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Sensitivity Analysis of Steady-State Methyl Acetate Synthesis
Reactive Distillation Column Using Aspen Plus
Sensitivity Analysis of Steady-State Methyl
Acetate Synthesis Reactive Distillation
Column Using Aspen Plus
In chemical processing, simultaneous reaction and separation of the product help to
increase conversion rate and productivity, and saves material handling and processing
costs. In this study, a sensitivity analysis of heterogeneous Reactive Distillation (RD)
using Aspen Plus was carried out to understand the complex behavior of a reactive
distillation column. The esterification reaction of methanol by acetic acid to form
methyl acetate was considered for the sensitivity analysis. The steady state results
were validated with the experimental results reported by Popken et al. (2001).
Considering these steady state results as reference, sensitivity analysis was done.
In the simulation, RADFRAC model was chosen to take care of the complexities
arising due to simultaneous reaction and separation in a single unit. UNIQUAC
property method was selected in the simulator for equilibrium calculations.
Dipaloy Datta* and Dipesh S Patle**
Introduction
Reactive Distillation (RD) is a combination of reaction and distillation in a single unit having
a number of specific advantages over conventional sequential approach of reaction followed by
distillation or any other separation techniques. The combined effect of reaction and separation
increases the selectivity of the product and enhances the conversion of the reactant. The RD
unit provides better control and proper utilization of reaction heat. Moreover, easier separation
of the components can be achieved and formation of azeotropes can be avoided in the RD
column. The complex behavior of the RD column arises because of the complicated vapor-
liquid interactions, mass transfer between solid, liquid and vapor phases, intra-particle (catalyst)
diffusion in the case of catalyzed reactions, and reaction kinetics involved with separation.
Therefore, such kinds of multi directional interactions in the RD system lead to multiple
steady-states and complex dynamics (Taylor and Krishna, 2000).
Therefore, to understand the complete behavior of the simultaneous reaction and
separation process, research on various fields, like modeling and simulation, process synthesis,
© 2010 IUP. All Rights Reserved.
* Lecturer, Chemical Engineering Group, Birla Institute of Technology and Science (BITS) Pilani, Pilani 333031,
Rajasthan, India; and is the corresponding author. E-mail: dipaloy@bits-pilani.ac.in
** Lecturer, Chemical Engineering Group, Birla Institute of Technology and Science (BITS) Pilani, Pilani 333031,
Rajasthan, India. E-mail: dipeshp@bits-pilani.ac.in
Keywords: Reactive distillation (RD), RADFRAC, UNIQUAC, Sensitivity analysis, Aspen Plus