SCI和EI收录∣中国化工学会会刊

Chin.J.Chem.Eng. ›› 2012, Vol. 20 ›› Issue (5): 980-987.

• PROCESS SYSTEMS ENGINEERING • Previous Articles     Next Articles

Reactive Distillation for Producing n-Butyl Acetate:Experiment and Simulation

TIAN Hui1, HUANG Zhixian2, QIU Ting2, WANG Xiaoda2, WU Yanxiang2   

  1. 1. College of Chemistry and Chemical Engineering, Yantai University, Yantai 264005, China;
    2. College of Chemistry and Chemical Engineering, Fuzhou University, Fuzhou 350002, China
  • Received:2011-06-07 Revised:2012-03-14 Online:2012-11-06 Published:2012-10-28

Reactive Distillation for Producing n-Butyl Acetate:Experiment and Simulation

田晖1, 黄智贤2, 邱挺2, 王晓达2, 吴燕翔2   

  1. 1. College of Chemistry and Chemical Engineering, Yantai University, Yantai 264005, China;
    2. College of Chemistry and Chemical Engineering, Fuzhou University, Fuzhou 350002, China
  • 通讯作者: WU Yanxiang,E-mail:wuyx@fzu.edu.cn

Abstract: In this paper, a reactive distillation (RD) column was applied for synthesis n-butyl acetate from n-butanol and acetic acid. The Langmuir-Hinshelwood-Hougen-Watson (LHHW) kinetic model and an equilibrium stage model for separation were employed to study the RD process. The results obtained from the equilibrium stage model agreed well with the experiments. The effects of operating variables on the n-butanol conversion and n-butyl acetate purity were further investigated. The optimal column configuration for the production of n-butyl acetate was designed with 5 rectifying stages, 8 reaction stages and 13 stripping stages by the simulation study. According to the simulation results, n-butanol conversion and n-butyl acetate purity all reached greater than 96%.

Key words: reactive distillation, esterification, n-butyl acetate, simulation

摘要: In this paper, a reactive distillation (RD) column was applied for synthesis n-butyl acetate from n-butanol and acetic acid. The Langmuir-Hinshelwood-Hougen-Watson (LHHW) kinetic model and an equilibrium stage model for separation were employed to study the RD process. The results obtained from the equilibrium stage model agreed well with the experiments. The effects of operating variables on the n-butanol conversion and n-butyl acetate purity were further investigated. The optimal column configuration for the production of n-butyl acetate was designed with 5 rectifying stages, 8 reaction stages and 13 stripping stages by the simulation study. According to the simulation results, n-butanol conversion and n-butyl acetate purity all reached greater than 96%.

关键词: reactive distillation, esterification, n-butyl acetate, simulation