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Dynamic Simulation of Reactive Batch Distillation Column for Ethyl Acetate Synthesis
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Rahul Patel
, Kailash Singh , Vishnu Pareek and Moses O. Tadé
Published/Copyright:
May 8, 2007
A detailed mathematical dynamic model of reactive batch distillation column is formulated for ethyl acetate synthesis and presented in terms of differential and algebraic equations (DAEs). These DAEs are solved using fourth order Runge-Kutta method in MATLAB® to obtain the detailed column dynamics. The simulation results provide the dynamics of reboiler and distillate compositions, reboiler temperature, ethyl acetate purity in the accumulated distillate and conversion of the reactants. These results are analyzed to derive the optimum operating policy, i.e., reflux ratio and batch time.
Published Online: 2007-5-8
©2011 Walter de Gruyter GmbH & Co. KG, Berlin/Boston
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Keywords for this article
reactive batch distillation column;
modelling;
simulation;
ethyl acetate synthesis
Articles in the same Issue
- Article
- Editorial: Special Issue Contributed from CHEMECA 2006-Australasian Process Modelling and Control Selected Papers
- Modelling of the Development of the Vertical Density Profile of MDF during Hot Pressing
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