化工进展 ›› 2019, Vol. 38 ›› Issue (06): 2905-2914.DOI: 10.16085/j.issn.1000-6613.2018-2126

• 生物与医药化工 • 上一篇    下一篇

舒巴坦钠溶析结晶工艺优化

李丽(),刘宝树,郑学明,孙华()   

  1. 河北科技大学化学与制药工程学院,河北 石家庄 050018
  • 收稿日期:2018-10-30 出版日期:2019-06-05 发布日期:2019-06-05
  • 通讯作者: 孙华
  • 作者简介:李丽(1992—),女,硕士研究生,研究方向为工业结晶、药物分离与纯化。E-mail:<email>lili_L0815@163.com</email>。

Optimization of anti-solvent crystallization process of sulbactam sodium

Li LI(),Baoshu LIU,Xueming ZHENG,Hua SUN()   

  1. College of Chemical and Pharmaceutical Engineering, Hebei University of Science and Technology, Shijiazhuang 050018, Hebei, China
  • Received:2018-10-30 Online:2019-06-05 Published:2019-06-05
  • Contact: Hua SUN

摘要:

目前舒巴坦钠粗品的提纯采用还原成舒巴坦酸后再经反应结晶合成舒巴坦钠的方式,耗时耗力且所需药品、试剂种类较多,不节能环保。针对该问题,采用正交实验 L 27 3 13 对舒巴坦钠的溶析结晶工艺进行优化,探明了6个因素6个交互作用对粒度、纯度以及两者的综合评分的影响,包括养晶时间(A)、溶析剂用量(B)、溶析剂中乙醇的体积分数(C)、溶析剂的滴加速率(D)、搅拌速率(E)、温度(F)以及养晶时间分别与溶析剂用量(A×B)、与溶析剂中乙醇的体积分数(A×C)的交互作用、溶析剂用量与溶析剂中乙醇的体积分数的交互作用(B×C),并得到了一组最优方案A 2 B 2 C 1 D 3 E 3 F 2。通过该方案可获得纯度x>97%,体积平均粒度D[4,3]≈290μm,质量收率约为84%的舒巴坦钠产品,并发现杂质舒巴坦青霉胺对舒巴坦钠的粒度分布有一定的影响。在解决原有问题的基础上,合适粒度分布的舒巴坦钠产品也可为后续制剂工艺提供方便。

关键词: 舒巴坦钠, 溶析结晶, 正交实验, 纯度, 晶体粒度分布

Abstract:

At present, the way of purifying sulbactam sodium is to synthesize sulbactam sodium by sulbactam acid, which is obtained by reduction reaction. The method is time-consuming, labor-intensive and requires a large variety of drugs and reagents, and is not energy-saving and environmentally friendly. For this problem, the orthogonal experiment L 27 3 13 was used to optimize the anti-solvent crystallization of sulbactam sodium. The effects of six factors and three interactions on crystal size distribution, purity and comprehensive scores of the two were considered, included aging time (A), volume of anti-solvent used(B), volume fraction of ethanol in the anti-solvent(C), rate of addition of the anti-solvent (D), stirring rate (E), crystallization temperature(F), and the interaction between the aging time and the volume of the anti-solvent (A×B), the interaction between the aging time and the volume fraction of ethanol in the decanting agent (A×C), the interaction between the volume of the anti-solvent used and the volume fraction of ethanol in the anti-solvent(B×C) . The results of variance analysis showed: the used volume of anti-solvent (B) has the most significant effect on crystal size distribution(CSD), but other factors and interactions are not significant; the volume fraction of ethanol in the anti-solvent(C), the dropping rate of the anti-solvent(D), the stirring rate (E) and the interaction between the aging time and the volume fraction of ethanol in the anti-solvent(A×C) have a highly significant impact on the purity, and both of interaction between the crystallization time and the volume of the anti-solvent(A×B), and the interaction between the volume of anti-solvent used and the volume fraction of ethanol in the anti-solvent(B×C) have a significant effect, but the others are not significant; when the significant level α is between 0.10 and 0.025, considering the purity-CSD at a ratio of 70% and 30% respectively, volume of the anti-solvent used(B) and the volume fraction of ethanol in the anti-solvent(C) are highly significant, and others are not significant. The optimal operating level combination is A 2 B 2 C 1 D 3 E 3 F 2. Repeated validation tests yielded: the purity of sulbactam sodium raw material can be increased from 79.58% to over 97% by only once anti-solvent crystallization, and the crystal size distribution D[4,3] can be increased from 41.1μm to above 290μm. The mass fraction yield of sulbactam sodium obtained by multiple confirmatory experiments is about 84%. It is found that the impurity sulbactam penicillamine has a certain influence on the particle size distribution of sulbactam sodium. On the basis of solving the original problems, the sulbactam sodium product with suitable particle size distribution can also provide convenience for the subsequent preparation process.

Key words: sulbactam sodium, anti-solvent crystallization, orthogonal test, purity, crystal size distribution

中图分类号: 

京ICP备12046843号-2;京公网安备 11010102001994号
版权所有 © 《化工进展》编辑部
地址:北京市东城区青年湖南街13号 邮编:100011
电子信箱:hgjz@cip.com.cn
本系统由北京玛格泰克科技发展有限公司设计开发 技术支持:support@magtech.com.cn