Tuning a Distillation Column Simulator

Kurt Erik Häggblom; Ramkrishna Ghosh

doi:10.1016/B978-0-444-53711-9.50165-6

Tuning a Distillation Column Simulator

Research output: Chapter in Book/Conference proceeding › Conference contribution › Scientific › peer-review

Abstract

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.

Original language	Undefined/Unknown
Title of host publication	21st European Symposium on Computer Aided Process Engineering – ESCAPE 21
Editors	EN Pistikopoulos, MC Georgiadis, AC Kokossis
Publisher	Elsevier
Pages	823–827
ISBN (Print)	978-0-444-53895-6
DOIs	https://doi.org/10.1016/B978-0-444-53711-9.50165-6
Publication status	Published - 2011
MoE publication type	A4 Article in a conference publication
Event	ESCAPE - 21st European Symposium on Computer Aided Process Engineering – ESCAPE 21 Duration: 29 May 2011 → 1 Jun 2011

Conference

Conference	ESCAPE
Period	29/05/11 → 01/06/11

Keywords

Data reconciliation
Distillation modelling
Dynamic simulator
Parameter estimation

Access to Document

10.1016/B978-0-444-53711-9.50165-6

https://www.sciencedirect.com/science/article/pii/B9780444537119501656

Cite this

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title = "Tuning a Distillation Column Simulator",

abstract = "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.",

keywords = "Data reconciliation, Distillation modelling, Dynamic simulator, Parameter estimation, Data reconciliation, Distillation modelling, Dynamic simulator, Parameter estimation, Data reconciliation, Distillation modelling, Dynamic simulator, Parameter estimation",

author = "H{\"a}ggblom, {Kurt Erik} and Ramkrishna Ghosh",

year = "2011",

doi = "10.1016/B978-0-444-53711-9.50165-6",

language = "Odefinierat/ok{\"a}nt",

isbn = "978-0-444-53895-6",

pages = "823–827",

editor = "EN Pistikopoulos and MC Georgiadis and AC Kokossis",

booktitle = "21st European Symposium on Computer Aided Process Engineering – ESCAPE 21",

publisher = "Elsevier",

note = "ESCAPE ; Conference date: 29-05-2011 Through 01-06-2011",

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TY - GEN

T1 - Tuning a Distillation Column Simulator

AU - Häggblom, Kurt Erik

AU - Ghosh, Ramkrishna

PY - 2011

Y1 - 2011

N2 - 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.

AB - 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.

KW - Data reconciliation

KW - Distillation modelling

KW - Dynamic simulator

KW - Parameter estimation

KW - Data reconciliation

KW - Distillation modelling

KW - Dynamic simulator

KW - Parameter estimation

KW - Data reconciliation

KW - Distillation modelling

KW - Dynamic simulator

KW - Parameter estimation

U2 - 10.1016/B978-0-444-53711-9.50165-6

DO - 10.1016/B978-0-444-53711-9.50165-6

M3 - Konferensbidrag

SN - 978-0-444-53895-6

SP - 823

EP - 827

BT - 21st European Symposium on Computer Aided Process Engineering – ESCAPE 21

A2 - Pistikopoulos, EN

A2 - Georgiadis, MC

A2 - Kokossis, AC

PB - Elsevier

T2 - ESCAPE

Y2 - 29 May 2011 through 1 June 2011

ER -