Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
Graphical abstract
Experimental and calculated partial molar volumes () of MIK with (♦) 2-PrOH, (♢) 2-BuOH, (●) 2-PenOH at T = 298.15 K. (—) PC-SAFT model.
Introduction
Thermodynamic properties of binary non-electrolyte mixtures are very valuable in the study of the type and nature of molecular interactions. Experimental densities and viscosities for binary mixtures are necessary to develop the equations of state. The aims of this study are to understand the intermolecular interactions between the methyl isobutyl ketone and 2-alkanols with different alkyl chain length. As a part of our systematic studies on the thermodynamic and transport properties of liquid mixtures containing 2-alkanols in previous papers [1], [2], [3], here, densities, viscosities, excess molar volumes and viscosity deviations of mixing for the binary mixtures of methyl isobutyl ketone with 2-propanol, 2-butanol and 2-pentanol at temperature intervals 293.15–323.15 K are reported. A survey of literature shows that there are few data about this kind of mixtures [4], [5]. Also prediction or correlation of volumetric properties with the PC-SAFT model is other background of this work. PC-SAFT model is able to predict the effects of molecular weight and hydrogen bonding on the thermodynamic properties of complex fluids and mixtures. In this paper PC-SAFT model has been applied to correlate and predict the values of isobaric thermal expansibility and partial molar volumes. Complete description of these systems requires three physically meaningful temperature-independent parameters: the segment number (m), the hard-core segment diameter (σ), and the segment-segment interaction energy parameter () for each pure non-associating fluid. They are typically fitted to vapour pressure and liquid density data. Associating fluids require two additional compound parameters, the association energy (), and the association volume (κAB).
Section snippets
Experimental section
Methyl isobutyl ketone, 2-propanol, 2-butanol and 2-pentanol were obtained from Merck with mass purity >99%. All of the materials were used without further purification. In Table1, we compared the measured densities and viscosities at T = 298.15 K with values available in the literature [6], [7]. Density and viscosity measurements were performed with a fully automated SVM 3000 Anton-Paar rotational Stabinger viscometer. The viscometer is based on a modified Couette principle with a rapidly
Densities and excess molar volumes
Excess molar volumes, for studied mixtures, were calculated at different temperatures by use of the following equation:where ρ is the density of the mixture, ρi is the density of pure component i, xi is the mole fraction, Mi is the molar mass of component i, and N stands for the number of components in the mixture. Excess molar volumes for binary mixtures of MIK + 2-alkanols at T = 298.15 K are plotted in Fig. 1. Values of densities are reported in Table 2. The values
Conclusions
This paper reports the densities and viscosities for binary mixtures of MIK and 2-alkanol. Excess molar volumes, isobaric thermal expansivity, partial molar volumes, and viscosity deviations were calculated from experimental data. Excess molar volumes are positive and viscosity deviations are negative over the whole composition range. The ability of the PC-SAFT equations of state to reproduce the volumetric behavior of the mixtures was also tested at various temperatures. Overall, PC-SAFT
Acknowledgments
The author thanks the University authorities for providing the necessary facilities to carry out this research project (Tarhe Pajooheshi).
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