Feasibility of Batch Reactive Distillation with Equilibrium-Limited Consecutive Reactions in Rectifier, Stripper, or Middle-Vessel Column
Joint Authors
Stéger, C.
Lukács, T.
Meyer, M.
Rév, E.
Lelkes, Z.
Source
International Journal of Chemical Engineering
Issue
Vol. 2011, Issue 2011 (31 Dec. 2011), pp.1-16, 16 p.
Publisher
Hindawi Publishing Corporation
Publication Date
2011-10-26
Country of Publication
Egypt
No. of Pages
16
Main Subjects
Engineering Sciences and Information Technology
Abstract EN
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.
American Psychological Association (APA)
Lukács, T.& Stéger, C.& Rév, E.& Meyer, M.& Lelkes, Z.. 2011. Feasibility of Batch Reactive Distillation with Equilibrium-Limited Consecutive Reactions in Rectifier, Stripper, or Middle-Vessel Column. International Journal of Chemical Engineering،Vol. 2011, no. 2011, pp.1-16.
https://search.emarefa.net/detail/BIM-455834
Modern Language Association (MLA)
Lukács, T.…[et al.]. Feasibility of Batch Reactive Distillation with Equilibrium-Limited Consecutive Reactions in Rectifier, Stripper, or Middle-Vessel Column. International Journal of Chemical Engineering No. 2011 (2011), pp.1-16.
https://search.emarefa.net/detail/BIM-455834
American Medical Association (AMA)
Lukács, T.& Stéger, C.& Rév, E.& Meyer, M.& Lelkes, Z.. Feasibility of Batch Reactive Distillation with Equilibrium-Limited Consecutive Reactions in Rectifier, Stripper, or Middle-Vessel Column. International Journal of Chemical Engineering. 2011. Vol. 2011, no. 2011, pp.1-16.
https://search.emarefa.net/detail/BIM-455834
Data Type
Journal Articles
Language
English
Notes
Includes bibliographical references
Record ID
BIM-455834