Tuning a distillation column simulator

A4 Conference proceedings

Internal Authors/Editors

Publication Details

List of Authors: Kurt E. Häggblom, Ramkrishna K. Ghosh
Editors: E.N. Pistikopoulos, M.C. Georgiadis, A.C. Kokossis
Publication year: 2011
Publisher: Elsevier
Book title: 21st European Symposium on Computer Aided Process Engineering – ESCAPE 21
Title of series: Computer Aided Chemical Engineering
Volume number: 29
Start page: 823
End page: 827
ISBN: 978-0-444-53895-6


A dynamic simulation model for binary distillation is presented. The
model is based on mass, component and energy balances as well as
pertinent expressions for the thermodynamic properties of the binary
mixture. The model includes a total condenser, producing a reflux with a
varying degree of subcooling, and a thermosyphon reboiler, which
introduces several operating parameters. Parameters related to the
operation of the condenser and the reboiler as well as tray efficiencies
and heat losses from the column are determined by fitting to
experimental data.


Data reconciliation, Distillation modelling, Dynamic simulator, Parameter estimation


Last updated on 2020-30-03 at 06:46