JPH0591895A - Production of d-serine - Google Patents

Production of d-serine

Info

Publication number
JPH0591895A
JPH0591895A JP20180791A JP20180791A JPH0591895A JP H0591895 A JPH0591895 A JP H0591895A JP 20180791 A JP20180791 A JP 20180791A JP 20180791 A JP20180791 A JP 20180791A JP H0591895 A JPH0591895 A JP H0591895A
Authority
JP
Japan
Prior art keywords
serine
tyrosine
cells
phenol
reaction
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
JP20180791A
Other languages
Japanese (ja)
Inventor
Masato Terasawa
真人 寺沢
Hisashi Yamagata
恒 山縣
Hideaki Yugawa
英明 湯川
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.)
Mitsubishi Petrochemical Co Ltd
Original Assignee
Mitsubishi Petrochemical 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 Mitsubishi Petrochemical Co Ltd filed Critical Mitsubishi Petrochemical Co Ltd
Priority to JP20180791A priority Critical patent/JPH0591895A/en
Publication of JPH0591895A publication Critical patent/JPH0591895A/en
Pending legal-status Critical Current

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  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Abstract

PURPOSE:To efficiently obtain D-serine in high purity by allowing a microbial cell having tyrosinase activity to act on a reaction liquid containing DL-serine and phenol and converting only L-serine into L-tyrosine. CONSTITUTION:A microorganismic cell having tyrosinase activity [preferably Escherichia coil TD-001 (FERM P-10838)] or treated product thereof is made to act on a reaction liquid containing DL-serine and phenol to convert L-serine into L-tyrosine and then unreacted D-serine is collected. The reaction is preferably carried out in a solvent such as 0.1M phosphoric acid buffer solution at 30-40 deg.C, normally for 2-72hr.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、酵素法によるD−セリ
ンの高効率な製造法に関する。本発明によれば、高効率
にD−セリンを製造でき、また併産されるL−チロシン
の分離は容易であるため、D−セリンが高純度高収量で
分離可能となる。
TECHNICAL FIELD The present invention relates to a highly efficient method for producing D-serine by an enzymatic method. According to the present invention, D-serine can be produced with high efficiency, and the co-produced L-tyrosine can be easily separated. Therefore, D-serine can be separated with high purity and high yield.

【0002】D−セリンは、医薬、食品、農薬等の中間
体原料として、産業上重要な化合物として期待されてい
るアミノ酸である。一方併産されるL−チロシンもま
た、医薬、化粧品等の原料として重要なアミノ酸であ
る。
D-serine is an amino acid expected as an industrially important compound as an intermediate raw material for medicines, foods, agricultural chemicals and the like. On the other hand, co-produced L-tyrosine is also an important amino acid as a raw material for medicines, cosmetics and the like.

【0003】[0003]

【発明が解決しようとする課題】D−セリンの工業的製
造は、これまでほとんど知られていない。本発明者ら
は、酵素法によるD−セリン製造プロセスの開発につい
て鋭意検討を行い、安価なDL−セリンより効率良くD
−セリンを製造する方法を見い出し、本発明を完成する
に到った。
The industrial production of D-serine has heretofore been largely unknown. The present inventors have conducted extensive studies on the development of a D-serine production process by an enzymatic method, and performed D-serine more efficiently than inexpensive DL-serine.
-Finding a method for producing serine, the present invention has been completed.

【0004】[0004]

【課題を解決するための手段】本発明は、チロシナーゼ
活性を有する微生物菌体又はその処理物を、DL−セリ
ンおよびフェノールを含有する反応液に作用させて、酵
素法によりL−セリンをL−チロシンに変換した後、生
成したL−チロシンと未反応D−セリンとを分離するこ
とにより、高収量でD−セリンを採取する方法を提供す
るものである。
[Means for Solving the Problems] The present invention allows a microbial cell having tyrosinase activity or a treated product thereof to act on a reaction solution containing DL-serine and phenol, and L-serine is converted into L-serine by an enzymatic method. It is intended to provide a method for collecting D-serine in high yield by separating L-tyrosine produced and unreacted D-serine after conversion into tyrosine.

【0005】本発明の方法によれば、L−チロシンの溶
解度(約0.04g/l 、25℃)とD−セリンの溶解度
(約600g/l 、25℃)との差により、効率良くD−
セリンを分離することができる。
According to the method of the present invention, due to the difference between the solubility of L-tyrosine (about 0.04 g / l, 25 ° C) and the solubility of D-serine (about 600 g / l, 25 ° C), D −
Serine can be separated.

【0006】本発明に使用する微生物菌体としては、チ
ロシナーゼ活性を有する微生物であれば、特に限定され
るものではないが、例えば、エシェリヒア・コリ(Esch
erichia coli)TD−001(FERM P−1083
8)が好適に用いられる。
The microbial cell used in the present invention is not particularly limited as long as it has a tyrosinase activity. For example, Escherichia coli ( Esch.
erichia coli ) TD-001 (FERM P-1083
8) is preferably used.

【0007】本発明の方法に使用される、上記微生物菌
体の調製に使用する培地は、特に限定されるものではな
く、一般の微生物の培養に使用されるものでよい。例え
ば、炭素源としては、グルコース、グリセロール等が使
用できる。また、培地の窒素源としては、例えばアンモ
ニア、硫酸アンモニウム、塩化アンモニウム、硝酸アン
モニウム、尿素等の無機塩を用いることができる。ま
た、ペプトン、酵母エキス、コンスティープリカー、カ
ザミノ酸等の有機栄養源は、炭素源及び窒素源として使
用することができる。無機塩としては、リン酸一水素カ
リウム、リン酸二水素カリウム、硫酸マグネシウム等が
用いられる。また、用いる菌の特性に応じて培養に必要
な成分を添加することができる。
The medium used for preparing the above-mentioned microbial cells used in the method of the present invention is not particularly limited and may be one used for culturing general microorganisms. For example, glucose, glycerol or the like can be used as the carbon source. As the nitrogen source of the medium, for example, inorganic salts such as ammonia, ammonium sulfate, ammonium chloride, ammonium nitrate and urea can be used. Further, organic nutrient sources such as peptone, yeast extract, constip liquor and casamino acid can be used as carbon sources and nitrogen sources. As the inorganic salt, potassium monohydrogen phosphate, potassium dihydrogen phosphate, magnesium sulfate and the like are used. Further, components necessary for culturing can be added depending on the characteristics of the bacterium used.

【0008】培養は通気攪拌、振盪等の好気的条件下で
行い、培養温度は20〜40℃、好ましくは28〜32
℃で行う。培養途中のpHは5〜10、好ましくは7〜8
付近に保ち、培養中のpHの調整には、酸又はアルカリを
添加して行う。培養期間は10時間〜4日間、最適期間
は1〜3日間である。
The culture is carried out under aerobic conditions such as aeration and stirring, and the culture temperature is 20 to 40 ° C., preferably 28 to 32.
Perform at ℃. The pH during the culture is 5 to 10, preferably 7 to 8.
Keeping the temperature around and adjusting the pH during culturing, add acid or alkali. The culture period is 10 hours to 4 days, and the optimum period is 1 to 3 days.

【0009】このようにして得られた培養物から菌体を
集めて、水又は適当な緩衝液で洗浄し、本発明のD−セ
リンの製造方法に供する。
The cells are collected from the culture thus obtained, washed with water or an appropriate buffer, and subjected to the method for producing D-serine of the present invention.

【0010】なお、本発明の方法では、上記調製した培
養菌体を菌体のまま用いることもできるが、該菌体を超
音波処理等で破砕した破砕物、又はその破砕物をさらに
水等で抽出した抽出物、又は該抽出物をさらに硫安等で
処理して酵素成分を沈殿させた粗精製物の形で使用する
こともできる。さらに該菌体又はそれらの処理物は必要
により固定化して用いることもできる。固定化法として
は、公知の例えばL. Goldstein, Method in Enzymolog
y, 19, 935 (1970)に記載の方法が利用でき、具体的に
はアクリルアミド等の重合性モノマー、アルギン酸塩、
カラギーナン等の適当な担体に菌体を固定化して不溶化
させる方法等がある。
In the method of the present invention, the above-prepared cultured cells can be used as they are, but the cells are crushed by ultrasonication or the like, or the crushed material is further treated with water or the like. It can also be used in the form of the extract extracted in step 1, or a crude product obtained by further treating the extract with ammonium sulfate or the like to precipitate the enzyme component. Further, the cells or their treated products can be used after being immobilized if necessary. As the immobilization method, known methods such as L. Goldstein, Method in Enzymolog
The method described in y, 19, 935 (1970) can be used, and specifically, a polymerizable monomer such as acrylamide, alginate,
There is a method of immobilizing the cells by immobilizing them on a suitable carrier such as carrageenan.

【0011】上記微生物菌体又はその処理物の存在下で
のDL−セリンとフェノールとの反応は、通常の酵素反
応と同様に、例えば0.1Mリン酸緩衝液(pH6.0〜
10.0)又は水(pH6.0〜10.0)等の溶媒中
で、約20〜50℃、好ましくは約30〜40℃の温度
で、通常約2〜72時間で行われる。反応は攪拌効果を
与えつつ行うのが好ましい。
The reaction between DL-serine and phenol in the presence of the above-mentioned microbial cells or a treated product thereof is, for example, a 0.1M phosphate buffer solution (pH 6.0 to pH 6.0) in the same manner as a usual enzyme reaction.
10.0) or water (pH 6.0 to 10.0) and the like at a temperature of about 20 to 50 ° C, preferably about 30 to 40 ° C, usually for about 2 to 72 hours. The reaction is preferably carried out while giving a stirring effect.

【0012】反応液中のフェノール濃度は特に厳密に限
定されるものではないが、反応液中の濃度が1.0%
(w/v )以下に保たれるように連続的又は断続的に培地
に添加して反応させるのが特に好ましい。またその全添
加量も特に限定されるものではないが、通常0.1〜1
0%、好ましくは0.5〜5%(w/v )である。
The phenol concentration in the reaction solution is not particularly limited, but the concentration in the reaction solution is 1.0%.
(W / v) It is particularly preferable to continuously or intermittently add to the medium so that the reaction is performed so that the reaction rate is kept below. The total addition amount is not particularly limited, but is usually 0.1 to 1
It is 0%, preferably 0.5 to 5% (w / v).

【0013】D−又はDL−セリンの反応液中の濃度
は、一般には0.1〜20%(w/v )、好ましくは1.
0〜10%(w/v )の範囲で使用するのが適当である。
The concentration of D- or DL-serine in the reaction solution is generally 0.1 to 20% (w / v), preferably 1.
It is suitable to use in the range of 0 to 10% (w / v).

【0014】[0014]

【発明の効果】本発明の製造方法によれば、原料DL−
セリン中のL−セリンをL−チロシンに効率良く変換
し、未反応D−セリンを高収率で分離、採取することが
できる。
According to the manufacturing method of the present invention, the raw material DL-
L-serine in serine can be efficiently converted into L-tyrosine, and unreacted D-serine can be separated and collected in high yield.

【0015】[0015]

【実施例】以下、実施例により本発明を更に詳細に説明
する。
The present invention will be described in more detail with reference to the following examples.

【0016】参考例:β−チロシナーゼ含有菌体の調製 表1に示した培地100mlを500ml容三角フラスコに
分注し、120℃で15分間減菌処理したものに、β−
チロシナーゼ生産菌であるエシェリヒア・コリTD−0
01(FERM P−10838)を植菌し、37℃で
1日振盪培養した。
Reference Example: Preparation of β-Tyrosinase-Containing Bacteria 100 ml of the medium shown in Table 1 was dispensed into a 500 ml Erlenmeyer flask and sterilized at 120 ° C. for 15 minutes.
Escherichia coli TD-0 which is a tyrosinase-producing bacterium
01 (FERM P-10838) was inoculated and cultured with shaking at 37 ° C for 1 day.

【0017】[0017]

【表1】 [Table 1]

【0018】該培養液の20mlを同様にして調製した培
地1000mlに接種し、通気攪拌培養槽を用い、37℃
にて回転数1000rpm 、通気量1 vvm、pH7.2(2
8%アンモニア水で調整)にて20時間培養した。
20 ml of the culture broth was inoculated into 1000 ml of a medium prepared in the same manner, and the culture was aerated with stirring at 37 ° C.
Rotation speed 1000 rpm, ventilation volume 1 vvm, pH 7.2 (2
It was cultured in 8% ammonia water) for 20 hours.

【0019】培養終了後、200mlづつ遠心分離(80
00rpm 、15分間、4℃)することにより集菌し、5
0mMリン酸緩衝液(pH8.0)20mlにより菌体を洗浄
後、集菌した菌体を−20℃にて1日間凍結させ、該菌
体を供試菌とした。
After completion of the culture, centrifugation was carried out in 200 ml portions (80
The cells were collected by collecting the cells at 00 rpm for 15 minutes at 4 ° C. for 5
After washing the cells with 20 ml of 0 mM phosphate buffer (pH 8.0), the collected cells were frozen at -20 ° C for 1 day, and the cells were used as test cells.

【0020】実施例 参考例で培養液200mlから集菌して調製したβ−チロ
シナーゼ含有菌体を、表2に示す反応液50mlに懸濁
後、500ml容三角フラスコにて30℃で24時間振盪
し、反応させた。
Example The β-tyrosinase-containing cells prepared by collecting cells from 200 ml of the culture solution in the reference example were suspended in 50 ml of the reaction solution shown in Table 2 and then shaken in a 500 ml Erlenmeyer flask at 30 ° C. for 24 hours. And allowed to react.

【0021】[0021]

【表2】 [Table 2]

【0022】反応終了後に、反応液全量を遠心分離(8
000rpm 、15分間、4℃)した上清中のD−セリン
量を測定したところ4.2mg/mlであった。なお、上清
液中のL−セリン対D−セリンの比率(L/D)を液体
クロマトグラフィー(島津LC−5A、カラム:東ソー
(株)EnantioL1)を用いて測定したところL/D<
1/1000であった。
After completion of the reaction, the whole reaction solution was centrifuged (8
The amount of D-serine in the supernatant after being subjected to 5,000 rpm, 15 minutes, 4 ° C.) was 4.2 mg / ml. The ratio of L-serine to D-serine (L / D) in the supernatant was measured by liquid chromatography (Shimadzu LC-5A, column: Tosoh Enantio L1), and L / D <
It was 1/1000.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 チロシナーゼ活性を有する微生物菌体又
はその処理物を、DL−セリンおよびフェノールを含有
する反応液に作用させて、酵素法によりL−セリンをL
−チロシンに変換し、これよりD−セリンを採取するこ
とを特徴とするD−セリンの製造法。
1. A microbial cell having tyrosinase activity or a treated product thereof is allowed to act on a reaction solution containing DL-serine and phenol to convert L-serine to L by an enzymatic method.
-A method for producing D-serine, which comprises converting to tyrosine and collecting D-serine from this.
JP20180791A 1991-08-12 1991-08-12 Production of d-serine Pending JPH0591895A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20180791A JPH0591895A (en) 1991-08-12 1991-08-12 Production of d-serine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20180791A JPH0591895A (en) 1991-08-12 1991-08-12 Production of d-serine

Publications (1)

Publication Number Publication Date
JPH0591895A true JPH0591895A (en) 1993-04-16

Family

ID=16447248

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20180791A Pending JPH0591895A (en) 1991-08-12 1991-08-12 Production of d-serine

Country Status (1)

Country Link
JP (1) JPH0591895A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002036803A1 (en) 2000-11-01 2002-05-10 Kyowa Hakko Kogyo Co., Ltd. Process for producing d-serine
JP2006254795A (en) * 2005-03-17 2006-09-28 Shimane Univ Aspartic acid dehydrogenase, alanine dehydrogenase, method for producing l-aspartic acid and method for producing d-malic acid
DE102010025124A1 (en) 2010-06-25 2011-12-29 Forschungszentrum Jülich GmbH Process for the preparation of D-amino acids, microorganism, and vector

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002036803A1 (en) 2000-11-01 2002-05-10 Kyowa Hakko Kogyo Co., Ltd. Process for producing d-serine
EP1331274A4 (en) * 2000-11-01 2005-08-10 Kyowa Hakko Kogyo Kk Process for producing d-serine
US7186532B2 (en) 2000-11-01 2007-03-06 Kyowa Hakko Kogyo Co., Ltd. Process for producing D-serine
JP2006254795A (en) * 2005-03-17 2006-09-28 Shimane Univ Aspartic acid dehydrogenase, alanine dehydrogenase, method for producing l-aspartic acid and method for producing d-malic acid
DE102010025124A1 (en) 2010-06-25 2011-12-29 Forschungszentrum Jülich GmbH Process for the preparation of D-amino acids, microorganism, and vector

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