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

Kurt Erik Häggblom
, Ramkrishna Ghosh

Tutkimustuotos: Artikkeli kirjassa/raportissa/konferenssijulkaisussa › Konferenssiartikkeli › Tieteellinen › vertaisarvioitu

Abstrakti

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.

Alkuperäiskieli	Ei tiedossa
Otsikko	21st European Symposium on Computer Aided Process Engineering – ESCAPE 21
Toimittajat	EN Pistikopoulos, MC Georgiadis, AC Kokossis
Kustantaja	Elsevier
Sivut	823–827
ISBN (painettu)	978-0-444-53895-6
DOI - pysyväislinkit	https://doi.org/10.1016/B978-0-444-53711-9.50165-6
Tila	Julkaistu - 2011
OKM-julkaisutyyppi	A4 Artikkeli konferenssijulkaisuussa
Tapahtuma	ESCAPE - 21st European Symposium on Computer Aided Process Engineering – ESCAPE 21 Kesto: 29 toukok. 2011 → 1 kesäk. 2011

Konferenssi

Konferenssi	ESCAPE
Ajanjakso	29/05/11 → 01/06/11

Keywords

Data reconciliation
Distillation modelling
Dynamic simulator
Parameter estimation

Pääsy asiakirjaan

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

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

Viittausmuodot

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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",

}

Tuning a Distillation Column Simulator. / Häggblom, Kurt Erik; Ghosh, Ramkrishna.
21st European Symposium on Computer Aided Process Engineering – ESCAPE 21. toim. / EN Pistikopoulos; MC Georgiadis; AC Kokossis. Elsevier, 2011. s. 823–827.

Tutkimustuotos: Artikkeli kirjassa/raportissa/konferenssijulkaisussa › Konferenssiartikkeli › Tieteellinen › vertaisarvioitu

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 - Publicerad konferensartikel

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 -