The influence of different models in obtaining multiple solutions in distillation columns
Author:
Publisher
Wiley
Subject
General Chemical Engineering
Link
http://onlinelibrary.wiley.com/wol1/doi/10.1002/cjce.5450750619/fullpdf
Reference33 articles.
1. The Influence of Equilibrium Chemical Reactions on Vapor-Liquid Phase Diagrams;Barbosa;Chem. Eng. Sci.,1988
2. The Simple Distillation of Homogeneous Reactive Mixtures;Barbosa;Chem. Eng. Sci.,1988
3. Design and Minimum-Reflux Calculations for Single-Feed Multicomponent Reactive Distillation Columns;Barbosa;Chem. Eng. Sci.,1988
4. Multiple Steady States in Homogeneous Azeotropic Distillation;Bekiaris;Ind. Eng. Chem. Res.,1993
5. Bekiaris, N., G. A. Meski and M. Morari, “Multiple Steady States in Azeotropic Distillation and their Effect on Column Operation and Design”, presented at the 4th IFAC Symposium on Dynamics and Control of Chemical Reactors, Distillation Columns and Batch Processes, Copenhagen, Denmark, June 7-9, 1995.
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2. An Extensive Analysis on the Start-up of a Simple Distillation Column with Multiple Steady States;The Canadian Journal of Chemical Engineering;2008-05-19
3. Strategies for Starting Up Azeotropic Distillation Columns with Multiple Steady States;The Canadian Journal of Chemical Engineering;2008-05-19
4. Analysis and Multiple Steady States of an Industrial Heterogeneous Azeotropic Distillation;Industrial & Engineering Chemistry Research;2001-06-01
5. Equilibrium-Staged Separations: A Bibliography Update (1997);Separation Science and Technology;1999-11
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