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International Journal of Chemical Engineering
Volume 2011 (2011), Article ID 231828, 16 pages
Research Article

Feasibility of Batch Reactive Distillation with Equilibrium-Limited Consecutive Reactions in Rectifier, Stripper, or Middle-Vessel Column

1Department of Chemical and Environmental Process Engineering, Budapest Univesity of Technology and Economics, Muegyetem rkp. 3, 1521 Budapest, Hungary
2Laboratoire de Génie Chimique, Ecole Nationale Supérieure d'Ingénieurs en Arts Chimiques et Technologiques, UMR CNRS 5503, ENSIACET-UPS-CNRS, BP 1301, 5 rue Paulin Talabot, 31106 Toulouse, France

Received 7 March 2011; Accepted 1 August 2011

Academic Editor: Raghunath V. Chaudhari

Copyright © 2011 T. Lukács et al. This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.


A general overall feasibility methodology of batch reactive distillation of multireaction systems is developed to study all the possible configurations of batch reactive distillation. The general model equations are derived for multireaction system with any number of chemical equilibrium-limited reactions and for any number of components. The present methodology is demonstrated with the detailed study of the transesterification of dimethyl carbonate in two reversible cascade reactions in batch reactive distillation process. Pure methanol is produced as distillate, and pure diethyl carbonate is produced at the bottom simultaneously in middle-vessel column; in each section, continuous feeding of ethanol is necessary. The results of feasibility study are successfully validated by rigorous simulations.