Chemical Industry and Engineering Progress ›› 2019, Vol. 38 ›› Issue (07): 3349-3354.DOI: 10.16085/j.issn.1000-6613.2018-2109

• Biochemical and pharmaceutical engineering • Previous Articles     Next Articles

Study and application of the continuous crystallization process of cefalexin

Junli ZHANG1,3(),Junbo GONG1(),Hua SUN2(),Zhigang DUAN3,Weiguo HU3   

  1. 1. College of Chemical Engineering, Tianjin University, Tianjin 307002, China
    2. College of Chemistry and Pharmaceutical Engineering, Hebei University of Science and Technology, Shijiazhuang 050018, Hebei, China
    3. North China Pharmaceutical Co. , Ltd. , Shijiazhuang 052165, Hebei, China
  • Received:2018-10-26 Online:2019-07-05 Published:2019-07-05
  • Contact: Junbo GONG,Hua SUN

头孢氨苄连续结晶研究及应用

张军立1,3(),龚俊波1(),孙华2(),段志钢3,胡卫国3   

  1. 1. 天津大学化工学院,天津 307002
    2. 河北科技大学化学与制药工程学院,河北 石家庄 050018
    3. 华北制药股份有限公司,河北 石家庄 052165
  • 通讯作者: 龚俊波,孙华
  • 作者简介:张军立(1967—),男,博士研究生,教授级高级工程师,研究方向为能源与环保。E-mail:<email>ncpcbeta2004@126.com</email>。
  • 基金资助:
    国家科技部基金(2017ZX07402003)

Abstract:

The traditional production method of cefalexin is mostly intermittent crystallization, which has the disadvantages of low efficiency and high energy consumption. In order to save energy consumption, improve production efficiency, shorten working hours and reduce cost, a two-stage continuous crystallization process was designed according to the characteristics of electrical point crystallization such as cephalexin. The effects of initial concentration, residence time, stirring rate, pH of crystallization end point and seed strategy of cefalexin aqueous solution on the yield, crystal habit and particle size distribution of cefalexin continuous crystallization products were systematically studied by single factor method.The results of single factor experiment showed that the product yield and particle size distribution reached the ideal results when the concentration of cefalexin aqueous solution was 14%, the optimal residence time was 12min, the pH of the end point of crystallization was controlled around 4.8, and the amount of seed addition was 5%.The process can effectively control the supersaturation of the crystallization process in the metastable region and avoid nucleation. Compared with intermittent crystallization, the working time of two-stage continuous crystallization is reduced by 30%. Product crystal integrity, particle size distribution uniformity, yield can reach 96%. At present, this technology has successfully realized the industrialization application of a single production line with a scale of 500 tons/year.

Key words: cefalexin, continuous crystallization, yield, crystal habits, crystal size distribution

摘要:

头孢氨苄的传统生产方法多为间歇结晶,存在效率低、能耗高等弊端。为节约能耗、提高生产效率、缩短工时、降低成本,针对头孢氨苄等电点结晶的特点,本文设计了两级连续结晶工艺。采用单因素法系统研究了头孢氨苄水溶液初始浓度、停留时间、搅拌速率、结晶终点pH、晶种策略等因素对头孢氨苄连续结晶过程产品的收率、晶习及粒度分布的影响。单因素实验结果显示头孢氨苄水溶液质量分数为14%、最佳停留时间为12min、结晶终点pH控制在4.8附近、晶种添加量为5%时其产品收率、粒度分布均达到了理想的效果。该工艺能将结晶过程的过饱和度有效地控制在介稳区内,避免了爆发成核。与间歇结晶相比,两级连续结晶工艺的工时缩短30%。产品晶习完整,粒度分布均匀,收率可以达到96%。目前该工艺已成功实现单条生产线规模为500t/a的产业化应用。

关键词: 头孢氨苄, 连续结晶, 收率, 晶习, 粒度分布

CLC Number: 

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