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European Congress of Chemical Engineering - 6
Copenhagen 16-21 September 2007

Abstract 205 - “Development of a Group Contribution Simplified PC-SAFT Equation of State”

“Development of a Group Contribution Simplified PC-SAFT Equation of State”

Advancing the chemical engineering fundamentals

Thermodynamics: Developments with SAFT EOS (T2-1c)

MSc Amra Tihic
Technical University of Denmark
IVC-SEP, Dpt. of Chemical Engineering
IVC-SEP, DTU
Building 229, room 206
2800 Kgs. Lyngby
Denmark
Denmark

Asc. Prof Nicolas von Solms
Technical University of Denmark
IVC-SEP, Dpt. of Chemical Engineering
Technical University of Denmark
Building 229
2800 Kgs. Lyngby
Denmark

Prof Georgios Kontogeorgis
Technical University of Denmark
IVC-SEP, Department of Chemical Engineering
Building 229
DK-2800
Lyngby
Denmark

Prof Michael Michelsen
Technical University of Denmark
IVC-SEP, Department of Chemical Engineering
Building 229
DK-2800
Lyngby
Denmark

PhD Leonidas Constantinou
Frederick Research Center
Dpt. of Chemical Engineering
Frederick Research Center
P.O. Box 24729, Nicosia
Cyprus
Cyprus

Keywords: Equation of state, PC-SAFT, Pure parameters,VLE, LLE

For the development of the various processes in the chemical, pharmaceutical, food, gas processing and petrochemical industry reliable models for the prediction of pure component properties and phase equilibria are required. Our primary focus is development of a group contribution simplified PC-SAFT EoS which will allow the model to be applied to complex mixtures for which experimental data are scarce or not even available.
As a continuation of our previously published work [1], the thermodynamic model developed by our group is a group-contribution version of the simplified Perturbed-Chain Statistical Associating Fluid Theory (PC-SAFT) [2] equation of state where the parameters of the model are estimated via group contributions which are based on the so-called “conjugation principle” [3]. The model has been applied to different families of compounds in order to describe their thermodynamic properties.
Firstly, pure component parameters of PC-SAFT are obtained through a regression method for approximately 550 non-associating compounds. Then we have treated pure compounds of various families including cycloalkenes, nitroalkanes, polynuclear aromatics, ketones, esters, sulphides, siloxanes, plasticizers, cyclo- and fluorinated- hydrocarbons, etc. Secondly, a functional group contribution scheme is developed for the calculation of the PC-SAFT parameters for various functional groups followed by testing the model with the parameters obtained using the group contribution scheme where the results are compared with those of the usual approach (fitting the molecular parameter of each compound to vapor pressure and liquid densities data).

In the presentation, following an outline about, the important steps in the development of the model, typical results of the group-contribution version of the simplified PC-SAFT for pure components as well for the mixtures, and possible applications of industrial interest will be presented.

[1] A. Tihic, G.M. Kontogeorgis, N. von Solms, M.L. Michelsen, Fluid Phase Equilibria 248 (2006), 29
[2] N. von Solms, M.L. Michelsen, G.M. Kontogeorgis, Ind. Eng. Chem. Res., 42 (2003), 1098
[3] L. Constantinou, R. Gani, AIChE J., 40 (1994), 1697

Presented Tuesday 18, 09:05 to 09:25, in session Thermodynamics: Developments with SAFT EOS (T2-1c).

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