JPH11103887A - Production of d-amino acid - Google Patents

Production of d-amino acid

Info

Publication number
JPH11103887A
JPH11103887A JP28614797A JP28614797A JPH11103887A JP H11103887 A JPH11103887 A JP H11103887A JP 28614797 A JP28614797 A JP 28614797A JP 28614797 A JP28614797 A JP 28614797A JP H11103887 A JPH11103887 A JP H11103887A
Authority
JP
Japan
Prior art keywords
amino acid
amino acids
phenylalanine
reaction solution
oxidase
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
JP28614797A
Other languages
Japanese (ja)
Other versions
JP4125809B2 (en
Inventor
Kimiyasu Isobe
公安 礒部
Yoshihiko Hirose
芳彦 広瀬
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.)
Amano Enzyme Inc
Original Assignee
Amano Pharmaceutical Co Ltd
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Application filed by Amano Pharmaceutical Co Ltd filed Critical Amano Pharmaceutical Co Ltd
Priority to JP28614797A priority Critical patent/JP4125809B2/en
Publication of JPH11103887A publication Critical patent/JPH11103887A/en
Application granted granted Critical
Publication of JP4125809B2 publication Critical patent/JP4125809B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To simplify the separation and purification of a D-amino acid from a reaction solution by allowing an enzyme preferentially or specifically acting on an L-amino acid to act on the L-amino acid. SOLUTION: This method for producing a D-amino acid comprises allowing an enzyme (e.g. an L-amino acid oxidase) preferentially or specifically acting on an L-amino acid to act on the D, L-amino acid to convert the L-amino acid into a compound having physical properties largely different from those of the objective D-amino acid, and subsequently separating the left D-amino acid. Only the D-amino acid useful as an intermediate for medicines or agrochemicals or as a modifying agent for antibiotics can easily be deposited.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、医薬・農薬中間体
或いは抗生物質の修飾剤として有用なD−アミノ酸の製
造法に関する。
[0001] The present invention relates to a method for producing a D-amino acid useful as a pharmaceutical / pesticide intermediate or a modifier of an antibiotic.

【0002】[0002]

【従来の技術】D−アミノ酸は非天然型の光学活性アミ
ノ酸であり、製造が困難な化合物として知られている。
これまでに、D−アミノ酸は、L−アミノ酸との物理的
性質の違いを利用した析晶法によって、D,L−アミノ酸
から製造されていた。しかし、両者は共にアミノ酸であ
るため物理的性質の差は小さく、D−アミノ酸の分離精
製には極めて厳密な条件の設定が必要である。
2. Description of the Related Art D-amino acids are unnatural optically active amino acids and are known to be difficult to produce.
Heretofore, D-amino acids have been produced from D, L-amino acids by a crystallization method utilizing a difference in physical properties from L-amino acids. However, since both are amino acids, the difference in physical properties is small, and the separation and purification of D-amino acids require extremely strict conditions.

【0003】また、アシル−D,L−アミノ酸にL−アミ
ノ酸アシラーゼを作用させ、アシル−L−アミノ酸をL
−アミノ酸に分解し、アシル−D−アミノ酸とL−アミ
ノ酸を分離後、アシル−D−アミノ酸を加水分解する方
法、5−置換ヒダントインに酵素を作用させる方法(特
開昭55−104890、特開昭55−114292など)、アシル−D,
L−アミノ酸にD−アミノ酸アシラーゼを作用させ、ア
シル−D−アミノ酸をD−アミノ酸に分解し、アシル−
L−アミノ酸とD−アミノ酸を分離する方法(特公昭53
−36035)等が報告されている。
Further, an acyl-D, L-amino acid is reacted with an L-amino acid acylase to convert the acyl-L-amino acid into an L-amino acid.
A method of hydrolyzing an acyl-D-amino acid after separation into an amino acid and separating an acyl-D-amino acid and an L-amino acid, and a method of allowing an enzyme to act on a 5-substituted hydantoin (JP-A-55-104890; 55-114292), acyl-D,
A D-amino acid acylase is allowed to act on an L-amino acid to decompose an acyl-D-amino acid into a D-amino acid.
A method for separating an L-amino acid and a D-amino acid (Japanese Patent Publication No. Sho 53)
−36035).

【0004】[0004]

【発明が解決しようとする課題】しかしながら、アミノ
酸とアミノ酸の誘導体の物理的性質の差も必ずしも十分
ではないため、上述したようなアミノ酸とアミノ酸の誘
導体の物理的性質の違いを利用するこれらの方法におい
てもD−アミノ酸の分離精製は極めて厳密な条件設定が
必要である。
However, since the difference in physical properties between amino acids and amino acid derivatives is not always sufficient, these methods utilizing the difference in physical properties between amino acids and amino acid derivatives as described above are used. In the above, the separation and purification of D-amino acids require extremely strict conditions.

【0005】更にまた、他の方法においても原料基質が
高価であることや、工程が煩雑であること等や、生成物
の収率、光学純度が低い等の問題点があり、更に低コス
トのD−アミノ酸を製造法が求められていた。
Further, other methods also have problems such as the fact that the raw material substrate is expensive, the steps are complicated, the yield of the product and the optical purity are low. There has been a need for a method for producing D-amino acids.

【0006】[0006]

【課題を解決するための手段】本発明は、D,L−アミノ
酸のうち目的化合物でないL−アミノ酸の物理的性質を
目的化合物であるD−アミノ酸の物理的性質と大きく異
なる化合物に変換し、D−アミノ酸の分離精製を簡便化
する方法を提供するものである。
Means for Solving the Problems The present invention converts the physical properties of an L-amino acid which is not a target compound among D, L-amino acids into a compound which is significantly different from the physical properties of a D-amino acid which is a target compound. It is intended to provide a method for simplifying the separation and purification of D-amino acids.

【0007】[0007]

【発明の実施の形態】本発明者らは温和な条件下でL−
アミノ酸を物理化学的性質の大きく異なり、かつ水溶性
の向上した化合物に変換するための方法を鋭意研究を行
った結果、D,L−アミノ酸を基質として用い、L−アミ
ノ酸酸化酵素のようなL−アミノ酸を優先的又は特異的
に酸化する酵素を用いてL−アミノ酸をオキソ酸に分解
することにより、未分解のD−アミノ酸のみを容易に析
出させることが可能となることを見い出し、D−アミノ
酸を簡便に単離精製して製造する方法を確立した。
BEST MODE FOR CARRYING OUT THE INVENTION The present inventors have found that L-
As a result of intensive studies on a method for converting an amino acid into a compound having greatly different physicochemical properties and improved water solubility, it was found that D, L-amino acid was used as a substrate and L-amino acid oxidase such as L-amino acid oxidase was used. -Decomposition of L-amino acids into oxo acids using an enzyme that preferentially or specifically oxidizes amino acids has been found to make it possible to easily precipitate only undecomposed D-amino acids. We have established a method for easily isolating and purifying amino acids for production.

【0008】即ち、本発明は例えばL−アミノ酸を優先
的又は特異的に酸化して、対応するオキソ酸に変換する
反応を触媒するL−アミノ酸酸化酵素を、D,L−アミノ
酸に作用させた後、残存するD−アミノ酸を分離するこ
とを特徴とするD−アミノ酸の製造法である。
[0008] That is, the present invention comprises reacting a D, L-amino acid with, for example, an L-amino acid oxidase that catalyzes a reaction of preferentially or specifically oxidizing an L-amino acid to convert it to a corresponding oxo acid. Thereafter, a method for producing a D-amino acid, comprising separating the remaining D-amino acid.

【0009】以下本発明について詳しく述べるが、本発
明は、これに限定されるものではない。
Hereinafter, the present invention will be described in detail, but the present invention is not limited thereto.

【0010】本発明の基質として使用できるD,L−アミ
ノ酸としては、例えば、D,L−グルタミン酸、D,L−バリ
ン、D,L−アスパラギン酸、D,L−メチオニン、D,L−ロ
イシン、D,L−イソロイシン、D,L−ヒスチジン、D,L−
アルギニン、D,L−フェニルアラニン、D,L−チロシン、
D,L−トリプトファン、D,L−アラニン、D,L−セリンな
どが挙げられる。これらのD,L−アミノ酸はL−アミノ
酸を適当な手段を用いてラセミ化した後に用いることも
できる。ラセミ化方法としては、例えば加熱する方法、
ラセマーゼを使用する方法などが挙げられる。
The D, L-amino acid which can be used as the substrate of the present invention includes, for example, D, L-glutamic acid, D, L-valine, D, L-aspartic acid, D, L-methionine, D, L-leucine , D, L-isoleucine, D, L-histidine, D, L-
Arginine, D, L-phenylalanine, D, L-tyrosine,
D, L-tryptophan, D, L-alanine, D, L-serine and the like can be mentioned. These D, L-amino acids can also be used after racemizing the L-amino acids using a suitable means. As a racemization method, for example, a heating method,
Examples include a method using racemase.

【0011】本発明に使用できる酵素は、L−アミノ酸
に優先的又は特異的に作用してL−アミノ酸を他の化合
物に変化させ、当該化合物と残存するD−アミノ酸の物
理化学的性質などの違いによりこれらを分離できるもの
であれば何れも使用可能である。より好ましくはL−ア
ミノ酸を優先的又は特異的に酸化する酵素が使用でき
る。例えば、L−アミノ酸酸化酵素(EC 1.4.3.2)、L
−グルタミン酸酸化酵素(EC 1.4.3.11)、L−リジン
酸化酵素(EC 1.4.3.14)などが挙げられる。これらの
酵素はその基質特異性を加味し、基質として使用される
D,L−アミノ酸に対応して選択することができる。
The enzyme which can be used in the present invention acts on the L-amino acid preferentially or specifically to change the L-amino acid into another compound, and to determine the physicochemical properties of the compound and the remaining D-amino acid. Any of these can be used as long as they can be separated by the difference. More preferably, an enzyme that preferentially or specifically oxidizes L-amino acids can be used. For example, L-amino acid oxidase (EC 1.4.3.2), L
-Glutamate oxidase (EC 1.4.3.11), L-lysine oxidase (EC 1.4.3.14) and the like. These enzymes are used as substrates, taking into account their substrate specificity
It can be selected corresponding to the D, L-amino acid.

【0012】更に具体的には、既に報告されているCrot
alus adamanteus[J. Biol. Chem.,235, 2013-2018(196
0)]、Neurospora属[J. Biol. Chem., 50, 258-2268(1
951)]、Proteus属(特公昭45-16789)、Colletotrichu
m属(特公昭62-43671)、Streptomyces属(特公昭59-26
267)、Cryptococcus属(特公平5-61909、特公平6-46
939)、Trichoderma属(特開平8-509367)のL−アミノ
酸酸化酵素、Streptomyces属(特公昭59-26267、特公昭
61-26357、特公平4-28353)のL−グルタミン酸酸化酵
素、Trichoderema属[J. Biol. Chem., 255, 976-981(1
980)]のL−リジン酸化酵素等が使用できる。より好ま
しくはCrotalus adamanteus由来のL−アミノ酸酸化酵
素が使用できる。
More specifically, the previously reported Crot
alus adamanteus [J. Biol. Chem., 235, 2013-2018 (196
0)], genus Neurospora [J. Biol. Chem., 50, 258-2268 (1
951)], genus Proteus (JP-B-45-16789), Colletotrichu
Genus m (JP-B 62-43671), genus Streptomyces (JP-B 59-26)
267), genus Cryptococcus (Japanese Patent Publication 5-61909, Japanese Patent Publication 6-46)
939), L-amino acid oxidase of the genus Trichoderma (JP-A-8-509367), genus Streptomyces (JP-B-59-26267, JP-B-
L-glutamate oxidase of the genus Trichoderema [J. Biol. Chem., 255, 976-981 (1
980)] can be used. More preferably, L-amino acid oxidase derived from Crotalus adamanteus can be used.

【0013】本発明の反応の条件は、使用する酵素によ
り異なるが、通常pH7〜10、温度25〜55℃の範囲で実施
される。pHは、反応中のpH変動を、酸、アルカリを添加
しながらコントロールしてもよいが、通常トリス−塩酸
等の緩衝液を使用してもよい。反応後、目的とするD−
アミノ酸は、反応液を濃縮したりL−アミノ酸から生成
したオキソ酸とD−アミノ酸の各種溶媒に対する溶解性
の差を利用するなどの方法により、反応液から容易に分
離精製することができる。分離手段としてはろ過、或い
は遠心分離などの方法が利用できる。
The reaction conditions of the present invention vary depending on the enzyme used, but are usually carried out at a pH of 7 to 10 and a temperature of 25 to 55 ° C. The pH may be controlled by adding an acid or an alkali while controlling the pH fluctuation during the reaction, but a buffer such as Tris-hydrochloric acid may be usually used. After the reaction, the desired D-
Amino acids can be easily separated and purified from the reaction solution by methods such as concentrating the reaction solution or utilizing the difference in solubility of oxo acids and D-amino acids generated from L-amino acids in various solvents. As a separation means, a method such as filtration or centrifugation can be used.

【0014】試験例1 HPLCによるL−アミノ酸
とD−アミノ酸の分析 L−アミノ酸とD−アミノ酸分析は、0.1Mのロイシ
ン、イソロイシン、メチオニン、バリン、グルタミン
酸、フェニルアラニンの各D,L−アミノ酸を50mMトリ
ス−塩酸緩衝液(pH7.5)に溶解し、この溶液を精製水
で100倍希釈後、SUMICHIRAL AO-5000を用いて下記の条
件にてHPLCを行い、その溶出パターン、溶出時間及
びピーク面積より分析した。
Test Example 1 L-amino acid by HPLC
Analysis of L-amino acid and D-amino acid The L-amino acid and D-amino acid analysis was performed using 0.1 M leucine, isoleucine, methionine, valine, glutamic acid, and phenylalanine D, L-amino acids in 50 mM Tris-HCl buffer (pH 7.5). After dissolving and diluting this solution 100 times with purified water, HPLC was carried out using SUMICHIRAL AO-5000 under the following conditions, and the elution pattern, elution time and peak area were analyzed.

【0015】 Solvent - A : 2 mM CuSO4 / 5% Isopropylalcohol Solvent - B : 2 mM CuSO4 / 10% Isopropylalcohol Flow rate : 0.5 mL / min Absorbance : 254 nmSolvent-A: 2 mM CuSO4 / 5% Isopropylalcohol Solvent-B: 2 mM CuSO4 / 10% Isopropylalcohol Flow rate: 0.5 mL / min Absorbance: 254 nm

【0016】その結果、ロイシン、イソロイシン、メチ
オニン、バリン、グルタミン酸は、Solvent - A でD体
とL体の分離が可能であった。(図1から図5を参照)
また、フェニルアラニンは Solvent - B で 分離可能で
あった。(図6を参照)
As a result, it was possible to separate D-form and L-form of Solvent-A from leucine, isoleucine, methionine, valine and glutamic acid. (See FIGS. 1 to 5)
Phenylalanine could be separated by Solvent-B. (See Fig. 6)

【0017】試験例2 L−アミノ酸酸化酵素による
L−アミノ酸の分解 25mMの各種アミノ酸(D,L−アミノ酸:D,L−ロイシン、
D,L−イソロイシン、D,L−メチオニン、D,L−バリン、
およびD,L−フェニルアラニン)を各々50mM トリス−塩
酸緩衝液(pH7.5)1mlに溶解し、基質溶液とした。
Test Example 2 Using L-amino acid oxidase
Decomposition of L-amino acids 25 mM of various amino acids (D, L-amino acids: D, L-leucine,
D, L-isoleucine, D, L-methionine, D, L-valine,
And D, L-phenylalanine) were each dissolved in 1 ml of 50 mM Tris-HCl buffer (pH 7.5) to obtain a substrate solution.

【0018】この基質溶液にL−アミノ酸酸化酵素(Cr
otalus adamanteus由来;Sigma Type I、0.55u/mg)2m
gを添加し、30℃,17時間反応した後、1M−塩酸を60
μl添加して反応を停止し、沈殿物は遠心分離にて除去
した。反応液に未反応で残存するアミノ酸の光学体の種
類及びその量は、得られた上澄液を精製水にて100倍希
釈後HPLCにて求めた。
In this substrate solution, L-amino acid oxidase (Cr
from otalus adamanteus; Sigma Type I, 0.55u / mg) 2m
g, and reacted at 30 ° C. for 17 hours.
The reaction was stopped by adding μl, and the precipitate was removed by centrifugation. The type and amount of the optical form of the amino acid remaining unreacted in the reaction solution were determined by HPLC after diluting the obtained supernatant 100-fold with purified water.

【0019】その結果、D,L−ロイシン、D,L−イソロイ
シン、D,L−メチオニン、D,L− バリン、およびD,L−フ
ェニルアラニンのL体アミノ酸のみが、L−アミノ酸酸
化酵素と反応しほぼ完全に分解され、反応終了液中には
D−アミノ酸のみが未反応アミノ酸として残存すること
が明かとなった。(図7から図11を参照)
As a result, only the L-amino acid of D, L-leucine, D, L-isoleucine, D, L-methionine, D, L-valine and D, L-phenylalanine reacted with L-amino acid oxidase. It was almost completely decomposed, and it became clear that only D-amino acids remained as unreacted amino acids in the reaction completed solution. (See FIGS. 7 to 11)

【0020】試験例3 L−アミノ酸酸化酵素による
L−グルタミン酸の分解 25mM D,L−グルタミン酸を用いて、反応液のpHを7に調
整し、L−グルタミン酸酸化酵素を用いて試験例2と同
様に反応を行った。その結果、試験例2と同様にL−グ
ルタミン酸のみが分解され、D−グルタミン酸のみが反
応液中に未反応化合物として残存することが明かとなっ
た。(図12を参照)
Test Example 3 Using L-amino acid oxidase
Decomposition of L-glutamic acid The pH of the reaction solution was adjusted to 7 using 25 mM D, L-glutamic acid, and the reaction was carried out in the same manner as in Test Example 2 using L-glutamic acid oxidase. As a result, it became clear that only L-glutamic acid was decomposed and only D-glutamic acid remained as an unreacted compound in the reaction solution as in Test Example 2. (See FIG. 12)

【0021】以上の試験例1〜3により、各種D,L−ア
ミノ酸にL体アミノ酸に優先的又は特異的に作用するア
ミノ酸酸化酵素を作用させることにより、L−アミノ酸
のみを分解し、D−アミノ酸を反応液中に未反応化合物
として残存させることが可能であることが明かとなっ
た。また、反応開始時のアミノ酸濃度を溶解不可能な濃
度まで高めても反応はスムーズに進行し、反応終了液に
D−アミノ酸のみを未反応アミノ酸として残存させるこ
とも可能であった。
According to the above Test Examples 1 to 3, various D, L-amino acids are allowed to act on amino acid oxidase which acts preferentially or specifically on L-form amino acids, whereby only L-amino acids are decomposed and D-L-amino acids are decomposed. It has become clear that amino acids can be left as unreacted compounds in the reaction solution. The reaction proceeded smoothly even if the amino acid concentration at the start of the reaction was increased to a level at which it could not be dissolved, and it was possible to leave only D-amino acids as unreacted amino acids in the reaction-terminated liquid.

【0022】なお、本明細書中「%」はいずれも「重量
/容量(g/dl)」を意味するものとする。
In this specification, "%" means "weight / volume (g / dl)".

【0023】[0023]

【実施例】実施例1 0.1M D,L−ロイシンを50mM トリス−塩酸緩衝液(pH7.
5)50mlに溶解後、そのpHを7.5に調整し、基質溶液とし
た。この基質溶液にL−アミノ酸酸化酵素(Crotalus a
damanteus由来;Sigma Type I、0.55u/mg)100mgを添
加し、30℃で24時間反応した。
EXAMPLES Example 1 0.1 M D, L-leucine was added to 50 mM Tris-HCl buffer (pH 7.
5) After dissolving in 50 ml, the pH was adjusted to 7.5 to obtain a substrate solution. L-amino acid oxidase (Crotalus a
(derived from damanteus; Sigma Type I, 0.55 u / mg), and reacted at 30 ° C. for 24 hours.

【0024】その後、0.1Mに相当する各種D,L−アミノ
酸と100mgのL−アミノ酸酸化酵素(いずれも粉末状)
を24時間反応ごとに添加しながら4日間反応した。
Thereafter, various D, L-amino acids corresponding to 0.1 M and 100 mg of L-amino acid oxidase (all in powder form)
Was added for 24 hours, and the reaction was continued for 4 days.

【0025】その結果、共存するL−ロイシンはいずれ
も24時間以内にL−アミノ酸酸化酵素(100mg)によっ
てほぼ完全に分解され、4日間反応した反応液において
もL−ロイシンは完全に消失し、D−ロイシンのみが未
反応アミノ酸として残存した。(図13を参照)
As a result, the coexisting L-leucine was almost completely decomposed by L-amino acid oxidase (100 mg) within 24 hours, and L-leucine completely disappeared even in the reaction solution reacted for 4 days. Only D-leucine remained as an unreacted amino acid. (See FIG. 13)

【0026】また、D−ロイシンの残存量は98.7%であ
り、D−ロイシンは殆ど分解されなかった。また、反応
液に残存するD−ロイシンのうち、約50mMに相当する量
が既に結晶状に析出しており、反応液をさらに濃縮する
ことによりL−ロイシンを全く含有しないD−ロイシン
を析出させることができた。さらに、析出したD−ロイ
シンを濾過にて集め、常法により精製した。その結果、
回収率約95%で精製されたD−ロイシンを得ることがで
きた。
The residual amount of D-leucine was 98.7%, and D-leucine was hardly decomposed. In addition, of the D-leucine remaining in the reaction solution, an amount corresponding to about 50 mM has already been precipitated in a crystalline state, and the reaction solution is further concentrated to precipitate D-leucine containing no L-leucine at all. I was able to. Further, the precipitated D-leucine was collected by filtration and purified by a conventional method. as a result,
Purified D-leucine was obtained with a recovery of about 95%.

【0027】実施例2 D,L−イソロイシンを基質として用いて実施例1と同一
の条件でD−イソロイシンの調製を検討した。その結
果、0.1M L−イソロイシンも24時間以内にL−アミノ酸
酸化酵素(100mg)によってほぼ完全に分解され、4日
間反応した反応液においてもL−イソロイシンは完全に
消失し、D−イソロイシンのみが未反応アミノ酸として
残存した。(図13を参照)
Example 2 The preparation of D-isoleucine was examined under the same conditions as in Example 1 using D, L-isoleucine as a substrate. As a result, 0.1 ML-isoleucine was almost completely decomposed by L-amino acid oxidase (100 mg) within 24 hours, L-isoleucine completely disappeared even in the reaction solution reacted for 4 days, and only D-isoleucine remained unreacted. It remained as a reactive amino acid. (See FIG. 13)

【0028】また、D−イソロイシンの残存量は100%
であり、D−イソロイシンは全く分解されなかった。ま
た、反応液に残存するD−イソロイシンのうち、約20mM
に相当する量が既に結晶状に析出しており、反応液をさ
らに濃縮することによりL−イソロイシンを全く含有し
ないD−イソロイシンを析出させることができた。さら
に、析出したD−イソロイシンを濾過にて集め、常法に
より精製した。その結果、回収率約96%で精製されたD
−イソロイシンを得ることができた。
The residual amount of D-isoleucine is 100%
And D-isoleucine was not decomposed at all. In addition, of the D-isoleucine remaining in the reaction solution, about 20 mM
Was already precipitated in a crystalline form, and D-isoleucine containing no L-isoleucine could be precipitated by further concentrating the reaction solution. Further, the precipitated D-isoleucine was collected by filtration and purified by a conventional method. As a result, the purified D was recovered at a recovery rate of about 96%.
-Isoleucine could be obtained.

【0029】実施例3 D,L−メチオニンを基質として用いて実施例1と同一の
条件でD−メチオニンの調製を検討した。その結果、0.
1M L−メチオニンも24時間以内にL−アミノ酸酸化酵素
(100mg)によってほぼ完全に分解され、4日間反応し
た反応液においてもL−メチオニンは完全に消失し、D
−メチオニンのみが未反応アミノ酸として残存した。
(図13を参照)
Example 3 The preparation of D-methionine was examined under the same conditions as in Example 1 using D, L-methionine as a substrate. As a result, 0.
1M L-methionine is also almost completely decomposed by L-amino acid oxidase (100 mg) within 24 hours, L-methionine completely disappears even in the reaction solution reacted for 4 days, and D
-Only methionine remained as unreacted amino acid.
(See FIG. 13)

【0030】また、D−メチオニンの残存量は92.4%で
あり、D−メチオニンは全く分解されなかった。また、
反応液に残存するD−メチオニンのうち、結晶状に析出
している量は約4mMであったが、反応液を濃縮すること
によりL−メチオニンを全く含有しないD−メチオニン
を析出させることができた。さらに、析出したD−メチ
オニンを濾過にて集め、常法により精製した。その結
果、回収率約86%で精製されたD−イソロイシンを得る
ことができた。
The residual amount of D-methionine was 92.4%, and D-methionine was not decomposed at all. Also,
Of the D-methionine remaining in the reaction solution, the amount precipitated in a crystalline form was about 4 mM. However, by concentrating the reaction solution, D-methionine containing no L-methionine could be precipitated. Was. Further, the precipitated D-methionine was collected by filtration and purified by a conventional method. As a result, purified D-isoleucine was obtained at a recovery rate of about 86%.

【0031】実施例4 D,L−バリンを基質として用いて実施例1と同一の条件
でD−バリンの調製を検討した。その結果、0.1M L−
バリンも24時間以内にL−アミノ酸酸化酵素(100mg)
によってほぼ完全に分解され、4日間反応した反応液に
おいてもL−バリンは完全に消失し、D−バリンのみが
未反応アミノ酸として残存した。(図13を参照)
Example 4 The preparation of D-valine was examined under the same conditions as in Example 1 using D, L-valine as a substrate. As a result, 0.1M L-
Valine also within 24 hours L-amino acid oxidase (100mg)
And L-valine completely disappeared even in the reaction solution reacted for 4 days, and only D-valine remained as an unreacted amino acid. (See FIG. 13)

【0032】また、D−バリンの残存量は100%であ
り、D−バリンは全く分解されなかった。また、反応液
に残存するD−バリンのうち、結晶状に析出している量
は約3mMであったが、反応液を濃縮することによりL−
バリンを全く含有しないD−バリンを析出させることが
できた。さらに、析出したD−バリンを濾過にて集め、
常法により精製した。その結果、回収率約96%で精製さ
れたD−バリンを得ることができた。
The residual amount of D-valine was 100%, and D-valine was not decomposed at all. The amount of D-valine remaining in the reaction solution precipitated in a crystalline form was about 3 mM, but the L-valine was concentrated by concentrating the reaction solution.
D-valine containing no valine could be precipitated. Further, the precipitated D-valine was collected by filtration,
Purified by a conventional method. As a result, purified D-valine was obtained with a recovery of about 96%.

【0033】実施例5 D,L−フェニルアラニンを基質として用いて実施例1と
同一の条件でD−フェニルアラニンの調製を検討した。
その結果、0.1M L−フェニルアラニンも24時間以内に
L−アミノ酸酸化酵素(100mg)によってほぼ完全に分
解され、4日間反応した反応液においてもL−フェニル
アラニンはほぼ消失し、D−フェニルアラニンが未反応
アミノ酸として残存した。(図13を参照)
Example 5 The preparation of D-phenylalanine was examined under the same conditions as in Example 1 using D, L-phenylalanine as a substrate.
As a result, 0.1 M L-phenylalanine was almost completely decomposed by L-amino acid oxidase (100 mg) within 24 hours, L-phenylalanine almost disappeared even in the reaction solution reacted for 4 days, and D-phenylalanine was not reacted. It remained as an amino acid. (See FIG. 13)

【0034】また、D−フェニルアラニンの残存量は10
0%であり、D−フェニルアラニンは全く分解されなか
った。また、反応液に残存するD−フェニルアラニンの
うち、約48mMに相当する量が既に結晶状に析出してお
り、反応液をさらに濃縮することによりL−フェニルア
ラニンを全く含有しないD−フェニルアラニンを析出さ
せることができた。さらに、析出したD−フェニルアラ
ニンを濾過にて集め、常法により精製した。その結果、
回収率約95%で精製されたD−フェニルアラニンを得る
ことができた。
The residual amount of D-phenylalanine is 10
0%, indicating that D-phenylalanine was not decomposed at all. In addition, of the D-phenylalanine remaining in the reaction solution, an amount corresponding to about 48 mM has already been precipitated in a crystalline form, and the reaction solution is further concentrated to precipitate D-phenylalanine containing no L-phenylalanine at all. I was able to. Further, the precipitated D-phenylalanine was collected by filtration and purified by a conventional method. as a result,
Purified D-phenylalanine was obtained with a recovery of about 95%.

【0035】実施例6 L−フェニルアラニン 1.0gを2N−水酸化ナトリウム
50mlに溶解し、封管中150℃で5時間加熱した。放冷
後、この溶液を2N−塩酸で中和し、析出した結晶をろ
過、水洗し、乾燥した。得られた結晶は、ラセミ化され
たD,L−フェニルアラニンで、その比率は、D:L=4
6:54 であった。ここで得られたD,L−フェニルアラニ
ン 920mgを用いて、実施例5と同一の条件でD−フェニ
ルアラニンの調製を行った。その結果、415mgの精製さ
れたD−フェニルアラニンを得た。(L−フェニルアラ
ニンからの収率42%)
Example 6 1.0 g of L-phenylalanine was added to 2N sodium hydroxide
Dissolved in 50 ml and heated in a sealed tube at 150 ° C. for 5 hours. After cooling, the solution was neutralized with 2N-hydrochloric acid, and the precipitated crystals were filtered, washed with water, and dried. The resulting crystals are racemized D, L-phenylalanine, the ratio of which is D: L = 4
It was 6:54. Using 920 mg of D, L-phenylalanine obtained here, D-phenylalanine was prepared under the same conditions as in Example 5. As a result, 415 mg of purified D-phenylalanine was obtained. (42% yield from L-phenylalanine)

【0036】実施例7 D,L−グルタミン酸を基質として用いて実施例1と同一
の条件でD−グルタミン酸の調製を検討した。その結
果、0.1M L−グルタミン酸も24時間以内にL−アミノ
酸酸化酵素(100mg)によってほぼ完全に分解され、4
日間反応した反応液においてもL−グルタミン酸は完全
に消失し、D−グルタミン酸のみが未反応アミノ酸とし
て残存した。
Example 7 The preparation of D-glutamic acid was examined under the same conditions as in Example 1 using D, L-glutamic acid as a substrate. As a result, 0.1 M L-glutamic acid was almost completely decomposed by L-amino acid oxidase (100 mg) within 24 hours, and
Even in the reaction solution reacted for one day, L-glutamic acid completely disappeared, and only D-glutamic acid remained as an unreacted amino acid.

【0037】また、D−グルタミン酸の残存量は100%
であり、D−グルタミン酸は全く分解されなかった。ま
た、反応液に残存するD−グルタミン酸のうち、約48mM
に相当する量が既に結晶状に析出しており、反応液をさ
らに濃縮することによりL−グルタミン酸を全く含有し
ないD−グルタミン酸を析出させることができた。さら
に、析出したD−グルタミン酸を濾過にて集め、常法に
より精製した。その結果、回収率約92%で精製されたD
−グルタミン酸を得ることができた。
The residual amount of D-glutamic acid is 100%
And D-glutamic acid was not decomposed at all. In addition, of D-glutamic acid remaining in the reaction solution, about 48 mM
Was already precipitated in a crystalline state, and D-glutamic acid containing no L-glutamic acid could be precipitated by further concentrating the reaction solution. Further, the precipitated D-glutamic acid was collected by filtration and purified by a conventional method. As a result, the purified D was recovered at a recovery rate of about 92%.
-Glutamic acid could be obtained.

【0038】実施例8 安価なL−グルタミン酸 3gを200℃に4時間減圧下に
加熱することにより、D,L−ピログルタミン酸 2.25gが
得られた。これを、2N−塩酸で5時間加水分解を行う
ことにより、完全にラセミ化されたD,L−グルタミン酸
2.5gを得た。
Example 8 By heating 3 g of inexpensive L-glutamic acid at 200 ° C. for 4 hours under reduced pressure, 2.25 g of D, L-pyroglutamic acid was obtained. This was hydrolyzed with 2N-hydrochloric acid for 5 hours to obtain completely racemic D, L-glutamic acid.
2.5 g were obtained.

【0039】ここで得られたD,L−グルタミン酸 2.25g
を用いて実施例7と同一の条件でD−グルタミン酸の調
製を行った。その結果、1.03gの精製されたD−グルタ
ミン酸を得た。(L−グルタミン酸からの収率34%)
2.25 g of D, L-glutamic acid obtained here
Was used to prepare D-glutamic acid under the same conditions as in Example 7. As a result, 1.03 g of purified D-glutamic acid was obtained. (34% yield from L-glutamic acid)

【0040】[0040]

【発明の効果】以上、詳細に説明したように、本発明に
かかるL−アミノ酸酸化酵素を利用するD−アミノ酸の
製造法は、物性の異なる化合物への変換により反応液か
らの分離精製が可能となり、効率よく、目的とするD-ア
ミノ酸を得ることができるため、実用的な製造法を提供
するものである。
As described above in detail, the method for producing a D-amino acid using an L-amino acid oxidase according to the present invention enables separation and purification from a reaction solution by conversion into a compound having different physical properties. Thus, the objective D-amino acid can be obtained efficiently, so that a practical production method is provided.

【図面の簡単な説明】[Brief description of the drawings]

【図1】試験例1のD,L−ロイシンのHPLCの溶出パ
ターンを示す図である。
FIG. 1 is a view showing an HPLC elution pattern of D, L-leucine in Test Example 1.

【図2】試験例1のD,L−イソロイシンのHPLCの溶
出パターンを示す図である。
FIG. 2 is a view showing an HPLC elution pattern of D, L-isoleucine in Test Example 1.

【図3】試験例1のD,L−メチオニンのHPLCの溶出
パターンを示す図である。
FIG. 3 is a diagram showing an HPLC elution pattern of D, L-methionine in Test Example 1.

【図4】試験例1のD,L−バリンのHPLCの溶出パタ
ーンを示す図である。
FIG. 4 is a view showing an HPLC elution pattern of D, L-valine in Test Example 1.

【図5】試験例1のD,L−グルタミン酸のHPLCの溶
出パターンを示す図である。
FIG. 5 is a diagram showing an HPLC elution pattern of D, L-glutamic acid in Test Example 1.

【図6】試験例1のD,L−フェニルアラニンのHPLC
の溶出パターンを示す図である。
FIG. 6: HPLC of D, L-phenylalanine in Test Example 1
FIG. 3 is a view showing an elution pattern of the present invention.

【図7】試験例2のD,L−ロイシンを用いた場合のHP
LCの溶出パターンを示す図である。
FIG. 7 shows the HP of Test Example 2 using D, L-leucine.
It is a figure which shows the elution pattern of LC.

【図8】試験例2のD,L−イソロイシンを用いた場合の
HPLCの溶出パターンを示す図である。
FIG. 8 is a view showing an HPLC elution pattern when D, L-isoleucine of Test Example 2 is used.

【図9】試験例2のD,L−メチオニンを用いた場合のH
PLCの溶出パターンを示す図である。
FIG. 9 shows H in the case of using D, L-methionine in Test Example 2.
It is a figure which shows the elution pattern of PLC.

【図10】試験例2のD,L−バリンを用いた場合のHP
LCの溶出パターンを示す図である。
FIG. 10 shows the HP in Test Example 2 using D, L-valine.
It is a figure which shows the elution pattern of LC.

【図11】試験例2のD,L−フェニルアラニンを用いた
場合のHPLCの溶出パターンを示す図である。
FIG. 11 is a view showing an HPLC elution pattern when D, L-phenylalanine of Test Example 2 is used.

【図12】試験例3のD,L−グルタミン酸を用いた場合
のHPLCの溶出パターンを示す図である。
FIG. 12 is a view showing an elution pattern of HPLC when D, L-glutamic acid of Test Example 3 was used.

【図13】実施例1〜実施例5の結果を示す図である。FIG. 13 is a diagram showing the results of Examples 1 to 5.

【符号の説明】[Explanation of symbols]

図中で−●−はL−アミノ酸の残存量を示し、−○−は
D−アミノ酸の残存量を示す。
In the figure,-●-indicates the remaining amount of L-amino acid, and-○-indicates the remaining amount of D-amino acid.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】D,L−アミノ酸にL−アミノ酸に優先的又
は特異的に作用する酵素を作用させた後、D−アミノ酸
を分離することを特徴とするD−アミノ酸の製造法。
(1) A method for producing a D-amino acid, which comprises reacting an enzyme acting preferentially or specifically on an L-amino acid with a D, L-amino acid, and separating the D-amino acid.
【請求項2】L−アミノ酸に優先的又は特異的に作用す
る酵素がL−アミノ酸酸化酵素である請求項1記載のD
−アミノ酸の製造法。
2. The enzyme according to claim 1, wherein the enzyme which acts preferentially or specifically on L-amino acids is L-amino acid oxidase.
-A method for producing amino acids.
【請求項3】D,L−アミノ酸がL−アミノ酸よりラセミ
化反応により製造されものである請求項1或いは請求項
2記載のD−アミノ酸の製造法。
3. The method for producing a D-amino acid according to claim 1, wherein the D, L-amino acid is produced from the L-amino acid by a racemization reaction.
【請求項4】L−アミノ酸酸化酵素がCrotalus adamant
eus由来である請求項1又は請求項2記載のD−アミノ
酸の製造法。
4. The method according to claim 1, wherein the L-amino acid oxidase is Crotalus adamant.
The method for producing a D-amino acid according to claim 1 or 2, which is derived from eus.
JP28614797A 1997-10-01 1997-10-01 Method for producing D-amino acid Expired - Fee Related JP4125809B2 (en)

Priority Applications (1)

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Application Number Priority Date Filing Date Title
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Publication Number Publication Date
JPH11103887A true JPH11103887A (en) 1999-04-20
JP4125809B2 JP4125809B2 (en) 2008-07-30

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ID=17700554

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Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10337614A1 (en) * 2003-08-16 2005-03-17 Degussa Ag Process for the preparation of D-amino acids
JP2016223190A (en) * 2015-06-01 2016-12-28 積水化学工業株式会社 Through-hole cover, and fire protection construction of compartment through-hole

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10337614A1 (en) * 2003-08-16 2005-03-17 Degussa Ag Process for the preparation of D-amino acids
JP2016223190A (en) * 2015-06-01 2016-12-28 積水化学工業株式会社 Through-hole cover, and fire protection construction of compartment through-hole

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