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JPS6327477A - Production of oxiracetam - Google Patents

Production of oxiracetam

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Publication number
JPS6327477A
JPS6327477A JP16776986A JP16776986A JPS6327477A JP S6327477 A JPS6327477 A JP S6327477A JP 16776986 A JP16776986 A JP 16776986A JP 16776986 A JP16776986 A JP 16776986A JP S6327477 A JPS6327477 A JP S6327477A
Authority
JP
Japan
Prior art keywords
oxiracetam
glycinamide
solvent
acid ester
mixture
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
JP16776986A
Other languages
Japanese (ja)
Inventor
Hideki Hirano
秀樹 平野
Hiroshi Kaneko
博 金子
Tsunehiko Shimizui
清水井 恒彦
Kyoji Aoki
青木 恭二
Toshiro Uchida
内田 寿郎
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.)
Denka Co Ltd
Original Assignee
Denki Kagaku Kogyo KK
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 Denki Kagaku Kogyo KK filed Critical Denki Kagaku Kogyo KK
Priority to JP16776986A priority Critical patent/JPS6327477A/en
Publication of JPS6327477A publication Critical patent/JPS6327477A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To obtain the titled compound useful as a cerebral metabolism improver, in short steps at a low cost, by using a halogenoacetic acid ester and ammonia as easily and inexpensively available raw materials and passing through glycinamide and oxiracetam as intermediates. CONSTITUTION:A halogenoacetic acid ester is made to react with preferably 3-50mol, especially 10-30mol of ammonia (based on 1mol of the ester) at 10-100 deg.C in the presence of a solvent (preferably an aliphatic alcohol) and the reaction mixture is concentrated to obtain glycinamide, its salt or their mixture. The above glycinamide, etc., is reacted with 4-chloro-3-hydroxybutyric acid ester of formula (R is lower alkyl) in a solvent (especially preferably ethanol) preferably in the presence of a neutralizing agent at 60-160 deg.C. The obtained liquid containing oxiracetam is filtered to remove insoluble components and concentrated to obtain the objective compound as precipitate.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、医薬(脳代謝改善剤)として矧られるオキシ
ラセタム(4−ヒドロキシ−2−オキシ−1−ピロリジ
ンアセトアミド)の製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for producing oxiracetam (4-hydroxy-2-oxy-1-pyrrolidine acetamide), which is used as a medicine (brain metabolism improving agent).

〔従来の技術〕[Conventional technology]

従来、本発明で目的とするオキシラセタムの合成法とし
ては、け)イミノジ酢酸エチルとエトキシカルポニルア
セチルクロリドヲ原刺とし、5工程の反応によって得る
方法〔特公昭58−22054号公報〕および(2)γ
−アミノーβ−ヒドロキシ酪酸t−m料とし、それにヘ
キサメチルジシラデンなどを反応させた後、3工程の反
応を経て得る方法(特開昭53−101 !167号公
報)、が仰られている。
Conventionally, methods for synthesizing oxiracetam, which is the object of the present invention, include a method in which ethyl iminodiacetate and ethoxycarponylacetyl chloride are used as base materials and obtained through a five-step reaction [Japanese Patent Publication No. 58-22054] and (2) )γ
- Amino-β-hydroxybutyric acid t-m material is reacted with hexamethyldisiladene, etc., and then a three-step reaction is performed (Japanese Unexamined Patent Publication No. 53-101!167). .

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

従来の方法は、いずれも、用いる原料が同価であり、ま
た、多工程の反応t−iするなどの欠点を有している。
All of the conventional methods have drawbacks such as using the same raw materials and requiring multiple reaction steps.

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

本発明は、下記(1)、(21及び(3)工程よりなる
オキシラセタムの製造方法である。
The present invention is a method for producing oxiracetam comprising the following steps (1), (21 and (3)).

(1)溶剤存在下、ハロデノ酢酸エステルt1アンモニ
アと反応させ、反応液を濃縮し、グリシンアミド、その
塩又はそれらの混合物を得るグリシンアミド製造工程 (2)前記グリシンアミド、その塩又はそれらの混合物
を溶剤存在下、一般式 %式% (Rは低級アルキル基を表わす) で表わされる4−クロロ−5−ヒドロキシ酪酸エステル
と反応させ、オキシラセタム含有液ヲ得るオキシラセタ
ム化工程 (aJ  titl記液を不浴物の濾過後濃縮し、析出
するオキシラセタム七得る単離工程 本発明により、従来の製造法に比較して容易でかつ安価
に入手できる涼料金用い、2段の容易な反応工程により
、オキシラセタムが得られる。
(1) Glycinamide manufacturing process in which the halidenoacetate t1 is reacted with ammonia in the presence of a solvent and the reaction solution is concentrated to obtain glycinamide, its salt, or a mixture thereof (2) The glycinamide, its salt, or a mixture thereof is reacted with 4-chloro-5-hydroxybutyric acid ester represented by the general formula % (R represents a lower alkyl group) in the presence of a solvent to obtain an oxiracetam-containing liquid (aJ titl liquid) According to the present invention, an isolation process for obtaining Oxiracetam 7, which is obtained by concentrating and precipitating Oxiracetam after filtration of the unbath product, is carried out by a two-step easy reaction process using a coolant that is easier and cheaper to obtain than in conventional production methods. , Oxiracetam is obtained.

各工程について、以下、詳細に説明する。Each step will be described in detail below.

本工程では、溶剤存在下ハロデノ酢酸エステルを、アン
モニアと反応させ、反応液を凝縮し、グリシンアミド又
はその塩を得る。本発明で使用するハロゲノ酢酸エステ
ルは、特に制限はないが、クロロ酢酸メチル、クロロ酢
酸エチル、クロロ酢酸プロざル、ブロモ酢酸メチル、ブ
ロモ酢酸エチル、ブロモ酢酸プロピルが工業的に容易に
入手できるので好ましい。アンモニアは、ハロデノ酢酸
エステルに対して、3〜50倍、好ましくは、10〜3
0倍モル使用される。少なすぎると、イミノジ酢酸アミ
ドが多量に生成し、多すぎても効果がない。
In this step, harodenoacetic acid ester is reacted with ammonia in the presence of a solvent, and the reaction solution is condensed to obtain glycinamide or a salt thereof. The halogenoacetate used in the present invention is not particularly limited, but methyl chloroacetate, ethyl chloroacetate, prozal chloroacetate, methyl bromoacetate, ethyl bromoacetate, and propyl bromoacetate are easily available industrially. preferable. Ammonia is 3 to 50 times, preferably 10 to 3 times as much as the harodenoacetic ester.
0 times molar amount is used. If it is too small, a large amount of iminodiacetic acid amide will be produced, and if it is too large, there will be no effect.

又杢糸に、触媒的に、ヘキサメチレンテトラミンを添加
するとアンモニア量を軽減する事ができる。
Furthermore, the amount of ammonia can be reduced by adding hexamethylenetetramine to the heathered yarn as a catalyst.

本発明の方法を実施するに当っては、オートクレーブ中
で、設定温度下、−括仕込あるいはハロデノ酢酸エステ
ルを分添し反応全行なう。
In carrying out the method of the present invention, the entire reaction is carried out in an autoclave at a predetermined temperature by either bulk charging or partial addition of halidenoacetic ester.

反応温度は一10〜100℃、特に0〜80℃がよい。The reaction temperature is preferably -10 to 100°C, particularly 0 to 80°C.

これより低温では反応が遅く、高温では選択性が上がら
ない。
At lower temperatures, the reaction is slow, and at higher temperatures, selectivity does not increase.

本発明は、溶剤の使用が好ましい。溶剤としては特に制
限はなく、アンモニア水が工業的に最も入手しやすいが
、反応後アルコールが生成するために、それと同一のB
肪族アルコール溶剤を用いた方が反応後の溶剤回収、再
利用に有利である。
The present invention preferably uses a solvent. There are no particular restrictions on the solvent, and aqueous ammonia is the easiest to obtain industrially, but since alcohol is produced after the reaction, the same B
Using an aliphatic alcohol solvent is more advantageous in terms of solvent recovery and reuse after the reaction.

反応液より、グリシンアミド又はその場會隼離する方法
としては、特に制限はないが、前記アミノ化液を脱アン
モニアさらに濃縮脱溶剤し、グリシンアミド又はその塩
を析出させる事ができる。
The method of separating glycinamide or its salt from the reaction solution is not particularly limited, but the amination solution can be deammoniated, further concentrated and desolvented to precipitate glycinamide or its salt.

生成物は、濃縮途中で一過するかあるいは脱溶剤後アル
コールにより洗浄する事によって、比較的純度の高い生
成物が得られる。しかし、本発明によれば、脱溶剤後の
グリシンアミド又はその塩あるいはそれらの混合物を特
に′1′ft製する事なく、イミノジ酢酸アミド、塩化
アンモニウム等の副生成物を含んだまま、次のオキシラ
セタム化工程に使用する事ができる。
A product with relatively high purity can be obtained by passing the product through during concentration or by washing with alcohol after removing the solvent. However, according to the present invention, glycinamide, its salt, or a mixture thereof after desolventization is not particularly produced in 1'ft. It can be used in the oxiracetamization process.

2、オキシラセタム化工程 本工程では、 前記グリシンアミドあるいはその塩、又はそれらの混合
物全溶剤存在下、一般式 %式% (Rは低級アルキル基を表わす) で表わされる。4−クロロ−3−ヒドロキシ酪酸エステ
ルと反応させ、オキシラセタム含Wi ’kWる。
2. Oxiracetamization step In this step, the glycinamide, its salt, or a mixture thereof is expressed by the general formula % (R represents a lower alkyl group) in the presence of a total solvent. It is reacted with 4-chloro-3-hydroxybutyric acid ester and contains oxiracetam.

本発明の方法において原料となる4−クロロ−3−ヒド
ロキシ酪酸エステルは、例えば、工業原料として安価に
入手し得るエビクロロヒドリンのカルボニル化反応によ
って容易に調造される(特開昭56−68644号公報
)。
4-chloro-3-hydroxybutyric acid ester, which is a raw material in the method of the present invention, is easily prepared, for example, by carbonylation reaction of shrimp chlorohydrin, which is inexpensively available as an industrial raw material (Japanese Patent Application Laid-open No. 68644).

Rは低級アルキル基であれば、特に制限はないが、1造
過程で脱離していく置換基であ夛、炭素数4以上では経
済的でない。従って、炭素数1〜6が好しい。
There is no particular restriction on R as long as it is a lower alkyl group, but R is a substituent that is eliminated during one production process, and it is not economical to use it with 4 or more carbon atoms. Therefore, it is preferable to have 1 to 6 carbon atoms.

本発明の方法ヲ芙施するに当っては、溶媒の使用が望ま
しく、水、メタノール、エタノール、プロパツール、ブ
タノール、2−メトキシエタノールの如きプロトン性溶
媒およびジオキサン、1゜2−ジメトキシエタン、ジグ
ライムの如!エーテル系溶媒、ならびにこれらの混合溶
媒を用いることができるが、プロトン性溶媒が望ましく
、特にエタノールが望ましい。
In carrying out the method of the present invention, it is desirable to use solvents, such as water, protic solvents such as methanol, ethanol, propatool, butanol, 2-methoxyethanol, and dioxane, 1.2-dimethoxyethane, diglyme, etc. Like! Ether solvents and mixed solvents thereof can be used, but protic solvents are preferred, and ethanol is particularly preferred.

本反応中、ハロゲン化水素が副生じてくるが、このハロ
ゲン化水素は、反応速度を減少させるため中和剤を加え
た万が好ましい。中和用無機塩基としては、水酸化ナト
リウム、水酸化カリウム、水酸化カルシウムの如きアル
カリ金属またはアルカリ土類金属の水酸化物2よび炭酸
ナトリウム、炭市水素ナトリウム、炭酸カリウムの如き
アルカリ金属炭酸塩を用い得るが、収率および経済性全
考慮すると、アルカリ金属炭#I塩が望ましく、特に炭
酸ナトリウムが望ましい。
During this reaction, hydrogen halide is produced as a by-product, but it is preferable to add a neutralizing agent to this hydrogen halide in order to reduce the reaction rate. Inorganic bases for neutralization include alkali metal or alkaline earth metal hydroxides such as sodium hydroxide, potassium hydroxide, and calcium hydroxide, and alkali metal carbonates such as sodium carbonate, sodium bicarbonate, and potassium carbonate. However, in consideration of yield and economy, alkali metal carbon #I salts are preferred, and sodium carbonate is particularly preferred.

有機塩基としては、アミン類たとえば、アンモニア、ト
リエチルアミン、ジメチルアニリン、グリシンアミドが
用いられる。
As the organic base, amines such as ammonia, triethylamine, dimethylaniline, and glycinamide are used.

反応温度は、60〜160°C1好ましくは70〜13
0℃であり、反応時間は、温度その他の条件によシ、1
〜70時間である。なお、触媒量のヨウ化カリウム、ヨ
ウ化ナトリウムの如きヨウ化物が本反応を促進する。
The reaction temperature is 60-160°C, preferably 70-13°C.
The temperature is 0°C, and the reaction time varies depending on the temperature and other conditions.
~70 hours. Note that a catalytic amount of iodide such as potassium iodide and sodium iodide promotes this reaction.

3、単離工程 前記反応液を、析出塩を濾過後濃縮し、冷却後析出して
いるオキシラセタムt?[過して得る、漠縮は、オキシ
ラセタムt?10〜50%、好ましくは、20〜30%
まで行なう。これ以下では、濾液への損失が大きく、こ
れ以上では不純物の混入が多くなる。
3. Isolation step The reaction solution is filtered to remove precipitated salts, concentrated, and cooled to remove the precipitated oxiracetam t? [Oxiracetam t? 10-50%, preferably 20-30%
I will do it up to If the amount is less than this, the loss to the filtrate will be large, and if it is more than this, more impurities will be mixed in.

溶剤が水の場合は、オキシラセタムの溶解度が^すぎる
ため、可能なかぎり水?除き、次いでオキシラセタムの
溶解度の低い溶媒たとえば、脂肪族アルコールで処理し
てオキシラセタムで得る。
If the solvent is water, the solubility of oxiracetam is too high, so use water as much as possible. Oxiracetam is obtained by removing and then treating with a solvent in which oxiracetam has low solubility, such as an aliphatic alcohol.

この状態の同感を、洗浄する事によって純度の高いオキ
シラセタムが得られる。洗浄剤としては特に制限はない
が、沸点が低く、乾燥の容易なメタノール、アセトン、
エタノール、プロパツールが好ましい。洗浄剤のiは、
0.5〜6倍、好1しくは、1〜2倍重黛f!用する。
Highly pure oxiracetam can be obtained by washing the same substance in this state. There are no particular restrictions on cleaning agents, but methanol, acetone, and
Ethanol and propatool are preferred. The i of the cleaning agent is
0.5 to 6 times, preferably 1 to 2 times as heavy! use

これより少ないと洗沖効来がなく2多いと、aI!を液
への損失が大きくなる。
If it is less than this, there will be no washing effect, and if there are 2 more, aI! The loss to the liquid will be greater.

さらに筒純度のオキシラセタムを祷るためには、たとえ
ばオキシラセタムを水浴液に希釈し、イオン交換樹脂処
理により完全に脱塩し、さらに活性灰処理により脱色す
る方法がある。イオン交換樹脂は、特に制約はなく市販
の強酸性イオン交換樹脂でよい。このイオン交換樹脂処
理は、反応液の析出塩m、通過後の一!ま行なう事も可
能であるが、これがイオン交A4N脂がその反応浴剤下
において使用可能な場合に限られる。活性炭も特に制限
はなく、市販のもので十分である。活性炭処理液を濃縮
し貧溶剤を加え、冷却後析出し、オキシラセタムtl−
1i1&過して得る。貧溶剤としては、水に可溶で、オ
キシラセタムが不溶であれば、特に問題はないが性成物
の乾kが容易なため、沸点の低い脂肪族低級アルコール
類たとえば、メタノール、エタノール、イングロパノー
ル又は、脂肪族低級ケトン類、アセトン、メチルエチル
ケトン及びジエチルケトン等が好ましい。
Furthermore, in order to obtain oxiracetam with pure purity, there is a method in which, for example, oxiracetam is diluted in a water bath, completely desalted by treatment with an ion exchange resin, and further decolorized by treatment with activated ash. The ion exchange resin is not particularly limited and may be a commercially available strong acidic ion exchange resin. In this ion exchange resin treatment, the precipitated salt m of the reaction solution is reduced to 1 after passing through it. It is also possible to do so, but only if the ionic A4N resin can be used in the reaction bath. Activated carbon is also not particularly limited, and commercially available ones are sufficient. The activated carbon treatment solution was concentrated, a poor solvent was added, and after cooling, it was precipitated and oxiracetam tl-
1i1 & get it. As a poor solvent, there is no particular problem as long as it is soluble in water and oxiracetam is insoluble, but since the chemical product dries easily, aliphatic lower alcohols with a low boiling point, such as methanol, ethanol, and oxiracetam, are recommended. Panol, aliphatic lower ketones, acetone, methyl ethyl ketone, diethyl ketone, etc. are preferred.

〔実施例〕〔Example〕

以下、実施例により更に詳゛シ<説明する。 Further details will be explained below with reference to Examples.

実施例1 クロロ酢酸メチル(108,5g、1モル)および20
チアンモニア−メタノールfa−1ft < 1.27
59 % NH3トして15モル)(クロロ酢酸メチル
/アンモニア−1/15:モル比) オートクレーブ中撹拌しながら、40℃に15時間加熱
する。反応後、液体クロマトグラフィー(以下HLOと
略す)で定量したところ、グリシンアミドが7661%
、イミノジ酢酸アミドが19.6チ生成した事がわかっ
た。
Example 1 Methyl chloroacetate (108.5 g, 1 mol) and 20
Thiammonia-methanol fa-1ft < 1.27
59% NH3 (15 mol) (methyl chloroacetate/ammonia - 1/15: molar ratio) Heated to 40°C for 15 hours with stirring in an autoclave. After the reaction, quantification using liquid chromatography (hereinafter abbreviated as HLO) revealed that glycinamide was 7661%.
It was found that 19.6 units of iminodiacetic acid amide were produced.

反応i’ti縮する事によってグリシンアミド0.77
モル含む白色固体が130!!得られた。
By condensing the reaction i'ti glycinamide 0.77
The white solid containing moles is 130! ! Obtained.

実施例2 実施例1によって得られた固体84.4 、? (グリ
シンアミド0.5モル含b) 、4−10ロー6−ヒド
ロキシ酪酸メチル(76,511,0,5モル)、炭酸
ナトリウム(53,9,0,5モル)〔グリシンアミP
74−クロロー6−ヒドロキシ酪酸メチル/炭酸ナトリ
ウム−1/1/1 (モル比〕〕およびエタノールC5
009)k20時間還流した。反応液、HLO分析を行
なうと、オキシラセタムが53%の収率で得られている
事がわかった。
Example 2 Solid obtained according to Example 1 84.4, ? (contains 0.5 mol of glycinamide b), methyl 4-10 rho-6-hydroxybutyrate (76,511,0.5 mol), sodium carbonate (53,9,0.5 mol) [glycinamide P
Methyl 74-chloro-6-hydroxybutyrate/sodium carbonate-1/1/1 (molar ratio)] and ethanol C5
009) Refluxed for 20 hours. When the reaction solution was subjected to HLO analysis, it was found that oxiracetam was obtained in a yield of 53%.

実施例6 実施例2の反応液を濾過後、全量200gに濃縮すると
((縮率21%)オキシラセタムが析出してくる。5℃
に冷却し、濾過する事によって純度70チのオキシラセ
タムが50.8.9 (オキシラセタム35.6 、!
i’ )得られた。これをメタノール55g〔オキシラ
セタムに対して1.5倍重輩〕で型温下洗浄すると、純
度95チのオキシラでタム56.3 g(オキシラセタ
ム54.5 & )が得られた。
Example 6 After filtering the reaction solution of Example 2 and concentrating the total amount to 200 g (condensation rate 21%), oxiracetam precipitates out. 5°C
Oxiracetam with a purity of 70% is obtained by cooling to 50.8.9 (Oxiracetam 35.6,!
i') Obtained. This was washed with 55 g of methanol (1.5 times heavier than oxiracetam) under warm mold conditions to obtain 56.3 g of tam (oxiracetam 54.5 & ) with a purity of 95%.

これを20チ水溶液希釈、強酸性イオン交換樹脂処理、
および活性炭処理した。全量55gに礫縮し、メタノー
ル779に加え、0°Cに冷却するとオキシラセタムが
析出してきた。結晶を集め、真空乾燥するとオキシラセ
タム28g(単離収率35−4%、融点161〜163
°C)k得た。
This was diluted with 20% aqueous solution, treated with strong acidic ion exchange resin,
and treated with activated carbon. The mixture was condensed to a total amount of 55 g, added to 779 g of methanol, and cooled to 0°C. Oxiracetam was precipitated. The crystals were collected and dried under vacuum to yield 28 g of oxiracetam (isolated yield 35-4%, melting point 161-163).
°C) was obtained.

〔発明の効果〕〔Effect of the invention〕

本発明の方法により、容易かつ安価に入手できる原料か
ら短かい反応工程により工業的に有利にオキシラセタム
t−製造する。
By the method of the present invention, oxiracetam t- is industrially advantageously produced from easily and inexpensively available raw materials through short reaction steps.

Claims (1)

【特許請求の範囲】 下記(1)、(2)及び(3)工程よりなるオキシラセ
タムの製造方法。 (1)溶剤存在下ハロゲノ酢酸エステルを、アンモニア
と反応させ、反応液を濃縮し、グリシンアミド、その塩
、又はそれらの混合物を得るグリシンアミド製造工程 (2)前記グリシンアミド、その塩又はそれらの混合物
を溶剤存在下、一般式 ▲数式、化学式、表等があります▼ (Rは低級アルキル基を表わす) で表わされる4−クロロ−3−ヒドロキシ酪酸エステル
と反応させ、オキシラセタム含有液を得るオキシラセタ
ム化工程 (3)前記液を不溶物の濾過後濃縮し、析出するオキシ
ラセタムを得る単離工程
[Scope of Claims] A method for producing oxiracetam comprising the following steps (1), (2) and (3). (1) Glycinamide manufacturing process in which a halogenoacetic acid ester is reacted with ammonia in the presence of a solvent and the reaction solution is concentrated to obtain glycinamide, its salt, or a mixture thereof. (2) The glycinamide, its salt, or a mixture thereof. The mixture is reacted with 4-chloro-3-hydroxybutyric acid ester represented by the general formula ▲Mathematical formula, chemical formula, table, etc.▼ (R represents a lower alkyl group) in the presence of a solvent to obtain an oxiracetam-containing liquid. Racetamization step (3) Isolation step of obtaining precipitated oxiracetam by concentrating the liquid after filtering the insoluble matter
JP16776986A 1986-07-18 1986-07-18 Production of oxiracetam Pending JPS6327477A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16776986A JPS6327477A (en) 1986-07-18 1986-07-18 Production of oxiracetam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16776986A JPS6327477A (en) 1986-07-18 1986-07-18 Production of oxiracetam

Publications (1)

Publication Number Publication Date
JPS6327477A true JPS6327477A (en) 1988-02-05

Family

ID=15855758

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16776986A Pending JPS6327477A (en) 1986-07-18 1986-07-18 Production of oxiracetam

Country Status (1)

Country Link
JP (1) JPS6327477A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100440494B1 (en) * 1998-07-24 2005-03-08 삼성정밀화학 주식회사 Method for preparing (S) -oxyracetam having optical activity
CN105820062A (en) * 2015-01-04 2016-08-03 哈尔滨三联药业股份有限公司 N-(1-oxo-4-hydroxy-2-butenyl)aminoacetamide compound and preparation method and application thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100440494B1 (en) * 1998-07-24 2005-03-08 삼성정밀화학 주식회사 Method for preparing (S) -oxyracetam having optical activity
CN105820062A (en) * 2015-01-04 2016-08-03 哈尔滨三联药业股份有限公司 N-(1-oxo-4-hydroxy-2-butenyl)aminoacetamide compound and preparation method and application thereof

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