TY - JOUR
T1 - Densities, viscosities, and refractive indices of the binary systems (PEG200 + 1,2-propanediol, +1,3-propanediol) and (PEG400 + 1,2-propanediol, +1,3-propanediol) at (288.15 to 333.15) K and atmospheric pressure
T2 - Measurements and modeling
AU - Bajić, Divna M.
AU - Ivaniš, Gorica R.
AU - Visak, Zoran P.
AU - Živković, Emila M.
AU - Šerbanović, Slobodan P.
AU - Kijevčanin, Mirjana Lj
PY - 2013/2/1
Y1 - 2013/2/1
N2 - Densities, viscosities, and refractive indices of four binary systems, (PEG200 + 1,2-propanediol), (PEG200 + 1,3-propanediol), (PEG400 + 1,2-propanediol), (PEG400 + 1,3-propanediol) were measured at 10 temperatures (288.15, 293.15, 298.15, 303.15, 308.15, 313.15, 318.15, 323.15, 328.15, and 333.15) K and at atmospheric pressure. From these data, excess molar volumes, viscosity deviations and deviations in refractive indices were calculated and fitted to the Redlich-Kister equation. The obtained results have been analyzed in terms of the existing specific molecular interactions and the observed mixing behavior between mixture components, taking into considerations the related effect of temperature. The correlations of VE binary data were performed by the Peng-Robinson-Stryjek-Vera cubic equation of state (PRSV CEOS) coupled with the van der Waals (vdW1) mixing rule and CEOS/GE mixing rule introduced by Twu, Coon, Bluck and Tilton (TCBT). The refractive indices of binary mixtures were predicted by various mixing rules and compared with experimental data. The viscosity modelling was done by two types of models: predictive UNIFAC-VISCO and correlative Teja-Rice and McAlister equations. In addition, the experimental values of viscosity were used to determine the new CH2O-CH3, CH2O-CH2, CH 2O-CH, CH2O-OH, CH-CH3, CH-CH2 and CH-OH interaction parameters for their application in the UNIFAC-VISCO model.
AB - Densities, viscosities, and refractive indices of four binary systems, (PEG200 + 1,2-propanediol), (PEG200 + 1,3-propanediol), (PEG400 + 1,2-propanediol), (PEG400 + 1,3-propanediol) were measured at 10 temperatures (288.15, 293.15, 298.15, 303.15, 308.15, 313.15, 318.15, 323.15, 328.15, and 333.15) K and at atmospheric pressure. From these data, excess molar volumes, viscosity deviations and deviations in refractive indices were calculated and fitted to the Redlich-Kister equation. The obtained results have been analyzed in terms of the existing specific molecular interactions and the observed mixing behavior between mixture components, taking into considerations the related effect of temperature. The correlations of VE binary data were performed by the Peng-Robinson-Stryjek-Vera cubic equation of state (PRSV CEOS) coupled with the van der Waals (vdW1) mixing rule and CEOS/GE mixing rule introduced by Twu, Coon, Bluck and Tilton (TCBT). The refractive indices of binary mixtures were predicted by various mixing rules and compared with experimental data. The viscosity modelling was done by two types of models: predictive UNIFAC-VISCO and correlative Teja-Rice and McAlister equations. In addition, the experimental values of viscosity were used to determine the new CH2O-CH3, CH2O-CH2, CH 2O-CH, CH2O-OH, CH-CH3, CH-CH2 and CH-OH interaction parameters for their application in the UNIFAC-VISCO model.
KW - Density
KW - Experimental measurement
KW - Modeling
KW - Refractive index
KW - Viscosity
UR - http://www.scopus.com/inward/record.url?scp=84870247300&partnerID=8YFLogxK
UR - https://www.sciencedirect.com/science/article/pii/S0021961412003035?via%3Dihub
U2 - 10.1016/j.jct.2012.07.024
DO - 10.1016/j.jct.2012.07.024
M3 - Article
AN - SCOPUS:84870247300
SN - 0021-9614
VL - 57
SP - 510
EP - 529
JO - Journal of Chemical Thermodynamics
JF - Journal of Chemical Thermodynamics
ER -