Title of article :
Volumetric behavior of the ternary system benzene-2-methoxy-2-methylbutane-2,2,4-trimethylpentane and all binary sub-systems at temperature range (298.15–318.15) K
Author/Authors :
Hou?kov?، نويسنده , , Hana and Mor?vkov?، نويسنده , , Lenka and Sedl?kov?، نويسنده , , Zuzana and Boubl?k، نويسنده , , Tom?? and Kolsk?، نويسنده , , Zde?ka، نويسنده ,
Issue Information :
روزنامه با شماره پیاپی سال 2013
Pages :
9
From page :
156
To page :
164
Abstract :
Densities of ternary liquid mixtures composed of benzene, 2-methoxy-2-methylbutane (i.e. tert-amyl methyl ether, TAME), and 2,2,4-trimethylpentane (i.e. isooctane, 2,2,4-TMP) are measured at three temperatures 298.15 K, 308.15 K, and 318.15 K at atmospheric pressure by a vibrating-tube densimeter as well as all its binary sub-systems. Excess molar volumes of the mixtures are calculated from the experimental densities and then correlated using the Redlich–Kister equation. The determination of its adjustable parameters is made by the method of least squares. For all studied systems, the positive deviations from ideal behavior are observed at all temperatures. The excess molar volume curves of binary systems differ in the shape and temperature dependence. The experimental binary data are compared with literature data and discussed. The ternary system mentioned above is measured newly. Moreover, the experimental excess molar volumes are compared to the calculation using Peng–Robinson equation with a corrected parameter. The novelty of this work is the prediction of ternary excess molar volumes from binary parameters in Peng–Robinson equation.
Keywords :
Benzene , 2 , 4-Trimethylpentane (isooctane) , Density , excess molar volume , Correlation , Redlich–Kister equation , Peng–Robinson equation , 2 , 2-Methoxy-2-methylbutane (tert-amyl methyl ether) , Vibrating-tube densimeter
Journal title :
Fluid Phase Equilibria
Serial Year :
2013
Journal title :
Fluid Phase Equilibria
Record number :
1989327
Link To Document :
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