Thermodynamic modeling of vapor-liquid equilibria and excess properties of the binary systems containing diethers and n-alkanes by cubic equation of state
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2004
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A comparison of the performances of two different approaches of cubic equations of state models, based on a classical van der Waals and mixing rules incorporating the G(E) equation, was carried out for correlation of Vapor-Liquid Equilibria (VLE), H-E and c(P)(E) data alone, and simultaneous correlation of VLE+H-E, VLE+c(P)(E), H-E+c(P)(E) and VLE+H-E+c(P)(E) data for the diethers (1,4-dioxane or 1,3-dioxolane) with n-alkane systems. For all calculations the Peng-Robinson-Stryjek-Vera cubic equation of state (PRSV CEOS) was used. A family of mixing rules for the PRSV CEOS based on the Modified van der Waals one-fluid mixing rule (MvdW1) and two well-known CEOS/GE mixing rules (MHV1 and MHV2), was considered. The NRTL equation, as the G(E) model with linear or reciprocal temperature dependent parameters, was incorporated in the CEOS/G(E) models. The results obtained by the CEOS/G(E) models exhibit significant improvement in comparison to the MvdW1 models.
Ključne reči:
cubic equation of state / thermodynamic properties / diether / n-alkane / simultaneous correlationIzvor:
Korean Journal of Chemical Engineering, 2004, 21, 4, 858-866Izdavač:
- Korean Institute Chemical Engineers, Seoul
DOI: 10.1007/BF02705531
ISSN: 0256-1115
WoS: 000223325700016
Scopus: 2-s2.0-7944236149
Institucija/grupa
Tehnološko-metalurški fakultetTY - JOUR AU - Šerbanović, Slobodan P. AU - Grgurić, Ivona R. AU - Kijevčanin, Mirjana AU - Tasić, AZ AU - Đorđević, Bojan D. PY - 2004 UR - http://TechnoRep.tmf.bg.ac.rs/handle/123456789/703 AB - A comparison of the performances of two different approaches of cubic equations of state models, based on a classical van der Waals and mixing rules incorporating the G(E) equation, was carried out for correlation of Vapor-Liquid Equilibria (VLE), H-E and c(P)(E) data alone, and simultaneous correlation of VLE+H-E, VLE+c(P)(E), H-E+c(P)(E) and VLE+H-E+c(P)(E) data for the diethers (1,4-dioxane or 1,3-dioxolane) with n-alkane systems. For all calculations the Peng-Robinson-Stryjek-Vera cubic equation of state (PRSV CEOS) was used. A family of mixing rules for the PRSV CEOS based on the Modified van der Waals one-fluid mixing rule (MvdW1) and two well-known CEOS/GE mixing rules (MHV1 and MHV2), was considered. The NRTL equation, as the G(E) model with linear or reciprocal temperature dependent parameters, was incorporated in the CEOS/G(E) models. The results obtained by the CEOS/G(E) models exhibit significant improvement in comparison to the MvdW1 models. PB - Korean Institute Chemical Engineers, Seoul T2 - Korean Journal of Chemical Engineering T1 - Thermodynamic modeling of vapor-liquid equilibria and excess properties of the binary systems containing diethers and n-alkanes by cubic equation of state EP - 866 IS - 4 SP - 858 VL - 21 DO - 10.1007/BF02705531 ER -
@article{ author = "Šerbanović, Slobodan P. and Grgurić, Ivona R. and Kijevčanin, Mirjana and Tasić, AZ and Đorđević, Bojan D.", year = "2004", abstract = "A comparison of the performances of two different approaches of cubic equations of state models, based on a classical van der Waals and mixing rules incorporating the G(E) equation, was carried out for correlation of Vapor-Liquid Equilibria (VLE), H-E and c(P)(E) data alone, and simultaneous correlation of VLE+H-E, VLE+c(P)(E), H-E+c(P)(E) and VLE+H-E+c(P)(E) data for the diethers (1,4-dioxane or 1,3-dioxolane) with n-alkane systems. For all calculations the Peng-Robinson-Stryjek-Vera cubic equation of state (PRSV CEOS) was used. A family of mixing rules for the PRSV CEOS based on the Modified van der Waals one-fluid mixing rule (MvdW1) and two well-known CEOS/GE mixing rules (MHV1 and MHV2), was considered. The NRTL equation, as the G(E) model with linear or reciprocal temperature dependent parameters, was incorporated in the CEOS/G(E) models. The results obtained by the CEOS/G(E) models exhibit significant improvement in comparison to the MvdW1 models.", publisher = "Korean Institute Chemical Engineers, Seoul", journal = "Korean Journal of Chemical Engineering", title = "Thermodynamic modeling of vapor-liquid equilibria and excess properties of the binary systems containing diethers and n-alkanes by cubic equation of state", pages = "866-858", number = "4", volume = "21", doi = "10.1007/BF02705531" }
Šerbanović, S. P., Grgurić, I. R., Kijevčanin, M., Tasić, A.,& Đorđević, B. D.. (2004). Thermodynamic modeling of vapor-liquid equilibria and excess properties of the binary systems containing diethers and n-alkanes by cubic equation of state. in Korean Journal of Chemical Engineering Korean Institute Chemical Engineers, Seoul., 21(4), 858-866. https://doi.org/10.1007/BF02705531
Šerbanović SP, Grgurić IR, Kijevčanin M, Tasić A, Đorđević BD. Thermodynamic modeling of vapor-liquid equilibria and excess properties of the binary systems containing diethers and n-alkanes by cubic equation of state. in Korean Journal of Chemical Engineering. 2004;21(4):858-866. doi:10.1007/BF02705531 .
Šerbanović, Slobodan P., Grgurić, Ivona R., Kijevčanin, Mirjana, Tasić, AZ, Đorđević, Bojan D., "Thermodynamic modeling of vapor-liquid equilibria and excess properties of the binary systems containing diethers and n-alkanes by cubic equation of state" in Korean Journal of Chemical Engineering, 21, no. 4 (2004):858-866, https://doi.org/10.1007/BF02705531 . .