[an error occurred while processing this directive]
化学工业与工程
 首页 |  在线投稿 |  期刊介绍 |  编 委 会 |  投稿指南 |  期刊订阅 |  下载中心 |  出版伦理 |  联系我们 |  English
化学工业与工程 2015, Vol. 32 Issue (1) :37-40    DOI: 10.13353/j.issn.1004.9533.2015.01.008
化学反应与工艺 最新目录 | 下期目录 | 过刊浏览 | 高级检索 << | >>
阿奇霉素二水合物溶析结晶工艺优化
马博爱1, 龚俊波1,2
1. 天津大学化工学院国家工业结晶工程技术研究中心, 天津 300072;
2. 天津大学现代药物传递及功能高效化天津市重点实验室, 天津 300072
Optimization of Crystallization Process of Azithromycin Dihydrate
Ma Boai1, Gong Junbo1,2
1. The State Research Center of Industrialization for Crystallization Technology, School of Chemical Engineering and Technology, Tianjin University, Tianjin 300072, China;
2. Key Laboratory Modern Drug Delivery and High Efficiency, Tianjin University, Tianjin 300072, China

摘要
参考文献
相关文章
Download: PDF (1585KB)   HTML ()   Export: BibTeX or EndNote (RIS)      Supporting Info
摘要 针对阿奇霉素二水合物的溶析结晶工艺,考察了结晶的初始浓度、溶析剂流加速率以及搅拌强度对结晶产品的粒度分布的影响规律,确定了优化的工艺参数为结晶温度40 ℃,初始浓度0.32 g/g,搅拌速率为200 r/min,溶析剂滴加速率为200 μL/min。在此条件下可获得粒度分布约为300 μm到800 μm且主粒度约为580 μm的产品,克服目前结晶产品存在的聚结、粒度分布不均一等问题。
Service
把本文推荐给朋友
加入我的书架
加入引用管理器
Email Alert
RSS
作者相关文章
关键词阿奇霉素;   溶析结晶;   粒度分布;   聚结     
Abstract: In this paper, the influence of initial concentration, pumping rate of anti-solvent and agitation intensity on the crystal size distribution (CSD) of products was considered and then an optimized crystallization technology was proposed. The optimized products were obtained at 40 ℃ with 0.32 g/g initial concentration, 200 r/min agitation rate and 200 μL/min feeding rate. The CSD of products is from 300 μm to 800 μm and the mean crystal size is 580 μm.
KeywordsAzithromycin;   dilution crystallization;   crystal size distribution   agg;lomeration     
Received 2013-04-11;
Corresponding Authors: 龚俊波,E-mail:junbo_gong@tju.edu.cn。     Email: junbo_gong@tju.edu.cn
About author: 马博爱(1987-),男,硕士研究生,现从事药物结晶方面的研究。
引用本文:   
马博爱, 龚俊波.阿奇霉素二水合物溶析结晶工艺优化[J].  化学工业与工程, 2015,32(1): 37-40
Ma Boai, Gong Junbo.Optimization of Crystallization Process of Azithromycin Dihydrate[J].  Chemcial Industry and Engineering, 2015,32(1): 37-40
Copyright 2010 by 化学工业与工程