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CN114195761B - A kind of preparation method of high-purity sitafloxacin 3/2 hydrate - Google Patents

A kind of preparation method of high-purity sitafloxacin 3/2 hydrate Download PDF

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CN114195761B
CN114195761B CN202111592708.7A CN202111592708A CN114195761B CN 114195761 B CN114195761 B CN 114195761B CN 202111592708 A CN202111592708 A CN 202111592708A CN 114195761 B CN114195761 B CN 114195761B
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sitafloxacin
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hydrate
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CN114195761A (en
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李晓黎
张鑫
唐武期
庄江海
熊小利
李开波
赫亚征
倪建昆
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Zhejiang Apeloa Jiayuan Pharmaceutical Co ltd
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Abstract

本发明公开了一种高纯度西他沙星3/2水合物的制备方法,包括以下步骤:将西他沙星粗品、水、溶剂和氨水混合、溶清、过滤,然后对滤液减压蒸馏或者通入惰性气体进行结晶,当总体积变化超过5~15%时,补加新鲜的溶剂和水的混合溶液;当pH在8.0~9.5,降温通入惰性气体继续结晶;达到结晶终点后,后处理得到所述的高纯度西他沙星3/2水合物。该制备方法得到的西他沙星纯度高,最大杂质≤0.6‰,含量高,外观类白色,长期稳定性好。The invention discloses a preparation method of high-purity sitafloxacin 3/2 hydrate, which comprises the following steps: mixing crude sitafloxacin, water, solvent and ammonia water, dissolving, filtering, and then distilling the filtrate under reduced pressure Or feed inert gas for crystallization, when the total volume change exceeds 5-15%, add a fresh mixed solution of solvent and water; when the pH is 8.0-9.5, cool down and feed inert gas to continue crystallization; after reaching the end point of crystallization, Post-treatment to obtain the high-purity sitafloxacin 3/2 hydrate. The sitafloxacin obtained by the preparation method has high purity, maximum impurity ≤ 0.6‰, high content, off-white appearance and good long-term stability.

Description

一种高纯度西他沙星3/2水合物的制备方法A kind of preparation method of high-purity sitafloxacin 3/2 hydrate

技术领域technical field

本发明属于化学制药领域,具体涉及一种高纯度西他沙星3/2水合物的制备方法。The invention belongs to the field of chemical pharmacy, and in particular relates to a preparation method of high-purity sitafloxacin 3/2 hydrate.

背景技术Background technique

西他沙星(sitafloxacin hydrate)是第一三共株式会社开发的喹诺酮类抗菌药,临床用其3/2水合物。西他沙星是一种新型口服、具有广谱抗菌效果的抗菌药,不仅对革兰阴性菌有抗菌活性,而且对革兰阳性菌、厌氧菌以及支原体、衣原体等具有较强的抗菌活性,对许多临床常见耐氟喹诺酮类菌株也具有良好杀菌作用。Sitafloxacin hydrate is a quinolone antibacterial drug developed by Daiichi Sankyo Co., Ltd., and its 3/2 hydrate is used clinically. Sitafloxacin is a new type of oral antibacterial drug with broad-spectrum antibacterial effect. It not only has antibacterial activity against Gram-negative bacteria, but also has strong antibacterial activity against Gram-positive bacteria, anaerobic bacteria, mycoplasma, chlamydia, etc. , It also has a good bactericidal effect on many common clinical fluoroquinolone-resistant strains.

西他沙星化学名:7-[(7S)-7-氨基-5-氮杂螺[2.4]庚-5-基]-8-氯-6-氟-1-[(1R,2S)-cis-2-氟环丙基]-1,4-二氢-4-氧代-3-喹啉羧酸。结构式如下:Sitafloxacin chemical name: 7-[(7S)-7-amino-5-azaspiro[2.4]hept-5-yl]-8-chloro-6-fluoro-1-[(1R,2S)- cis-2-fluorocyclopropyl]-1,4-dihydro-4-oxo-3-quinolinecarboxylic acid. The structural formula is as follows:

Figure BDA0003430292660000011
Figure BDA0003430292660000011

西他沙星是多晶型化合物,文献[International Journal of Pharmaceutics(2012)422,1–8]中报道了无水的α,β型,含水的1/2水合物,1水合物,3/2水合物,共计五种晶型。其临床药物所用晶型为3/2水合物。该文同时介绍了三种含水化合物晶型通过热处理可以转化为α,β型。Sitafloxacin is a polymorphic compound. It is reported in the literature [International Journal of Pharmaceuticals (2012) 422,1–8] that it is anhydrous α, β, water-containing 1/2 hydrate, 1 hydrate, 3/ 2 hydrates, a total of five crystal forms. The crystal form used in clinical medicine is 3/2 hydrate. This article also introduced that three crystal forms of hydrated compounds can be transformed into α and β forms by heat treatment.

原研专利CN1106006公开了西他沙星的五种晶型的制备方法及参数范围,其中3/2水合物是通过氨水、含水的乙醇溶剂重结晶得到。其中,3/2水合物的制备方法如下:将粗品溶解在乙醇、水和氨水的混合溶剂中,活性炭脱色后,减压蒸去大约一半的溶剂,然后冷却至室温,真空干燥得到3/2水合物。该工艺存在的问题是通过重结晶得到产品的杂质高、纯度差,外观颜色深、发黄,溶剂残留高。The original research patent CN1106006 discloses the preparation methods and parameter ranges of five crystal forms of sitafloxacin, in which the 3/2 hydrate is obtained by recrystallization from ammonia water and aqueous ethanol solvent. Among them, the preparation method of 3/2 hydrate is as follows: the crude product is dissolved in the mixed solvent of ethanol, water and ammonia water, after activated carbon is decolorized, about half of the solvent is evaporated under reduced pressure, then cooled to room temperature, and vacuum-dried to obtain 3/2 hydrate Hydrate. The problem that this technology exists is that the impurity of the product obtained by recrystallization is high, the purity is poor, and appearance color is deep, turns yellow, and solvent residue is high.

专利CN105566287公开了一种在乙酸体系条件下重结晶制备西他沙星3/2水合物的方法,该工艺重结晶的产品收率偏低仅为86%、放大生产时酸性条件下产品稳定性差。Patent CN105566287 discloses a method for preparing sitafloxacin 3/2 hydrate by recrystallization under the condition of acetic acid system. The product yield of recrystallization in this process is only 86%, and the product stability is poor under acidic conditions during scale-up production .

公开号为CN 103524887 A的中国专利申请公开了一种西他沙星的制备方法,并公开了西他沙星的精制方法,该精制方法采用乙醇和氨水将西他沙星溶解,然后加入丙酮析出晶体;然而本发明人重复该工艺时发现在乙醇:氨水=2:1时西他沙星不容易溶解、所用氨水浓度大,导致杂质增大;同时该工艺在结晶时会伴随着油状凝结物固化,导致产品外观不均匀局部偏黄;离心抽滤时氨气味道较浓,影响结晶区工作环境;产品的稳定性差、易变色;此外,本申请的发明人按照其文本记载的精制方法将西他沙星的纯度由99.4%左右提高至99.7%左右,收率只有75%,精制效率不高。The Chinese patent application whose publication number is CN 103524887 A discloses a preparation method of sitafloxacin, and discloses a refining method of sitafloxacin. The refining method uses ethanol and ammonia water to dissolve sitafloxacin, and then adds acetone Crystals are precipitated; however, when the inventor repeats the process, he finds that sitafloxacin is not easy to dissolve when ethanol: ammonia water=2:1, and the concentration of ammonia water used is large, resulting in an increase in impurities; simultaneously, the process will be accompanied by oily condensation during crystallization solidification of the product, resulting in uneven and local yellowish appearance of the product; strong ammonia smell during centrifugal suction filtration, which affects the working environment in the crystallization area; poor stability and easy discoloration of the product; The purity of sitafloxacin is increased from about 99.4% to about 99.7%, the yield is only 75%, and the refining efficiency is not high.

综上所述,现有专利、文献中报道的重结晶方法制备西他沙星3/2水合物,普遍具有得到的产品杂质数量多、单杂大、批次间重复性差异大,外观颜色深的缺点。To sum up, the recrystallization method reported in existing patents and literatures to prepare sitafloxacin 3/2 hydrate generally has the following problems: the obtained product has many impurities, large single impurities, large repeatability differences between batches, and appearance color deep flaws.

发明内容Contents of the invention

本发明提供了一种高纯度西他沙星3/2水合物的制备方法,该制备方法收率高,得到的产品纯度高、杂质少,并且便于重复。The invention provides a preparation method of high-purity sitafloxacin 3/2 hydrate. The preparation method has high yield, and the obtained product has high purity, less impurities and is easy to repeat.

一种高纯度西他沙星3/2水合物的制备方法,包括以下步骤:A preparation method of high-purity sitafloxacin 3/2 hydrate, comprising the following steps:

将西他沙星粗品、水、溶剂和氨水混合、溶清、过滤,然后对滤液减压蒸馏或者通入惰性气体,当釜内体积变化超过5~15%时,补加新鲜的溶剂和水的混合溶剂进行结晶,当pH在8.0~9.5,降温通入惰性气体继续结晶,达到结晶终点后,后处理得到所述的高纯度西他沙星3/2水合物。Mix the crude sitafloxacin, water, solvent and ammonia water, dissolve and filter, then distill the filtrate under reduced pressure or pass inert gas, when the volume change in the kettle exceeds 5-15%, add fresh solvent and water The mixed solvent is used for crystallization. When the pH is 8.0-9.5, the temperature is lowered and inert gas is introduced to continue the crystallization. After reaching the crystallization end point, post-treatment is performed to obtain the high-purity sitafloxacin 3/2 hydrate.

本发明通过大量的实验数据积累,探索出一种西他沙星3/2水合物的新结晶方法,该结晶方法除了加入结晶溶剂和氨水之外,还额外补充一定量的水作为溶剂,然后通过减压蒸馏或者通入惰性气体的方式将体系中的氨气赶出,当达到指定pH值时,继续用通入惰性气体的方式继续进行结晶,可以使西他沙星晶体平稳析出,得到的产品纯度高、杂质少、外观类白色。The present invention explores a new crystallization method of sitafloxacin 3/2 hydrate through the accumulation of a large amount of experimental data. In addition to adding crystallization solvent and ammonia water, the crystallization method also supplements a certain amount of water as a solvent, and then The ammonia gas in the system is driven out by vacuum distillation or the way of feeding inert gas, and when the specified pH value is reached, the method of feeding inert gas is continued to continue crystallization, so that sitafloxacin crystals can be precipitated stably, and the obtained The product has high purity, less impurities and off-white appearance.

本发明的制备方法,所采用的溶剂是通过对大量的实验得到的。实验过程中使用的溶剂有水、氨水、甲醇、乙醇、异丙醇,正丁醇,乙腈、二氯甲烷、乙酸乙酯、丙酮、甲苯、四氢呋喃中的一种或两种混合,所用的溶剂最优选为乙醇。In the preparation method of the present invention, the solvent used is obtained through a large number of experiments. The solvents used in the experiment process are water, ammonia water, methanol, ethanol, isopropanol, n-butanol, acetonitrile, dichloromethane, ethyl acetate, acetone, toluene, tetrahydrofuran or a mixture of two, the solvent used Most preferred is ethanol.

作为优选,起始阶段混合时,西他沙星粗品与溶剂、水、氨水的比例范围为:西他沙星粗品、溶剂、水、氨水的重量比在1:(2~5):(3~8):(1~4)。同不加入水的方法相比,水的加入可以促进西他沙星粗品的溶解,进而保证后续结晶的顺利进行。As preferably, when mixing at the initial stage, the ratio range of sitafloxacin crude product to solvent, water and ammonia water is: the weight ratio of sitafloxacin crude product, solvent, water and ammonia water is 1: (2~5): (3 ~8): (1~4). Compared with the method without adding water, the addition of water can promote the dissolution of crude sitafloxacin, thereby ensuring the smooth progress of subsequent crystallization.

本发明引入的惰性气体为氩气、氮气等,通常采用氮气。流量根据投料量的大小,可控制在1~10升/小时。惰性气体经酸处理吸收后可循环使用,该酸通常为盐酸、硫酸、乙酸、磷酸或硝酸的水溶液等。The inert gas introduced in the present invention is argon, nitrogen, etc., and nitrogen is usually used. The flow rate can be controlled at 1-10 liters/hour according to the size of the feeding amount. The inert gas can be recycled after being treated and absorbed by an acid, which is usually an aqueous solution of hydrochloric acid, sulfuric acid, acetic acid, phosphoric acid or nitric acid, etc.

本发明的制备方法中,所使用的氨水的浓度为10~28%,优选的使用范围为氨水浓度在20~28%之间。氨水的加入温度通常为30~60℃,优选为40~60℃。In the preparation method of the present invention, the concentration of the ammonia water used is 10-28%, and the preferred use range is that the concentration of the ammonia water is between 20-28%. The temperature for adding ammonia water is usually 30-60°C, preferably 40-60°C.

本发明的控制釜内体积连续减压蒸馏或通入惰性气体重结晶时,补充新鲜的溶剂与水的混合溶液,保持结晶釜内体积恒定。补加新鲜的混合溶剂中水和溶剂的重量比在10:1~1:10,进一步优选控制在6:1~1:6。补加的混合溶剂的重量或体积以控制釜内体积恒定±10%为标准。When the volume in the control tank of the present invention is continuously distilled under reduced pressure or passed through inert gas for recrystallization, fresh mixed solution of solvent and water is added to keep the volume in the crystallization tank constant. The weight ratio of water and solvent in the added fresh mixed solvent is 10:1-1:10, more preferably controlled at 6:1-1:6. The weight or volume of the added mixed solvent is based on the constant ±10% of the volume in the control kettle.

本发明的制备方法中,在pH值达到8.0~9.5之前,控制结晶釜内温度为30~50℃条件下、减压蒸馏或通入惰性气体,进一步优选控制在35~45℃。In the preparation method of the present invention, before the pH value reaches 8.0-9.5, the temperature in the crystallization tank is controlled at 30-50°C, vacuum distillation or inert gas is introduced, more preferably controlled at 35-45°C.

本发明的制备方法中,在pH值达到8.0~9.5后,降温通入惰性气体的温度为0~5℃,搅拌时间为1~3小时。In the preparation method of the present invention, after the pH value reaches 8.0-9.5, the temperature for cooling and feeding inert gas is 0-5° C., and the stirring time is 1-3 hours.

同现有技术相比,本发明的有益效果体现在:Compared with the prior art, the beneficial effects of the present invention are reflected in:

(1)采用本发明的制备方法,得到的西他沙星纯度高,最大杂质≤0.6‰,含量高,外观类白色,长期稳定性好,便于长期存放;(1) By adopting the preparation method of the present invention, the obtained sitafloxacin has high purity, maximum impurity≤0.6‰, high content, off-white appearance, good long-term stability, and is convenient for long-term storage;

(2)采用本发明的制备方法,具有产品收率高的优点,便于工业上应用。(2) Adopting the preparation method of the present invention has the advantage of high product yield and is convenient for industrial application.

附图说明Description of drawings

图1为本发明西他沙星3/2水合物的X衍射粉末衍射谱图;Fig. 1 is the X-ray diffraction powder diffraction spectrogram of sitafloxacin 3/2 hydrate of the present invention;

图2为西他沙星3/2水合物的质谱;Fig. 2 is the mass spectrum of sitafloxacin 3/2 hydrate;

图3为西他沙星3/2水合物的氢谱;Fig. 3 is the hydrogen spectrum of sitafloxacin 3/2 hydrate;

图4为西他沙星3/2水合物的碳谱;Fig. 4 is the carbon spectrum of sitafloxacin 3/2 hydrate;

图5为西他沙星3/2水合物的红外谱图。Figure 5 is the infrared spectrum of sitafloxacin 3/2 hydrate.

具体实施方式Detailed ways

本发明的一般操作步骤包括:General operating steps of the present invention include:

在惰性气体保护下,向结晶釜中加入西他沙星粗品、水、乙醇、氨水的比例为1:2~5:3~8:1~4(重量比),升温至30~60℃,搅拌20~60分钟溶清,热过滤。控制釜内温度在30~50℃,将滤液减压蒸馏或持续通入惰性气体;蒸馏或通入气体时保持釜内体积恒定不变,当釜内体积变化超过±10%时补加新鲜的乙醇/水混合溶液,混合溶液中物料配比控制在乙醇:水=10:1~1:10(重量比)范围内;冷却装置要求温度在-20~15℃范围内将蒸馏出的乙醇/水混合溶液泠凝;通入的惰性气体(流量1~10升/小时)带走的氨通入酸性溶液中、回收成铵盐,并将惰性气体通入下一只重结晶反应釜。减压蒸馏或通入惰性气体至结晶釜内以釜内结晶液的pH在5.0~9.5范围为结晶终点。结晶釜降温至0~5℃,保温2小时。离心,用水、乙醇/水、乙醇洗涤。20~25℃、减压烘干得到产品,收率在90~97%。Under the protection of inert gas, add sitafloxacin crude product, water, ethanol, and ammonia water into the crystallization kettle in a ratio of 1:2~5:3~8:1~4 (weight ratio), and heat up to 30~60°C. Stir for 20-60 minutes to dissolve, and filter hot. Control the temperature in the kettle at 30-50°C, distill the filtrate under reduced pressure or continuously feed inert gas; keep the volume in the kettle constant when distilling or feeding gas, and add fresh when the volume change in the kettle exceeds ±10%. Ethanol/water mixed solution, the ratio of materials in the mixed solution is controlled within the range of ethanol:water=10:1~1:10 (weight ratio); The water mixed solution is condensed; the ammonia that is taken away by the inert gas (flow rate 1-10 liters/hour) is passed into the acidic solution, and recovered into ammonium salt, and the inert gas is passed into the next recrystallization reactor. Distill under reduced pressure or pass inert gas into the crystallization tank, and the pH of the crystallization liquid in the tank is in the range of 5.0 to 9.5 as the crystallization end point. The temperature of the crystallization kettle was lowered to 0-5°C, and the temperature was kept for 2 hours. Centrifuge, wash with water, ethanol/water, ethanol. Dry at 20-25°C under reduced pressure to obtain the product with a yield of 90-97%.

所用西他沙星粗品具体制备方法如下:The specific preparation method of the sitafloxacin crude product used is as follows:

在装有机械搅拌装置和温度计的反应瓶里加入三氟乙酸(5.5L),搅拌下冷却至-5℃,加入7-[(7S)-7-叔丁氧羰基氨基-5-氮杂螺[2,4]-庚-5-基]-8-氯-6-氟-1-[(1R,2S)-cis-2-氟-1-环丙基]-1,4-二氢-4-氧代喹啉-3-羧酸(540g,1.06mol)和苯甲醚(110ml),缓慢升温至0~5℃,搅拌反应30min(HPLC显示原料残留小于0.5%)。35℃减压浓缩,剩余物中加入二氯甲烷(4.5L),0~10℃加入0.5mol/L氢氧化钠溶液(约150L)调至pH=10~12,待固体全部溶解后分出水层,有机层用0.1mol/L氢氧化钠(1.5L×2)萃取。合并水层,以二氯甲烷(4L×2)洗涤,过滤,滤液在0~10℃加入15%枸橼酸溶液(约4.8L)调至pH=7,同温搅拌30min,抽滤,滤饼用水洗涤,40℃减压干燥12h,得黄色固体粗品(410g)。Add trifluoroacetic acid (5.5 L) into a reaction flask equipped with a mechanical stirring device and a thermometer, cool to -5°C under stirring, add 7-[(7S)-7-tert-butoxycarbonylamino-5-azaspiro [2,4]-Hept-5-yl]-8-chloro-6-fluoro-1-[(1R,2S)-cis-2-fluoro-1-cyclopropyl]-1,4-dihydro- 4-Oxoquinoline-3-carboxylic acid (540g, 1.06mol) and anisole (110ml) were slowly warmed up to 0-5°C, and stirred for 30min (HPLC showed that the remaining raw material was less than 0.5%). Concentrate under reduced pressure at 35°C, add dichloromethane (4.5L) to the residue, add 0.5mol/L sodium hydroxide solution (about 150L) at 0-10°C to adjust to pH = 10-12, separate the water after all the solids are dissolved layer, and the organic layer was extracted with 0.1mol/L sodium hydroxide (1.5L×2). Combine the aqueous layers, wash with dichloromethane (4L×2), filter, add 15% citric acid solution (about 4.8L) to the filtrate at 0-10°C to adjust to pH = 7, stir at the same temperature for 30min, suction filter, filter The cake was washed with water and dried under reduced pressure at 40° C. for 12 hours to obtain a crude yellow solid (410 g).

下面结合实施例对本发明做进一步的说明,使本领域专业技术人员更好的理解本发明。实施例仅为解释性的,决不意味着它以任何方式限制本发明的范围。The present invention will be further described below in conjunction with the examples, so that those skilled in the art can better understand the present invention. The examples are illustrative only and are in no way meant to limit the scope of the invention in any way.

实施例1Example 1

反应釜中加入西他沙星粗品(HPLC纯度99.4%)10g,乙醇35g、水60g,缓慢升温至50~55℃,加入28%氨水28g溶清后,恒温压滤;滤液通入氮气流量3升/小时,开启冷凝器降温至0~5℃,尾气经50%硫酸水溶液中和转化成硫酸铵;结晶釜降温至35~40℃反应釜中持续通入氮气,并补加20g 15%的水乙醇混合溶剂,当结晶釜pH达到8~9时,降温至0~5℃,继续通入氮气。0~5℃、恒温搅拌2小时,离心,烘干得到9.5g西他沙星成品,收率95%,纯度99.8%,得到的西他沙星成品的X衍射粉末衍射谱图、质谱、氢谱、碳谱和红外谱图见图1~5。Add 10 g of sitafloxacin crude product (HPLC purity 99.4%), 35 g of ethanol, and 60 g of water in the reaction kettle, slowly heat up to 50-55° C., add 28 g of 28% ammonia water to dissolve, and press filter at a constant temperature; liter/hour, open the condenser and cool down to 0-5°C, the tail gas is neutralized by 50% sulfuric acid aqueous solution and converted into ammonium sulfate; Water and ethanol mixed solvent, when the pH of the crystallization tank reaches 8-9, cool down to 0-5°C, and continue to feed nitrogen. Stir at 0-5°C for 2 hours at a constant temperature, centrifuge, and dry to obtain 9.5 g of sitafloxacin finished product, with a yield of 95% and a purity of 99.8%. The X-ray powder diffraction spectrum, mass spectrum, and hydrogen Spectrum, carbon spectrum and infrared spectrum are shown in Figures 1-5.

同时,对西他沙星成品进行稳定性试验,25℃、湿度60±10%、长期稳定性试验结果见下表:At the same time, a stability test was carried out on the finished sitafloxacin product. The results of the long-term stability test at 25°C and a humidity of 60±10% are shown in the table below:

Figure BDA0003430292660000051
Figure BDA0003430292660000051

实施例2Example 2

反应釜中加入西他沙星粗品(HPLC纯度99.4%)10g,乙醇55g、水30g,缓慢升温至50~55℃,加入28%氨水25g溶清后,保温压滤;滤液鼓入氮气流量2升/小时,开启冷凝器降温至0~5℃,尾气经50%硫酸水溶液中和转化成硫酸铵;45~50℃反应釜中持续通入氮气并补加30g 25%的水乙醇混合溶剂;当结晶釜pH达到8~9时,降温至0~5℃,继续通入氮气。0~5℃、恒温搅拌2小时,离心,烘干得到9.6g西他沙星成品,收率96%,纯度99.8%。Add 10 g of sitafloxacin crude product (HPLC purity 99.4%), 55 g of ethanol, and 30 g of water in the reaction kettle, slowly heat up to 50-55° C., add 25 g of 28% ammonia water to dissolve, then heat-preserve and press filter; liter/hour, open the condenser and cool down to 0-5°C, the tail gas is neutralized by 50% sulfuric acid aqueous solution and converted into ammonium sulfate; nitrogen is continuously fed into the reaction kettle at 45-50°C and 30g of 25% water-ethanol mixed solvent is added; When the pH of the crystallization tank reaches 8-9, lower the temperature to 0-5°C, and continue feeding nitrogen. Stir at 0-5°C for 2 hours at a constant temperature, centrifuge, and dry to obtain 9.6 g of finished sitafloxacin, with a yield of 96% and a purity of 99.8%.

实施例3Example 3

反应釜中加入西他沙星粗品(HPLC纯度99.4%)10g,乙醇50g、水25g,缓慢升温至50~55℃,加入28%氨水26g溶清后,保温压滤;控制釜内温度为35~40℃将滤液减压蒸馏,开启冷凝器降温至0~5℃;减压蒸馏过程中通过补加18%的水乙醇溶液、保持釜内体积恒定;当结晶釜内pH达到8~9时,降温至0~5℃,继续通入氮气。0~5℃、恒温搅拌2小时,离心,烘干得到9.4g西他沙星成品,收率94%,纯度99.9%。Add 10 g of sitafloxacin crude product (HPLC purity 99.4%), 50 g of ethanol, and 25 g of water into the reaction kettle, slowly heat up to 50-55° C., add 26 g of 28% ammonia water to dissolve it, and then heat-preserve and press filter; control the temperature in the kettle to 35 Distill the filtrate under reduced pressure at ~40°C, open the condenser and cool down to 0~5°C; during the vacuum distillation process, add 18% water-ethanol solution to keep the volume in the kettle constant; when the pH in the crystallization kettle reaches 8~9 , lower the temperature to 0-5°C, and continue to feed nitrogen. Stir at a constant temperature at 0-5°C for 2 hours, centrifuge, and dry to obtain 9.4 g of finished sitafloxacin, with a yield of 94% and a purity of 99.9%.

实施例4Example 4

反应釜中加入西他沙星粗品(HPLC纯度99.4%)10g,乙醇45g、水25g,缓慢升温至50~55℃,加入28%氨水27g溶清后,保温压滤;控制釜内温度为35~40℃将滤液减压蒸馏,开启冷凝器降温至0~5℃;减压蒸馏过程中通过补加20%的水乙醇溶液、保持釜内体积恒定;当结晶釜内pH达到8~9时,降温至0~5℃,继续通入氮气。0~5℃、恒温搅拌2小时,离心,烘干得到9.7g西他沙星成品,收率97%,纯度99.8%。Add 10 g of sitafloxacin crude product (HPLC purity 99.4%), 45 g of ethanol, and 25 g of water into the reaction kettle, slowly heat up to 50-55° C., add 27 g of 28% ammonia water to dissolve, then heat-preserve and press filter; control the temperature in the kettle to 35 Distill the filtrate under reduced pressure at ~40°C, open the condenser and cool down to 0~5°C; during the vacuum distillation process, add 20% water-ethanol solution to keep the volume in the kettle constant; when the pH in the crystallization kettle reaches 8~9 , lower the temperature to 0-5°C, and continue to feed nitrogen. Stir at a constant temperature at 0-5°C for 2 hours, centrifuge, and dry to obtain 9.7 g of finished sitafloxacin, with a yield of 97% and a purity of 99.8%.

对比例1Comparative example 1

将7-[(7-(S)-氨基-5-氮杂螺[2,4]庚-5-基]-8-氯-6-氟-1-[(1R,2S)-2-氟环丙基]-4-氧代-1,4-二氢喹啉-3-羧酸的结晶粗品7.7g加入至45ml乙醇、37ml水、25ml的28%氨水中,加热升温至45℃,搅拌溶清,减压浓缩(真空度约0.09MPa~0.095Mpa),蒸馏至37ml左右,停止浓缩,降温至室温,搅拌30分钟,过滤,滤饼洗涤烘干得到产品。外观浅黄色粉末,最大单杂>0.05%,收率85%,HPLC纯度为99.7%。7-[(7-(S)-amino-5-azaspiro[2,4]hept-5-yl]-8-chloro-6-fluoro-1-[(1R,2S)-2-fluoro Cyclopropyl]-4-oxo-1,4-dihydroquinoline-3-carboxylic acid crystalline crude 7.7g was added to 45ml of ethanol, 37ml of water, 25ml of 28% ammonia water, heated to 45°C, stirred Dissolve, concentrate under reduced pressure (vacuum degree is about 0.09MPa~0.095Mpa), distill to about 37ml, stop concentrating, cool down to room temperature, stir for 30 minutes, filter, wash and dry the filter cake to obtain the product. The appearance is light yellow powder, the largest single Impurities > 0.05%, yield 85%, HPLC purity 99.7%.

对比例2Comparative example 2

向西他沙星粗品210g中加入无水乙醇/28%氨水(2:1,V/V)1680ml,加热升温至35~40℃,搅拌1小时无法溶清,继续升温至50℃溶清,加入活性炭脱色,过滤。35~40℃,滤液加入840ml丙酮,加毕,降温至0~5℃冷却1小时(丙酮加入过程中,局部过饱和度大,观察到产品发生出油现象,油滴固化形成黄色凝结的产品,影响产品的外观和纯度),过滤,滤饼40~45℃烘干,得到西他沙星,最大单杂>0.05%,收率75%,HPLC纯度为99.8%,产品外观不均匀局部偏黄。Add 1680ml of absolute ethanol/28% ammonia water (2:1, V/V) to 210g of sitafloxacin crude product, heat up to 35-40°C, stir for 1 hour to dissolve, continue to heat up to 50°C to dissolve, Add activated carbon for decolorization and filter. 35~40℃, add 840ml acetone to the filtrate, after the addition, cool down to 0~5℃ and cool for 1 hour (during the process of adding acetone, the local supersaturation degree is high, it is observed that the product produces oil, and the oil droplets solidify to form a yellow condensed product , affect the appearance and purity of the product), filter, and dry the filter cake at 40-45° C. to obtain sitafloxacin, the maximum single impurity > 0.05%, the yield is 75%, the HPLC purity is 99.8%, and the product appearance is uneven and partially partial yellow.

对比例2的结果表明,直接采用无水乙醇和氨水的混合溶剂进行溶解时,西他沙星粗品溶解困难,并且采用该种方法结晶过程不易控制,得到的产品收率较低,并且产品外观不好。The results of comparative example 2 show that when the mixed solvent of absolute ethanol and ammonia water is directly used for dissolving, the sitafloxacin crude product is difficult to dissolve, and the crystallization process is not easy to control by this method, and the product yield obtained is low, and the product appearance not good.

Claims (6)

1. A preparation method of high-purity sitafloxacin hydrate 3/2 is characterized by comprising the following steps:
mixing a sitafloxacin crude product, water, a solvent and ammonia water, dissolving, filtering, then carrying out reduced pressure distillation on the filtrate or introducing inert gas for crystallization, and supplementing a fresh mixed solvent of the solvent and the water when the total volume change exceeds 5-15%; when the pH value is 8.0-9.5, cooling and introducing inert gas for continuous crystallization; after the crystallization end point is reached, post-treating to obtain the high-purity sitafloxacin hydrate 3/2;
the solvent is ethanol;
the supplemented solvent is ethanol;
in the mixed solvent, the weight ratio of water to ethanol is 10;
the crude product of sitafloxacin: solvent: water: the weight ratio of ammonia water is 1: (2-5): (3-8): (1-4);
the temperature of mixing, dissolving and filtering is 30-60 ℃.
2. The method for preparing high-purity sitafloxacin 3/2 hydrate as claimed in claim 1, wherein the concentration of the ammonia water is 10-28%.
3. The method for preparing high-purity sitafloxacin 3/2 hydrate according to claim 1, wherein the inert gas is nitrogen or argon, and the feeding speed is 1-10 liters/hour.
4. The method for preparing high purity sitafloxacin 3/2 hydrate as claimed in claim 1 or 2, wherein the temperature of the reduced pressure distillation or the inert gas introduction is 30-50 ℃.
5. The method for preparing high-purity sitafloxacin 3/2 hydrate according to claim 1, wherein the weight ratio of the added mixed solvent to the water to the ethanol is 6.
6. The method for preparing high-purity sitafloxacin 3/2 hydrate as claimed in claim 1, wherein the temperature of the inert gas is lowered to 0-5 ℃, and the stirring time is 1-3 hours.
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