の炭素源としてのグルコース濃度を10
%以下、窒素源としての硫酸アンモニウム濃度を5%以
下とすることを特徴とするトリプトファン・シンセター
ゼ生産菌培養法。
(1) In the culture of an Escherichia coli mutant strain that produces tryptophan synthetase, an enzyme used as a catalyst when producing L-tryptophan by reacting indole and L-serine, carbon sources in the medium The glucose concentration as 10
% or less, and a method for culturing tryptophan synthetase-producing bacteria, characterized in that the concentration of ammonium sulfate as a nitrogen source is 5% or less.
JP60111207A 1985-05-23 1985-05-23 Cultivation of tryptophan synthetase-producing microbial strain Pending JPS61268175A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60111207A JPS61268175A (en) 1985-05-23 1985-05-23 Cultivation of tryptophan synthetase-producing microbial strain

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60111207A JPS61268175A (en) 1985-05-23 1985-05-23 Cultivation of tryptophan synthetase-producing microbial strain

Publications (1)

Publication Number Publication Date
JPS61268175A true JPS61268175A (en) 1986-11-27

Family

ID=14555230

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60111207A Pending JPS61268175A (en) 1985-05-23 1985-05-23 Cultivation of tryptophan synthetase-producing microbial strain

Country Status (1)

Country Link
JP (1) JPS61268175A (en)

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