Reactive Distillation for Producing <i>n</i>-Butyl Acetate:Experiment and Simulation

田晖; 黄智贤; 邱挺; 王晓达; 吴燕翔

doi:10.1016/S1004-9541(12)60426-1

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

Updated：2026-01-06

- Reactive Distillation for Producing n-Butyl Acetate:Experiment and Simulation
- Chinese Journal of Chemical Engineering Vol. 20, Issue 5, Pages: 980-987(2012)
- Affiliations：
  
  1. College of Chemistry and Chemical Engineering, Yantai University,Yantai,China,264005
  2. College of Chemistry and Chemical Engineering, Fuzhou University,Fuzhou,China,350002
- Author bio：
- Funds：
- DOI：10.1016/S1004-9541(12)60426-1
  CLC：
- Published：2012
- Accepted：
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-Butyl Acetate:Experiment and Simulation[J]. Chinese Journal of Chemical Engineering, 2012, 20(5): 980-987.
DOI：

-Butyl Acetate:Experiment and Simulation[J]. Chinese Journal of Chemical Engineering, 2012, 20(5): 980-987. DOI： 10.1016/S1004-9541(12)60426-1.

摘要

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

-butyl acetate purity were further investigated. The optimal column configuration for the production of

-butyl acetate was designed with 5 rectifying stages

8 reaction stages and 13 stripping stages by the simulation study. According to the simulation results

-butanol conversion and

-butyl acetate purity all reached greater than 96%.

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

DOI：10.1016/S1004-9541(12)60426-1

摘要

Abstract

关键词

Keywords

references