期刊文献+

环孢菌素A结晶工艺的优化

Optimization of crystal process of cyclosrporine A
在线阅读 下载PDF
导出
摘要 为了确定环孢菌素A结晶工艺,对溶剂种类、反溶剂加入量、结晶温度和降温方式等因素的影响进行研究。首先通过静态结晶研究,确定了丙酮/水结晶体系和溶剂比例。在此基础上,设计了正交试验L9(34)考察动态结晶中各因素对环孢菌素A结晶收率和纯度的影响,并进一步优化了结晶降温方式。结果表明:确定环孢菌素A结晶的最佳条件为采用梯度程序降温,养晶温度为-5℃,丙酮和水的体积比为2∶1,反溶剂水流加时间为0.5 h,开始流加点为降温至0℃,结晶时间约为3 h。经HPLC分析环孢菌素A的纯度平均值为99.15%,收率平均值为87.7%。 The crystalization technology of cyclosporine A was studied by using single factor test and or- thogonal experiment design. Effects of different solvents, solvent ratio, and temperature on the crystalli- zation were investigated. Results revealed that the water content had important effects on the purity and recovery of cyclosporine A and crystallization temperature was also another important factor. The optimum crystalization conditions of cyclosporine A were determined as follows: the cooling in gradient was applied; crystal temperature was -5 ℃ ; solvent ration was 2:1 (acetone: water), feeding time of water was 30 rain; and crystallization period was 3 h. The average HPLC purity of cyclosporine A reached 99. 15%. The average crystalline recovery was 87.7%.
出处 《生物加工过程》 CAS CSCD 2012年第2期15-18,共4页 Chinese Journal of Bioprocess Engineering
基金 国家科技支撑计划资助项目(2007BAI29B01)
关键词 环孢菌素A 结晶 优化 cyclosporine A crystallization optimization
  • 相关文献

参考文献10

二级参考文献53

  • 1强黎明,周彩荣,王建召,蒋登高,吴彬.反式-1,2-环己二醇和甲酸钠的结晶介稳区研究[J].高校化学工程学报,2004,18(5):653-658. 被引量:8
  • 2李秉琦,周红梅.口腔扁平苔藓的治疗方法及方案[J].临床口腔医学杂志,1994,10(3):186-188. 被引量:15
  • 3谭龙泉,张所明,欧庆瑜.薄层色谱在高速逆流色谱溶剂系统选择过程中的应用[J].分析化学,1996,24(12):1448-1451. 被引量:19
  • 4张举之 易新铨.口泰Ⅱ期临床试验研究报告[J].华西口腔医学杂志,1992,10(3):234-234.
  • 5张天佑.逆流色谱技术[M].北京:北京科学技术出版社,1993.290.
  • 6Garside J,Jancie S J. Growth and dissolution of potash alum crystals in the subsieve size range[ J ]. AIChE Journal, 1976,22 (5) : 887 - 894.
  • 7Jones A G, Budz J, Mulin J W. Crystallization kinetics of potassium sulfate in an MSMPR agitated vessel[ J]. AIChE Journal, 1986,32 (12) :2002 -2009.
  • 8Mydlarz J, Jones A G. On modelling the size - dependent growth rate of potassium sulphate in an MSMPR crystallizer [ J ]. Chem. Eng. Commun. ,1989,90:47.
  • 9Garside J ,Jancic S J. Measurement and scale - up of secondary nucleation kinetics for the potash alum - water system [ J ]. AIChE Journal, 1979,25 (6) :948 - 958.
  • 10Randolph A D,Larson M A. Theory of Particulate Processes[ M]. New York : Academic Press, 1971.

共引文献49

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部