化工进展

• 工业催化 • 上一篇    下一篇

活性炭固载三氯化铁催化蔗糖产乙酰丙酸

王 攀,于宏兵,王 璐,庄源益   

  1. 南开大学环境科学与工程学院
  • 出版日期:2009-05-05 发布日期:2009-05-05

Production of levulinic acid from sucrose catalyzed by ferric chloride supported on activated carbon

WANG Pan,YU Hongbing,WANG Lu,ZHUANG Yuanyi   

  1. College of Environmental Science and Engineering,Nankai University
  • Online:2009-05-05 Published:2009-05-05

摘要: 采用活性炭固载氯化铁为催化剂,催化蔗糖转化为乙酰丙酸。利用响应面这一多因素过程优化的有效工具,通过Box—Beknhen实验,对反应温度、反应时间、催化剂投加量和蔗糖浓度4个因素进行了优化。优化后的实验条件为:反应温度218 ℃,反应时间28 min,催化剂投加量0.05 mol/L,蔗糖浓度0.3 mol/L,该条件下乙酰丙酸产率为47.33%。

Abstract: Production of levulinic acid catalyzed by ferric chloride supported on activated carbon was studied. The response surface method, a useful tool for multi-factor process optimization, was used through Box-Beknhen experiment design. The selected four factors were reaction temperature, reaction time, dose of catalyst and concentration of sucrose. The optimized experiment conditions were: reaction temperature 218℃, reaction time 28min, dose of catalyst 0.05 mol/L, concentration of sucrose 0.3 mol/L. The maximum levulinic acid production reached 47.33% under the optimized experiment conditions.

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