A Comparison of Steady-State Equilibrium and Rate-Based Models for Packed Reactive Distillation Columns
Author:
Affiliation:
1. Department of Chemical Engineering, The Separations Research Program, The University of Texas at Austin, Austin, TX 78712-1062
Publisher
American Chemical Society (ACS)
Subject
Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/ie010969b
Reference21 articles.
1. Dynamic simulation of the multicomponent reactive distillation
2. Development of a new catalytic distillation process for fuel ethers via a detailed nonequilibrium model
3. Modeling of homogeneous reactive separation processes in packed columns
4. Nonequilibrium modelling of reactive distillation: Multiple steady states in MTBE synthesis
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