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Thermodynamic modeling of phase and chemical equilibrium in systems with ester synthesis reaction. / Tsvetov, N.; Toikka, A.

2012. Paper presented at 20th International Congress of Chemical and Process Engineering, CHISA 2012 and 15th Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction, PRES 2012, Prague, Czech Republic.

Research output: Contribution to conference › Paper › peer-review

Harvard

Tsvetov, N & Toikka, A 2012, 'Thermodynamic modeling of phase and chemical equilibrium in systems with ester synthesis reaction', Paper presented at 20th International Congress of Chemical and Process Engineering, CHISA 2012 and 15th Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction, PRES 2012, Prague, Czech Republic, 25/08/12 - 29/08/12.

APA

Tsvetov, N., & Toikka, A. (2012). Thermodynamic modeling of phase and chemical equilibrium in systems with ester synthesis reaction. Paper presented at 20th International Congress of Chemical and Process Engineering, CHISA 2012 and 15th Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction, PRES 2012, Prague, Czech Republic.

Vancouver

Tsvetov N, Toikka A. Thermodynamic modeling of phase and chemical equilibrium in systems with ester synthesis reaction. 2012. Paper presented at 20th International Congress of Chemical and Process Engineering, CHISA 2012 and 15th Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction, PRES 2012, Prague, Czech Republic.

Author

Tsvetov, N. ; Toikka, A. / Thermodynamic modeling of phase and chemical equilibrium in systems with ester synthesis reaction. Paper presented at 20th International Congress of Chemical and Process Engineering, CHISA 2012 and 15th Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction, PRES 2012, Prague, Czech Republic.

BibTeX

@conference{8dffbd36a303418f9389013bd766a8f9,
title = "Thermodynamic modeling of phase and chemical equilibrium in systems with ester synthesis reaction",
abstract = "Thermodynamic modeling of equilibria in reacting systems was studied using systems with ester synthesis reaction as an example of multicomponent system with liquid phase splitting. The processes in these systems include several stages, i.e., one or few phase transitions (liquid- liquid, vapor- liquid and chemical reaction. Chemical equilibrium in quaternary reacting systems with ester synthesis reaction (acetic acid-n-propanol- n-propyl acetate-water and acetic acid-ethanol-ethyl acetate-water) was calculated. The results were in good agreement with the experimental data sets on LLE. Model calculations for all ternary subsystems with miscibility gap were carried out. The results confirmed the potentialities of the use UNIFAC model for robust approximation LLE data in this type of reactive systems. This is an abstract of a paper presented at the CHISA 2012 - 20th International Congress of Chemical and Process Engineering and PRES 2012 - 15th Conference PRES (Prague, Czech Republic 8/25-29/2012).",
author = "N. Tsvetov and A. Toikka",
year = "2012",
month = dec,
day = "1",
language = "English",
note = "20th International Congress of Chemical and Process Engineering, CHISA 2012 and 15th Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction, PRES 2012 ; Conference date: 25-08-2012 Through 29-08-2012",

}

RIS

TY - CONF

T1 - Thermodynamic modeling of phase and chemical equilibrium in systems with ester synthesis reaction

AU - Tsvetov, N.

AU - Toikka, A.

PY - 2012/12/1

Y1 - 2012/12/1

N2 - Thermodynamic modeling of equilibria in reacting systems was studied using systems with ester synthesis reaction as an example of multicomponent system with liquid phase splitting. The processes in these systems include several stages, i.e., one or few phase transitions (liquid- liquid, vapor- liquid and chemical reaction. Chemical equilibrium in quaternary reacting systems with ester synthesis reaction (acetic acid-n-propanol- n-propyl acetate-water and acetic acid-ethanol-ethyl acetate-water) was calculated. The results were in good agreement with the experimental data sets on LLE. Model calculations for all ternary subsystems with miscibility gap were carried out. The results confirmed the potentialities of the use UNIFAC model for robust approximation LLE data in this type of reactive systems. This is an abstract of a paper presented at the CHISA 2012 - 20th International Congress of Chemical and Process Engineering and PRES 2012 - 15th Conference PRES (Prague, Czech Republic 8/25-29/2012).

AB - Thermodynamic modeling of equilibria in reacting systems was studied using systems with ester synthesis reaction as an example of multicomponent system with liquid phase splitting. The processes in these systems include several stages, i.e., one or few phase transitions (liquid- liquid, vapor- liquid and chemical reaction. Chemical equilibrium in quaternary reacting systems with ester synthesis reaction (acetic acid-n-propanol- n-propyl acetate-water and acetic acid-ethanol-ethyl acetate-water) was calculated. The results were in good agreement with the experimental data sets on LLE. Model calculations for all ternary subsystems with miscibility gap were carried out. The results confirmed the potentialities of the use UNIFAC model for robust approximation LLE data in this type of reactive systems. This is an abstract of a paper presented at the CHISA 2012 - 20th International Congress of Chemical and Process Engineering and PRES 2012 - 15th Conference PRES (Prague, Czech Republic 8/25-29/2012).

UR - http://www.scopus.com/inward/record.url?scp=84874915291&partnerID=8YFLogxK

M3 - Paper

AN - SCOPUS:84874915291

T2 - 20th International Congress of Chemical and Process Engineering, CHISA 2012 and 15th Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction, PRES 2012

Y2 - 25 August 2012 through 29 August 2012

ER -

ID: 45871123