JPH0260594A - Production method of α-acetamido-β-hydroxybutyric acid ester - Google Patents
Production method of α-acetamido-β-hydroxybutyric acid esterInfo
- Publication number
- JPH0260594A JPH0260594A JP21019088A JP21019088A JPH0260594A JP H0260594 A JPH0260594 A JP H0260594A JP 21019088 A JP21019088 A JP 21019088A JP 21019088 A JP21019088 A JP 21019088A JP H0260594 A JPH0260594 A JP H0260594A
- Authority
- JP
- Japan
- Prior art keywords
- acetamido
- acid ester
- hydroxybutyric acid
- production method
- 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
Links
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明はα−アセトアミド−アセト酢酸エステルを特定
のカビで処理して、α−アセトアミド−β−ヒドロキシ
酪酸エステルを製造する方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for producing α-acetamido-β-hydroxybutyrate by treating α-acetamido-acetoacetate with a specific mold.
[従来の技術]
α−アセトアミド−β−ヒドロキシ酪酸エステルはLス
レオニンを製造するための有用な原料である。[Prior Art] α-acetamido-β-hydroxybutyric acid ester is a useful raw material for producing L-threonine.
従来、かかる酪酸エステルを微生物学的に′fJ!造す
る方法として、例えばα−アセトアミド−アセト酢酸エ
ステルにサツカロミセス ロウキシ(Saccharo
myces rouxii)を作用さ仕る方法が知られ
ている。CHe l v、 Ch im、Ac t a
、、70゜232 (1987))[発明が解決しよう
とする課題]
しかし、かかる方法は目的物の収率が32%程度と低い
ため、実用的な製造方法としては満足出来ず、収率の高
い方法の開発が要望されている。Conventionally, such butyrate esters have been microbiologically evaluated as 'fJ! For example, α-acetamide-acetoacetic acid ester can be prepared using Saccharomyces waxi (Saccharomyces waxi).
myces rouxii). CHe l v, Ch im, Act a
,, 70° 232 (1987)) [Problems to be Solved by the Invention] However, this method has a low yield of the target product of about 32%, so it is not satisfactory as a practical manufacturing method, and the yield is low. There is a need for the development of sophisticated methods.
[課題を解決するための手段]
本発明者等は上記問題を解決するために鋭意研究を行っ
た結果、α−アセトアミド−アセト酢酸エステルにアル
テナリア属、アスペルギルス属、オーレオバソディウム
属、セファロスポリウム属、エメリセロプシス属、フザ
リウム属、ジベレラ属、ヒポミセス属、ロドセプトリア
属、トリコデルマ属から選ばれるカビの少なくとも一種
を作用させる場合、収率良くα−アセトアミド−β−ヒ
ドロキノ酪酸エステルを製造し得ることを見出し本発明
を完成するに至った。[Means for Solving the Problems] As a result of intensive research in order to solve the above problems, the present inventors have found that α-acetamido-acetoacetate contains Altenaria sp., Aspergillus sp., Aureobasodium sp., Cephalosporium sp. We have found that α-acetamido-β-hydroquinobutyric acid ester can be produced with good yield when at least one mold selected from the genus Emericelopsis, Fusarium, Gibberella, Hypomyces, Rhodoceptria, and Trichoderma is used. The present invention has now been completed.
本発明で用いる出発原料のα−アセトアミド−アセト酢
酸エステルは一般式CCH3C0CHCOOR)NHC
OCI−I3
で示される化合物で、Rは通常アルキル基である。アル
キル基としては炭素数1から10程度のもの例えばメチ
ル、エチル、プロピル、ブチル、アミル、ヘキシル、ヘ
ブヂル、オクチル等が上げられる。The starting material α-acetamide-acetoacetate used in the present invention has the general formula CCH3C0CHCOOR)NHC.
In the compound represented by OCI-I3, R is usually an alkyl group. Examples of the alkyl group include those having about 1 to 10 carbon atoms, such as methyl, ethyl, propyl, butyl, amyl, hexyl, hebutyl, octyl, and the like.
又、本発明で用いるカビとしては、アルテナリア マリ
(Alternaria maxi) (I F O8
984〕、アスペルギルス ソジャx (Asperg
illus 5ojae) CT FO4389〕、オ
ーレオバンプイウム プルランス(Aureobasi
dium pullulams) CI Fo 4
464 ) 、セファ(7スボリウム クリソゲナム(
Cephalosporium chrysogenu
n)CIFO30055)、エメリセロプシス フミコ
ラ(Emericellopsis humicola
) (I F 0 8518 )、フザリウム サム
ブシナム(Fusarium sumbucinum)
(ATCC24384)、ジベレラ フジクロイ(Gi
bberella rujikuroi) (ATC
C14164)、ヒポミセス ロセルス(Ilypom
yces rosellus) (A T CC+6
240)、aドセプトリア S P (Rhodose
ptoriasp、)CATCC11833:l、トリ
コデルマ ビリデ(Trichoderma vird
e) CI F O5720〕等が挙げられる。α−
アセトアミド−アセト酢酸エステルとの反応は水系(水
、生理食塩水、バッファー液、培地等)にカビを分散さ
せ、エネルギー源として糖類を添加し、次いで該エステ
ルを加えて10〜70℃好ましくは20〜40℃で0.
1〜150時間、好ましくは1〜40時間程度振とう、
撹拌あるいは静置反応させれば良い。In addition, the mold used in the present invention is Alternaria maxi (I F O8
984], Aspergillus soja x
illus 5 ojae) CT FO4389], Aureobumpium pullulans (Aureobasi
CI Fo 4
464), Cepha (7 Suborium chrysogenum (
Cephalosporium chrysogenu
n) CIFO30055), Emerycellopsis humicola
) (IF 0 8518), Fusarium sumbucinum
(ATCC24384), Gibberella fujikuroi (Gi
bberella rujikuroi) (ATC
C14164), Hypomyces rosellus (Ilypom
yces rosellus) (AT CC+6
240), aDoseptria S P (Rhodose
ptoriasp,) CATCC11833:l, Trichoderma vird
e) CI FO5720] and the like. α−
For the reaction with acetamide-acetoacetate, mold is dispersed in an aqueous system (water, physiological saline, buffer solution, culture medium, etc.), sugar is added as an energy source, and then the ester is added to the mixture at 10 to 70°C, preferably 20°C. 0 at ~40°C.
Shaking for 1 to 150 hours, preferably 1 to 40 hours,
The reaction may be carried out by stirring or standing still.
系のP I−(は3〜IO好ましくは4〜8が適当であ
る。PI-(of the system) is suitably 3 to IO, preferably 4 to 8.
又、カビを別途固定化して作用せしめる等゛の任彦の方
法が採用される。反応形式としてはバッチ方式あるいは
固定化された微生物を管や塔に充填しα−アセトアミド
アセト酢酸エステルを流下させる連続方式等任偉の手段
が採用出来る。In addition, a method such as that of immobilizing mold separately and making it work is adopted. As the reaction method, a batch method or a continuous method in which immobilized microorganisms are packed in a tube or column and α-acetamidoacetoacetic ester is allowed to flow down can be adopted.
かかる反応時の媒体は水のみならず水と相溶性のある有
機溶媒例えばアルコール、アセトン等の水/有機溶媒混
合系が用いられる。微生物に対して害とならない有機溶
媒を選択することは勿論必要である。As a medium for such a reaction, not only water but also an organic solvent compatible with water, such as a mixed water/organic solvent system such as alcohol or acetone, is used. It is of course necessary to select an organic solvent that is not harmful to microorganisms.
系に対しα−アセトアミド−アセト酢酸エステルはその
ままあるいは有機溶媒に溶解あるいは分散させて添加さ
れる。該エステルの系中濃度は通常0.01〜30重屯
%好ましくはO1〜10重量%が適当である。更に該エ
ステルとカビの重量比(乾燥重量)は1以下、好ましく
は001〜0.8程度が有利である。α-acetamido-acetoacetate is added to the system as it is or after being dissolved or dispersed in an organic solvent. The concentration of the ester in the system is usually 0.01 to 30% by weight, preferably 1 to 10% by weight. Further, it is advantageous that the weight ratio (dry weight) of the ester and mold is 1 or less, preferably about 0.001 to 0.8.
反応時にグルコース等の糖類や他の栄養素を共存させて
も差し支えない。かかる糖類や他の栄養素の添加は反応
の任意の段階で可能であり、−括、連続、分割のいずれ
の手段も実胞出来る。又、必要に応じてフッ化フェニル
メチルスルホニル等のエステラーゼ阻害剤を適宜添加し
ても良い。There is no problem in allowing sugars such as glucose and other nutrients to coexist during the reaction. Such sugars and other nutrients can be added at any stage of the reaction, and can be carried out in bulk, continuously or in portions. Furthermore, an esterase inhibitor such as phenylmethylsulfonyl fluoride may be added as appropriate.
反応終了後はカビを遠心分離等の常法に従って分離し、
が液をエーテル、四塩化炭素、ベンゼン等の有機溶媒を
用いて抽出する。After the reaction is complete, separate the mold using conventional methods such as centrifugation.
The liquid is extracted using an organic solvent such as ether, carbon tetrachloride, or benzene.
抽出液から溶媒を溜去することによってα−アセトアミ
ド−β−ヒドロキシ酪酸エステルが得られる。α-acetamido-β-hydroxybutyric acid ester is obtained by distilling off the solvent from the extract.
[作 用][効 果]
本発明においてはα−アセトアミド−β−ヒドロキシ酪
酸エステルが50%以上の高収率で得られるので、該方
法は工業的に極めて意義が高い上、該エステルはスレオ
ニンの中間体として有用なものである。[Function] [Effect] In the present invention, α-acetamido-β-hydroxybutyric acid ester can be obtained in a high yield of 50% or more. It is useful as an intermediate for
[実施例コ 次に実例を挙げて本発明の方法を詳しく説明する。[Example code] Next, the method of the present invention will be explained in detail by giving examples.
実施例1〜IO
サブロー培地(ブドウ糖40g、ペプトンI09、水I
QSP)−16)5mlを試験管にとり、所定のカビを
1白金耳接種して30℃で72時間振とう培養し、種培
養液を得た。Example 1 ~ IO Sabouraud medium (40 g glucose, peptone I09, water I
QSP)-16) 5 ml was placed in a test tube, one platinum loop of the specified mold was inoculated, and cultured with shaking at 30°C for 72 hours to obtain a seed culture solution.
次に同組成の培地100m1を500m1容坂ロフラス
コにとり、種培養液を5mlを接種して30℃で72時
間振とう培養を行った。培養後集画しP H7の0.1
モルリン酸バッファーで1回洗浄して菌体(we t)
4.5?を得た。Next, 100 ml of a medium having the same composition was placed in a 500 ml Sakaro flask, 5 ml of the seed culture was inoculated, and cultured with shaking at 30° C. for 72 hours. After culturing, collect and collect PH7 of 0.1
Wash the cells once with molar phosphate buffer (wet).
4.5? I got it.
同バッファー10m1を30m1容り字管にとり、菌体
49を入れ菌@濁液を製造した。10 ml of the same buffer was placed in a 30 ml tube, and 49 bacterial cells were added thereto to produce a bacterial suspension.
続いて、α−アセトアミド−アセト酢酸エステルを菌懸
濁液に対して1%(w/v)添加し30℃で24時間振
とう反応を行った。Subsequently, 1% (w/v) of α-acetamide-acetoacetate was added to the bacterial suspension, and a shaking reaction was performed at 30° C. for 24 hours.
反応後、酢酸エチルにて基質及び生成物を抽出しロータ
リーエバポレーターにて酢酸エチルを留去して目的物(
αアセトアミド−β−ヒドロキシ酪酸エステル)を得た
。After the reaction, the substrate and product are extracted with ethyl acetate, and the ethyl acetate is distilled off using a rotary evaporator to obtain the target product (
α-acetamide-β-hydroxybutyric acid ester) was obtained.
該目的物を高速液クロ法にて分析し収率を求めた。The target product was analyzed by high performance liquid chromatography to determine the yield.
これらの結果を表に示す。These results are shown in the table.
高速液りaの測定条件は以下の遺りである。The measurement conditions for high-speed liquid a are as follows.
カラム・0PP−50461111110−溶出液;
CH2ON/H,0(1/9 )流速; 0 、5 m
l/lN1n
検出、R1
5m1LColumn・0PP-50461111110-eluate;
CH2ON/H, 0 (1/9) flow rate; 0, 5 m
l/lN1n detection, R1 5m1L
Claims (1)
ア属、アスペルギルス属、オーレオバシディウム属、セ
ファロスポリウム属、エメリセロプシス属、フザリウム
属、ジベレラ属、ヒポミセス属、ロドセプトリア属、ト
リコデルマ属から選ばれるカビの少なくとも一種を作用
させることを特徴とするα−アセトアミド−β−ヒドロ
キシ酪酸エステルの製法。α-acetamide-acetoacetate and at least one mold selected from the genus Altenaria, Aspergillus, Aureobasidium, Cephalosporium, Emeryseropsis, Fusarium, Gibberella, Hypomyces, Rhodoseptria, and Trichoderma. 1. A method for producing α-acetamido-β-hydroxybutyric acid ester.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21019088A JPH0260594A (en) | 1988-08-24 | 1988-08-24 | Production method of α-acetamido-β-hydroxybutyric acid ester |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21019088A JPH0260594A (en) | 1988-08-24 | 1988-08-24 | Production method of α-acetamido-β-hydroxybutyric acid ester |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0260594A true JPH0260594A (en) | 1990-03-01 |
Family
ID=16585274
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP21019088A Pending JPH0260594A (en) | 1988-08-24 | 1988-08-24 | Production method of α-acetamido-β-hydroxybutyric acid ester |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0260594A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007029089A (en) * | 2005-06-24 | 2007-02-08 | Api Corporation | Method for producing optically active hydroxyamino acid derivative |
-
1988
- 1988-08-24 JP JP21019088A patent/JPH0260594A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007029089A (en) * | 2005-06-24 | 2007-02-08 | Api Corporation | Method for producing optically active hydroxyamino acid derivative |
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