CN102603607B - Preparation method of (R)-oxiracetam - Google Patents
Preparation method of (R)-oxiracetam Download PDFInfo
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Abstract
一种(R)-奥拉西坦的制备方法,采用甘氨酸乙酯盐酸盐与(R)-4-卤-3-羟基-丁酸乙酯为原料在醇溶剂和碱性条件下反应,用无机醇洗涤、浓缩再经萃取、分离通入氨水制得(R)-奥拉西坦粗品和粗品的纯化处理;所述甘氨酸乙酯盐酸盐先要采用乙醚和氨气游离成甘氨酸乙酯。本发明的主要原料为(R)-4-卤-3-羟基丁酸乙酯和甘氨酸乙酯盐酸盐,原料价廉易得且环保、无污染;本发明首先将甘氨酸乙酯盐酸盐进行所述的游离处理,有效减少了反应中物料的用量、降低了成本,同时对反应的收率也起到积极的作用。本发明制备(R)-奥拉西坦的成本低、收率高可高达33%,反应条件温和利于工业化规模生产,制得的(R)-奥拉西坦产品HPLC纯度达98.5%以上。A preparation method of (R)-oxiracetam, adopting glycine ethyl ester hydrochloride and (R)-4-halo-3-hydroxyl-butyric acid ethyl ester as raw materials to react under alcohol solvent and alkaline conditions, Washing with inorganic alcohol, concentration, extraction, separation and introduction of ammonia water to obtain (R)-oxiracetam crude product and purification treatment of the crude product; the glycine ethyl ester hydrochloride must first be dissociated into glycine ethyl ester hydrochloride with ether and ammonia gas ester. The main raw materials of the present invention are (R)-4-halo-3-hydroxybutyric acid ethyl ester and glycine ethyl ester hydrochloride, the raw materials are cheap and easy to get and are environmentally friendly and pollution-free; The above free treatment effectively reduces the amount of materials used in the reaction, lowers the cost, and also plays a positive role in the yield of the reaction. The preparation of (R)-oxiracetam in the present invention has low cost and high yield up to 33%, mild reaction conditions are favorable for industrial scale production, and the HPLC purity of the prepared (R)-oxiracetam product reaches over 98.5%.
Description
技术领域 technical field
本发明涉及奥拉西坦的制备,具体涉及一种(R)-奥拉西坦的制备方法。 The invention relates to the preparation of oxiracetam, in particular to a preparation method of (R)-oxiracetam. the
背景技术 Background technique
奥拉西坦(oxiracetam),是由意大利史克比切姆公司于1974年首次合成的促智药,该药于1987年在意大利上市,奥拉西坦是由两种异构体(S)-奥拉西坦((S)-oxiracetam)和(R)-奥拉西坦((R)-oxiracetam)组成的消旋体。(R)-奥拉西坦是奥拉西坦的一个单一对映体,化学名为:(R)-4-羟基-2-氧代-1-吡咯烷乙酰胺。益智药奥拉西坦是一种合成的羟基氨基丁酸(GABOB)衍生物,它是一种能促进学习,增强记忆力,保护受损神经细胞的中枢神经系统药物。 Oxiracetam is a nootropic drug synthesized for the first time in 1974 by the Italian Skelebechem Company. The drug was launched in Italy in 1987. Oxiracetam is composed of two isomers (S) - A racemate of oxiracetam ((S)-oxiracetam) and (R)-oxiracetam ((R)-oxiracetam). (R)-Oxiracetam is a single enantiomer of oxiracetam with the chemical name: (R)-4-hydroxy-2-oxo-1-pyrrolidineacetamide. The nootropic drug oxiracetam is a synthetic hydroxyaminobutyric acid (GABOB) derivative, which is a central nervous system drug that can promote learning, enhance memory, and protect damaged nerve cells. the
授予I.S.F.Spa的美国专利4,124,594、4,173,569和4,629,797公开了一种制备旋光纯oxyracetam的方法。这些专利中公开的方法包括使旋光纯(s)-γ氨基-β-羟基丁酸与硅烷化试剂反应以保护羟基,使所得产物在酸受体存在下与其中Hal代表卤素原子的式Hal(CH2C00R)的脂族酸卤素化合物反应,然后经环化和水解得到旋光纯oxyracetam。虽然该方法提供了旋光纯oxyracetam,但是它的缺点是:原料昂贵,步骤多、收率低,以及高成本。授予Lonza Ltd的美国专利4,824,966、4,843,166和5,276,164公开了oxyracetam及其中间体的制备方法。这些专利中公开的方法包括使4-(C1-C2)-烷氧基-3-吡咯啉-2-酮-1-基-乙酸(C1-C4)-烷基酯与三氯甲基硅烷反应以保护羟基,然后对所得产物进行氢化和酰胺化。根据该方法,经氢化双键还原得到外消旋oxyracetam。因此,该方法具有不适用于制备旋光纯oxyracetam的缺点。此外,4-(C1-C2)-烷氧基-3-吡咯啉-2-酮-1-基-乙酸(C1-C4)-烷基酯的制备收率低。但到目前还没有见有关文献报道过(R)-奥拉西坦的制备方法。 US Patents 4,124,594, 4,173,569 and 4,629,797 to ISFSpa disclose a process for preparing optically pure oxyracetam. The methods disclosed in these patents include reacting optically pure (s)-gamma amino-beta-hydroxybutyric acid with a silylating agent to protect the hydroxyl group, allowing the resulting product to react with the formula Hal( CH 2 COOR) aliphatic acid halogen compound reaction, followed by cyclization and hydrolysis to obtain optically pure oxyracetam. Although this method provides optically pure oxyracetam, its disadvantages are: expensive raw materials, many steps, low yield, and high cost. US Patents 4,824,966, 4,843,166 and 5,276,164 to Lonza Ltd disclose the preparation of oxyracetam and its intermediates. The process disclosed in these patents involves reacting 4-(C 1 -C 2 )-alkoxy-3-pyrrolin-2-one-1-yl-acetic acid (C 1 -C 4 )-alkyl ester with trichloro Methylsilane is reacted to protect the hydroxyl group, and the resulting product is then subjected to hydrogenation and amidation. According to this method, racemic oxyracetam is obtained by hydrogenation double bond reduction. Therefore, this method has the disadvantage that it is not suitable for the preparation of optically pure oxyracetam. In addition, 4-(C1-C2)-alkoxy-3-pyrrolin-2-on-1-yl-acetic acid (C1-C4)-alkyl esters were prepared in low yields. But up to now, no related literature has reported the preparation method of (R)-oxiracetam.
发明内容 Contents of the invention
本发明的目的在于提供一种成本低、收率高的(R)-奥拉西坦的制备方法。 The purpose of the present invention is to provide a preparation method of (R)-oxiracetam with low cost and high yield. the
本发明目的是通过以下技术方案实现的: The object of the invention is achieved through the following technical solutions:
(R)-奥拉西坦的制备方法,其特征在于:采用甘氨酸乙酯盐酸盐与(R)-4-卤-3-羟基-丁酸乙酯为原料在醇溶剂和碱性条件下反应,经过滤,用无机醇洗涤、浓缩,再经萃取、水相浓缩,通入氨水制得(R)-奥拉西坦粗品和粗品的纯化处理;所述甘氨酸乙酯盐酸盐先要采用乙醚和氨气游离成甘氨酸乙酯。 The preparation method of (R)-oxiracetam is characterized in that: using glycine ethyl ester hydrochloride and (R)-4-halo-3-hydroxyl-butyric acid ethyl ester as raw materials under alcohol solvent and alkaline conditions The reaction is filtered, washed with inorganic alcohol, concentrated, then extracted, concentrated in the water phase, and passed through ammonia water to obtain the crude product of (R)-oxiracetam and the purification treatment of the crude product; the glycine ethyl ester hydrochloride is first Ethyl ether and ammonia are used to dissociate into ethyl glycine. the
为了进一步提高本发明(R)-奥拉西坦的收率,在上述经萃取、水相浓缩之后还进行柱层析分离,再通入氨水制备(R)-奥拉西坦粗品。 In order to further increase the yield of (R)-oxiracetam in the present invention, column chromatography separation is carried out after the above-mentioned extraction and concentration of the aqueous phase, and then ammonia water is introduced to prepare the crude product of (R)-oxiracetam. the
为了减少本发明反应过程中反应原料的用量、降低成本,同时将甘氨酸乙酯盐酸盐更充分地游离以提高收率以及利于纯化处理,本发明对甘氨酸乙酯盐酸盐的游离优选将甘氨酸乙酯盐酸盐加入乙醚中,再在低温下通入氨气。 In order to reduce the consumption of reaction raw materials in the reaction process of the present invention, reduce cost, simultaneously with glycine ethyl ester hydrochloride free more fully to improve yield and be beneficial to purifying treatment, the present invention preferably glycine ethyl ester hydrochloride free Ethyl ester hydrochloride was added to ether, and ammonia gas was introduced at low temperature. the
本发明对甘氨酸乙酯盐酸盐的游离处理过程中,为了更进一步充分地游离得到甘氨酸乙酯,其通入氨气的温度为2℃~-5℃,进一步优选为-3℃~-5℃,其中甘氨酸乙酯盐酸盐、乙醚与氨气的用量比例关系为1mol∶1100~1300ml∶1.2~1.7mol。 In the process of dissociating ethyl glycine hydrochloride in the present invention, in order to further fully dissociate and obtain ethyl glycine, the temperature for feeding ammonia gas is 2°C to -5°C, more preferably -3°C to -5°C. ℃, wherein the proportion of glycine ethyl ester hydrochloride, ether and ammonia is 1mol: 1100~1300ml: 1.2~1.7mol. the
具体地说,本发明对甘氨酸乙酯盐酸盐的游离处理是将甘氨酸乙酯盐酸盐加入无水乙醚中,冰冷至-3℃~-5℃,通入氨气,过滤、将滤液浓缩得甘氨酸乙酯,其中甘氨酸乙酯盐酸盐、乙醚与氨气的用量比例关系为1mol∶1250ml∶1.5mol。 Specifically, the free treatment of glycine ethyl ester hydrochloride in the present invention is to add glycine ethyl ester hydrochloride into anhydrous ether, ice-cool to -3°C ~ -5°C, feed ammonia gas, filter, and concentrate the filtrate Obtain glycine ethyl ester, wherein the consumption ratio relation of glycine ethyl ester hydrochloride, ether and ammonia gas is 1mol: 1250ml: 1.5mol. the
为了使得反应物和产物易于溶解以及反应完成后的处理方便,本发明醇溶剂优选为无水甲醇或无水乙醇。 In order to make the reactants and products easy to dissolve and the treatment after the reaction is completed, the alcohol solvent of the present invention is preferably absolute methanol or absolute ethanol. the
本发明(R)-4-卤-3-羟基-丁酸乙酯优选采用(R)-4-氯-3-羟基-丁酸乙酯;本发明加入的碱优选采用碳酸钠或碳酸氢钠。 (R)-4-halo-3-hydroxyl-butyric acid ethyl ester of the present invention preferably adopts (R)-4-chloro-3-hydroxyl-butyric acid ethyl ester; the alkali that the present invention adds preferably adopts sodium carbonate or sodium bicarbonate . the
为了进一步提高收率以及更利于纯化处理,本发明各物料的用量比例以摩尔比计优选为甘氨酸乙酯∶碳酸氢钠∶(R)-4-氯-3-羟基-丁酸乙酯=1∶1~1.5∶1.2~1.8,所述无水乙醇的用量为碳酸氢钠的3~7倍,以重量份计;进一步优选为,甘氨酸乙酯∶碳酸氢钠∶(R)-4-氯-3-羟基-丁酸乙酯=1∶1.4∶1.6,无水乙醇的用量为碳酸氢钠的4倍。 In order to further improve the yield and be more beneficial to purification treatment, the consumption ratio of each material of the present invention is preferably glycine ethyl ester in terms of molar ratio: sodium bicarbonate: (R)-4-chloro-3-hydroxyl-butyric acid ethyl ester=1 : 1~1.5: 1.2~1.8, the consumption of described dehydrated alcohol is 3~7 times of sodium bicarbonate, in parts by weight; More preferably, ethyl glycine: sodium bicarbonate: (R)-4-chloro -3-hydroxyl-butyric acid ethyl ester=1:1.4:1.6, the consumption of dehydrated alcohol is 4 times of sodium bicarbonate. the
更具体地说,本发明(R)-奥拉西坦粗品的制备是先将甘氨酸乙酯盐酸盐加入无水乙醚中,冰冷至-4℃~-5℃,通入氨气,过滤、将滤液浓缩得甘氨酸乙酯;然后加入无水乙醇,碳酸氢钠和滴加入(R)-4-氯-3-羟基-丁酸乙酯,所述滴加(R)-4-氯-3-羟基-丁酸乙酯的时间为3~3.5小时,控制pH为8~9,反应温度为65~75℃,反应20~30小时;过滤、将滤液用甲醇或乙醇充分洗涤、浓缩,浓缩物溶于水中,再加入4倍滤液重量的氯仿进行萃取,水相浓缩;最后再加入浓氨水,在25~32℃下反应4~7小时;所述甘氨酸乙酯∶碳酸氢钠∶(R)-4-氯-3-羟基-丁酸乙酯=1∶1~1.5∶1.2~1.8,所述无水乙醇的用量为碳酸氢钠重量的3~7倍。 More specifically, the preparation of the crude product of (R)-oxiracetam in the present invention is to first add glycine ethyl ester hydrochloride into anhydrous ether, ice-cool to -4°C ~ -5°C, pass through ammonia gas, filter, Concentrate the filtrate to obtain glycine ethyl ester; then add absolute ethanol, sodium bicarbonate and dropwise add (R)-4-chloro-3-hydroxy-butyric acid ethyl ester, the dropwise addition of (R)-4-chloro-3 -Hydroxy-butyric acid ethyl ester time is 3 to 3.5 hours, the pH is controlled to 8 to 9, the reaction temperature is 65 to 75 ° C, and the reaction is 20 to 30 hours; filter, fully wash the filtrate with methanol or ethanol, concentrate, concentrate The product was dissolved in water, then added 4 times the weight of the filtrate in chloroform for extraction, and the aqueous phase was concentrated; finally, concentrated ammonia was added, and reacted for 4 to 7 hours at 25~32°C; the glycine ethyl ester: sodium bicarbonate: (R )-4-chloro-3-hydroxyl-butyric acid ethyl ester=1: 1~1.5: 1.2~1.8, the consumption of described dehydrated alcohol is 3~7 times of sodium bicarbonate weight. the
为了更进一步提高本发明制备(R)-奥拉西坦的收率,本发明(R)-奥拉西 坦粗品的制备是先将甘氨酸乙酯盐酸盐加入无水乙醚中,冰冷至-4℃~-5℃,通入氨气,过滤、将滤液浓缩得甘氨酸乙酯,其中甘氨酸乙酯盐酸盐、乙醚与氨气的用量比例关系为1mol∶1250ml∶1.5mol;然后加入无水乙醇,碳酸氢钠和滴加所述的(R)-4-氯-3-羟基-丁酸乙酯,滴加3小时,控制pH为8.5,反应温度为75℃,反应28小时;过滤、用乙醇充分洗涤滤液、浓缩,再加入4倍滤液重量的氯仿进行萃取、水相浓缩,柱层析分离;最后加入质量百分浓度为28%的浓氨水,在30℃下反应5小时;所述甘氨酸乙酯∶碳酸氢钠∶(R)-4-氯-3-羟基-丁酸乙酯=1∶1.4∶1.6,以摩尔比计,无水乙醇的用量为碳酸氢钠重量的4倍;所述28%浓氨水的加入量为上述柱分离产物重量的4-8倍。 In order to further improve the yield of (R)-oxiracetam prepared by the present invention, the preparation of (R)-oxiracetam crude product of the present invention is to add glycine ethyl ester hydrochloride in anhydrous ether earlier, ice-cooled to- 4°C~-5°C, feed ammonia gas, filter, and concentrate the filtrate to obtain glycine ethyl ester, wherein the ratio of glycine ethyl ester hydrochloride, ether and ammonia gas is 1mol: 1250ml: 1.5mol; then add anhydrous Ethanol, sodium bicarbonate and the (R)-4-chloro-3-hydroxy-butyric acid ethyl ester were added dropwise for 3 hours, the pH was controlled to be 8.5, the reaction temperature was 75°C, and the reaction was carried out for 28 hours; filtration, Fully wash the filtrate with ethanol, concentrate, then add 4 times the weight of the filtrate in chloroform for extraction, concentrate the water phase, and separate by column chromatography; finally add concentrated ammonia water with a mass percentage concentration of 28%, and react at 30°C for 5 hours; Described glycine ethyl ester: sodium bicarbonate: (R)-4-chloro-3-hydroxyl-butyric acid ethyl ester=1: 1.4: 1.6, in mol ratio, the consumption of dehydrated alcohol is 4 times of sodium bicarbonate weight ; The addition of the 28% concentrated ammonia water is 4-8 times the weight of the column separation product. the
本发明粗产品的纯化处理是将粗产品用水溶解后通过强酸性阳离子交换树脂并收集,再通过强碱性阴离子交换树脂中和收集的溶液,使所述收集的溶液的pH值为中性时完成;然后将中和收集的溶液浓缩后的粗产品进行重结晶处理。 The purification process of the crude product of the present invention is to dissolve the crude product in water and collect it through a strong acidic cation exchange resin, and then neutralize the collected solution through a strong basic anion exchange resin, so that the pH value of the collected solution is neutral. Complete; Then the crude product after neutralizing the collected solution and concentrating it is subjected to recrystallization treatment. the
为了提高交换容量、交换速度,本发明强酸性阳离子交换树脂优选为732#强酸性阳离子交换树脂;本发明强碱性阴离子交换树脂优选为711#强碱性阴离子交换树脂。 In order to improve exchange capacity and exchange speed, the strongly acidic cation exchange resin of the present invention is preferably 732# strongly acidic cation exchange resin; the strongly basic anion exchange resin of the present invention is preferably 711# strongly basic anion exchange resin. the
本发明重结晶处理是采用乙醇进行第一次重结晶处理,采用甲醇/丙酮的混合溶剂进行第二次重结晶处理。 The recrystallization treatment of the present invention uses ethanol for the first recrystallization treatment, and uses a mixed solvent of methanol/acetone for the second recrystallization treatment. the
为了进一步提高本发明(R)-奥拉西坦产品的纯度,本发明纯化处理过程中,所述粗产品的水溶液按粗产品∶水=1克∶1.2毫升,所述强酸性阳离子交换树脂的用量为:所述粗产品∶所述强酸性阳离子交换树脂=1克∶13毫升;所述用乙醇进行第一次重结晶处理的用量为:所述浓缩后的粗产品∶乙醇=1克∶1.5毫升;所述第二次重结晶处理中的用量为:第一次重结晶后的粗产品∶甲醇=1克∶2毫升,其中甲醇/丙酮的混合溶剂中甲醇与丙酮的体积比为1∶2。 In order to further improve the purity of the (R)-oxiracetam product of the present invention, in the purification treatment process of the present invention, the aqueous solution of described crude product presses crude product: water=1 gram: 1.2 milliliters, the strong acidic cation exchange resin Consumption is: described crude product: described strongly acidic cation exchange resin=1 gram: 13 milliliters; Described the consumption that carries out recrystallization treatment for the first time with ethanol is: described concentrated crude product: ethanol=1 gram: 1.5 milliliters; The consumption in the described second recrystallization process is: crude product after the first recrystallization: methyl alcohol=1 gram: 2 milliliters, wherein the volume ratio of methanol and acetone in the mixed solvent of methanol/acetone is 1 : 2. the
本发明有如下的有益效果: The present invention has the following beneficial effects:
1、本发明使用的主要原料为(R)-4-卤-3-羟基丁酸乙酯和甘氨酸乙酯盐酸盐,均为市售商品,原料价廉易得且环保、无污染;同时,本发明首先将甘氨酸乙酯盐酸盐进行所述的游离处理,有效减少了反应中物料的用量、降低了成本,同时对反应的收率也起到了积极的作用。本发明制备的(R)-奥拉西坦的成本低、收率可高达33%,反应条件温和、周期短、操作简单,利于工业化规模生产,同时制得的(R)-奥拉西坦产品HPLC纯度达98.5%以上。 1, the main raw material that the present invention uses is (R)-4-halogen-3-hydroxybutyric acid ethyl ester and glycine ethyl ester hydrochloride, all are commercially available commodity, and raw material is cheap and easy to get and environmental protection, pollution-free; Simultaneously , the present invention first carries out the described free treatment of glycine ethyl ester hydrochloride, which effectively reduces the consumption of materials in the reaction, reduces the cost, and also plays a positive role in the yield of the reaction. The (R)-oxiracetam prepared by the present invention has low cost, the yield can be as high as 33%, the reaction conditions are mild, the cycle is short, and the operation is simple, which is beneficial to industrial scale production, and the (R)-oxiracetam prepared at the same time The HPLC purity of the product is above 98.5%. the
2、本发明在纯化最终产品(R)-奥拉西坦中采用了离子交换树脂处理,与现 有技术中采用硅胶柱层析方法相比,虽然处理效果相当,但是,一方面离子交换树脂可以多次再生重复使用,降低了成本,另一方面离子交换树脂是使用纯水来洗脱,避免了使用有机溶剂,无污染,同时更适宜用于规模化工业大生产。本发明中使用的大部分有机溶剂毒性小、污染低,后处理过程中使用的水更是无污染无毒性的,所以本发明不仅宜于工业化生产,也符合国家环保要求。 2. The present invention adopts ion exchange resin treatment in purifying the final product (R)-oxiracetam. Compared with the silica gel column chromatography method in the prior art, although the treatment effect is equivalent, on the one hand, the ion exchange resin It can be regenerated and reused many times, which reduces the cost. On the other hand, the ion exchange resin is eluted with pure water, which avoids the use of organic solvents, has no pollution, and is more suitable for large-scale industrial production. Most of the organic solvents used in the present invention have low toxicity and low pollution, and the water used in the post-treatment process is pollution-free and non-toxic, so the present invention is not only suitable for industrial production, but also meets the national environmental protection requirements. the
具体实施方式 Detailed ways
下面通过实施例对本发明进行具体的描述,有必要在此指出的是以下实施例只用于对本发明进行进一步说明,不能理解为对本发明保护范围的限制,该领域的技术熟练人员可以根据上述本发明内容对本发明作出一些非本质的改进和调整。 The present invention is specifically described below through the examples, it is necessary to point out that the following examples are only used to further illustrate the present invention, and can not be interpreted as limiting the protection scope of the present invention, those skilled in the art can according to above-mentioned this SUMMARY OF THE INVENTION Some non-essential improvements and adjustments are made to the present invention. the
实施例1 Example 1
(R)-奥拉西坦的制备方法,按如下步骤进行: The preparation method of (R)-oxiracetam, carries out as follows:
1、粗品的制备: 1. Preparation of crude product:
(a)将甘氨酸乙酯盐酸盐139.6g加入到无水乙醚1250ml中,冰冷至-4℃通入氨气25.5g使甘氨酸乙酯盐酸盐游离成甘氨酸乙酯,其中甘氨酸乙酯盐酸盐∶无水乙醚∶氨气为1mol∶1250ml∶1.5mol; (a) Add 139.6 g of ethyl glycine hydrochloride into 1250 ml of anhydrous ether, cool it to -4°C and blow in 25.5 g of ammonia gas to dissociate ethyl glycine hydrochloride into ethyl glycine, wherein ethyl glycine hydrochloride Salt: anhydrous ether: ammonia gas is 1mol: 1250ml: 1.5mol;
(b)向上述产物中加入无水乙醇470ml,碳酸氢钠117.6g、滴加(R)-4-氯-3-羟基-丁酸乙酯266.6g,所述滴加时间为3小时,在pH8.5、温度为75℃下反应28小时; (b) Add absolute ethanol 470ml, sodium bicarbonate 117.6g, dropwise (R)-4-chloro-3-hydroxyl-butyric acid ethyl ester 266.6g in the above-mentioned product, and described dropping time is 3 hours, in React for 28 hours at pH 8.5 and temperature 75°C;
(c)过滤、用乙醇充分洗涤滤液、浓缩,浓缩物溶于水,再加入4.5倍滤液重量的氯仿进行萃取、水相浓缩,柱层析分离;最后加入质量百分浓度为28%的氨水,在30℃下反应5小时制得(R)-奥拉西坦粗品,其中28%氨水的用量为柱层析分离产物重量的6倍; (c) filter, fully wash the filtrate with ethanol, concentrate, dissolve the concentrate in water, then add 4.5 times the weight of the filtrate in chloroform for extraction, concentrate the water phase, and separate by column chromatography; finally add ammonia water with a mass percentage concentration of 28% , reacted at 30°C for 5 hours to obtain the crude product of (R)-oxiracetam, wherein the consumption of 28% ammonia water was 6 times of the weight of the product separated by column chromatography;
其中甘氨酸乙酯∶碳酸氢钠∶(R)-4-氯-3-羟基-丁酸乙酯=1∶1.4∶1.6,以摩尔比计,无水乙醇的用量为碳酸氢钠重量的4倍; Wherein ethyl glycine: sodium bicarbonate: (R)-4-chloro-3-hydroxyl-butyric acid ethyl ester=1: 1.4: 1.6, in mol ratio, the consumption of dehydrated alcohol is 4 times of sodium bicarbonate weight ;
2、粗品的纯化: 2. Purification of crude product:
(a)用水溶解上述制得的粗品,通过732#强酸性阳离子交换树脂,然后通过711#强碱性阴离子交换树脂中和并收集溶液、浓缩;所述粗品∶水=1克∶1.2毫升,所述粗产品∶所述强酸性阳离子交换树脂=1克∶13毫升; (a) dissolving the above-mentioned crude product in water, passing through 732# strongly acidic cation exchange resin, and then neutralizing and collecting the solution and concentrating through 711# strongly basic anion exchange resin; described crude product: water=1 gram: 1.2 milliliters, Described crude product: described strongly acidic cation exchange resin=1 gram: 13 milliliters;
(b)然后将上述通过离子交换树脂浓缩后的粗品采用乙醇进行第一次重结晶处理,采用甲醇/丙酮的混合溶剂进行第二次重结晶处理制得(R)-奥拉西坦 产品;所述通过离子交换树脂后浓缩的粗产品∶乙醇=1克∶1.5毫升;所述第一次重结晶后的粗产品∶甲醇=1克∶2毫升,其中甲醇/丙酮的混合溶剂中甲醇与丙酮的体积比为1∶2。 (b) then carry out the first recrystallization treatment with ethanol to the above-mentioned crude product after ion exchange resin concentration, and use the mixed solvent of methanol/acetone to carry out the second recrystallization treatment to obtain (R)-oxiracetam product; The crude product concentrated after passing through the ion exchange resin: ethanol=1 gram: 1.5 milliliters; The crude product after the described first recrystallization: methanol=1 gram: 2 milliliters, wherein in the mixed solvent of methanol/acetone, methanol and The volume ratio of acetone is 1:2. the
最终制得的(R)-奥拉西坦产品的HPLC纯度达99.5%,收率高达33%。 The HPLC purity of the finally prepared (R)-oxiracetam product reaches 99.5%, and the yield is as high as 33%. the
实施例2 Example 2
(R)-奥拉西坦的制备方法,按如下步骤进行: The preparation method of (R)-oxiracetam, carries out as follows:
1、粗品的制备: 1. Preparation of crude product:
(a)将甘氨酸乙酯盐酸盐加入到无水乙醚中,冰冷至-4℃通入氨气使甘氨酸乙酯盐酸盐游离成甘氨酸乙酯,其中甘氨酸乙酯盐酸盐∶无水乙醚∶氨气为1mol∶1300ml∶1.2mol; (a) Add glycine ethyl ester hydrochloride to anhydrous ether, cool to -4°C and pass through ammonia gas to dissociate glycine ethyl ester hydrochloride into glycine ethyl ester, wherein glycine ethyl ester hydrochloride: anhydrous ether : Ammonia is 1mol: 1300ml: 1.2mol;
(b)向上述产物中加入无水甲醇,碳酸钠、(R)-4-碘-3-羟基-丁酸乙酯,在pH8、温度为65℃下反应20小时; (b) Add anhydrous methanol, sodium carbonate, (R)-4-iodo-3-hydroxy-butyric acid ethyl ester to the above product, and react at pH 8 and temperature at 65°C for 20 hours;
(c)过滤、用乙醇充分洗涤滤液、浓缩,浓缩物溶于水,再加入5倍滤液重量的乙酸乙酯进行萃取、水相浓缩,柱层析分离;最后加入质量百分浓度为27%的氨水,在25℃下反应7小时制得(R)-4-羟基-2-氧代-1-吡咯烷乙酰胺粗品,其中27%氨水的用量为柱层析分离产物重量的8倍;其中甘氨酸乙酯∶碳酸钠∶(R)-4-碘-3-羟基-丁酸乙酯=1∶1.5∶1.8,以摩尔比计,无水甲醇的用量为碳酸钠重量的7倍; (c) Filtrate, fully wash the filtrate with ethanol, concentrate, dissolve the concentrate in water, then add ethyl acetate 5 times the weight of the filtrate for extraction, concentrate the water phase, and separate by column chromatography; finally add a mass percent concentration of 27% Aqueous ammonia was reacted at 25°C for 7 hours to obtain the crude product of (R)-4-hydroxyl-2-oxo-1-pyrrolidineacetamide, wherein the amount of 27% ammonia was 8 times the weight of the product separated by column chromatography; Wherein ethyl glycine: sodium carbonate: (R)-4-iodo-3-hydroxyl-butyric acid ethyl ester=1: 1.5: 1.8, in mol ratio, the consumption of anhydrous methanol is 7 times of sodium carbonate weight;
2、粗品的纯化: 2. Purification of crude product:
(a)用水溶解上述制得的粗品,通过001×7强酸性苯乙烯系阳离子交换树脂,然后通过201×7碱性苯乙烯系阴离子交换树脂中和并收集溶液、浓缩;所述粗品∶水=1克∶0.6毫升,所述粗产品∶所述强酸性阳离子交换树脂=1克∶10毫升; (a) dissolve the above-mentioned crude product in water, pass through 001×7 strong acidic styrene-based cation exchange resin, and then pass through 201×7 basic styrene-based anion-exchange resin to neutralize and collect the solution and concentrate; the crude product: water =1 gram: 0.6 milliliters, described crude product: described strongly acidic cation exchange resin=1 gram: 10 milliliters;
(b)然后将上述通过离子交换树脂浓缩后的粗品采用乙醇进行第一次重结晶处理,采用甲醇/丙酮的混合溶剂进行第二次重结晶处理制得(R)-奥拉西坦产品;所述通过离子交换树脂后浓缩的粗产品∶乙醇=1克∶1.5毫升;所述第一次重结晶后的粗产品∶甲醇=1克∶1毫升,其中甲醇/丙酮的混合溶剂中甲醇与丙酮的体积比为1∶2。 (b) then carry out the first recrystallization treatment with ethanol to the crude product concentrated by the ion exchange resin, and use the mixed solvent of methanol/acetone to carry out the second recrystallization treatment to obtain the (R)-oxiracetam product; The crude product concentrated after passing through the ion exchange resin: ethanol=1 gram: 1.5 milliliters; The crude product after the described first recrystallization: methanol=1 gram: 1 milliliter, wherein in the mixed solvent of methanol/acetone, methanol and The volume ratio of acetone is 1:2. the
最终制得的(R)-奥拉西坦产品的HPLC纯度达99.2%,收率达28%。 The HPLC purity of the finally obtained (R)-oxiracetam product reaches 99.2%, and the yield reaches 28%. the
实施例3 Example 3
(R)-奥拉西坦的制备方法,按如下步骤进行: The preparation method of (R)-oxiracetam, carries out as follows:
1、粗品的制备: 1. Preparation of crude product:
(a)将甘氨酸乙酯盐酸盐悬浮于化学纯乙醚中,然后通入氨气使甘氨酸乙酯盐酸盐游离成甘氨酸乙酯; (a) Glycine ethyl ester hydrochloride is suspended in chemically pure ether, feeds ammonia gas then and glycine ethyl ester hydrochloride is freed into glycine ethyl ester;
(b)向上述产物中加入无水乙醇,碳酸氢钠、滴加(R)-4-溴-3-羟基-丁酸乙酯,所述滴加时间为3.5小时,在pH9、温度为70℃下反应20~26小时; (b) Add absolute ethanol, sodium bicarbonate, dropwise (R)-4-bromo-3-hydroxyl-butyric acid ethyl ester to the above product, the time for the addition is 3.5 hours, at a pH of 9 and a temperature of 70 Reaction at ℃ for 20-26 hours;
(c)然后过滤,用乙醇充分洗涤滤液、浓缩,浓缩物溶于水,再加入4倍滤液重量的氯仿进行萃取、水相浓缩;最后加入质量百分浓度为26%的氨水,在28℃下反应6小时制得(R)-奥拉西坦粗品; (c) then filter, fully wash the filtrate with ethanol, concentrate, and the concentrate is dissolved in water, then add 4 times the weight of the filtrate in chloroform for extraction, and concentrate the water phase; finally add the ammonia water with a mass percentage concentration of 26%, at 28 ° C Down reaction made (R)-oxiracetam crude product in 6 hours;
其中甘氨酸乙酯∶碳酸氢钠∶(R)-4-溴--3-羟基-丁酸乙酯=1∶1∶1.2,以摩尔比计,无水乙醇的用量为碳酸氢钠重量的3倍; Wherein ethyl glycine: sodium bicarbonate: (R)-4-bromo--3-hydroxyl-butyric acid ethyl ester=1: 1: 1.2, in terms of molar ratio, the consumption of dehydrated alcohol is 3% of the weight of sodium bicarbonate times;
2、粗品的纯化: 2. Purification of crude product:
(a)用水溶解上述制得的粗品,通过732#强酸性阳离子交换树脂,然后通过711#强碱性阴离子交换树脂中和并收集溶液、浓缩;所述粗品∶水=1克∶0.6毫升,所述粗产品∶所述强酸性阳离子交换树脂=1克∶10毫升; (a) dissolving the above-mentioned crude product in water, passing through 732# strongly acidic cation exchange resin, and then neutralizing and collecting the solution and concentrating through 711# strongly basic anion exchange resin; described crude product: water=1 gram: 0.6 milliliters, Described crude product: described strongly acidic cation exchange resin=1 gram: 10 milliliters;
(b)然后将上述通过离子交换树脂浓缩后的粗品采用乙醇进行第一次重结晶处理,采用甲醇/丙酮的混合溶剂进行第二次重结晶处理制得(R)-奥拉西坦产品;所述通过离子交换树脂后浓缩的粗产品∶乙醇=1克∶1.5毫升;所述第一次重结晶后的粗产品∶甲醇=1克∶2毫升,其中甲醇/丙酮的混合溶剂中甲醇与丙酮的体积比为1∶3。 (b) then carry out the first recrystallization treatment with ethanol to the crude product concentrated by the ion exchange resin, and use the mixed solvent of methanol/acetone to carry out the second recrystallization treatment to obtain the (R)-oxiracetam product; The crude product concentrated after passing through the ion exchange resin: ethanol=1 gram: 1.5 milliliters; The crude product after the described first recrystallization: methanol=1 gram: 2 milliliters, wherein in the mixed solvent of methanol/acetone, methanol and The volume ratio of acetone is 1:3. the
最终制得的(R)-奥拉西坦产品的HPLC纯度达99.3%,收率高达26%。 The HPLC purity of the finally prepared (R)-oxiracetam product reaches 99.3%, and the yield is as high as 26%. the
实施例4~8: Embodiment 4~8:
一种(R)-奥拉西坦的制备方法,按以下物料及工艺参数进行,其余同实施例1。 A preparation method of (R)-oxiracetam is carried out according to the following materials and process parameters, and the rest are the same as in Example 1. the
以上实施例最终制得的(R)-奥拉西坦产品的HPLC纯度达98.5%~99.26%以上,收率达28%~33%。 The HPLC purity of the (R)-oxiracetam product finally obtained in the above examples reaches above 98.5%-99.26%, and the yield reaches 28%-33%. the
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Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1956953A (en) * | 2004-05-25 | 2007-05-02 | 安国药品株式会社 | Process for the preparation of optically pure 4-hydroxy-2-oxo-1-pyrrolidine acetamide |
| CN101367757A (en) * | 2008-10-13 | 2009-02-18 | 重庆润泽医疗器械有限公司 | Preparation method of (S) -4-hydroxy-2-oxo-1-pyrrolidine acetamide |
-
2011
- 2011-01-21 CN CN201110024526.XA patent/CN102603607B/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1956953A (en) * | 2004-05-25 | 2007-05-02 | 安国药品株式会社 | Process for the preparation of optically pure 4-hydroxy-2-oxo-1-pyrrolidine acetamide |
| CN101367757A (en) * | 2008-10-13 | 2009-02-18 | 重庆润泽医疗器械有限公司 | Preparation method of (S) -4-hydroxy-2-oxo-1-pyrrolidine acetamide |
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