Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Experimental and theoretical surface tension deviations in the binary systems propyl propanoate + o-, m- and p-xylene at 298.15K

Dominguez-Perez, M.[Montserrat], Segade, Luisa, Franjo, C.[Carlos], Cabeza, Oscar, Jimenez, E.[Eulogio]
Fluid Phase Equilib. 2005, 232, 1-2, 9-15
ABSTRACT
This paper reports on the surface tension of the binary mixtures {propyl propanoate + o-xylene}, {propyl propanoate +m-xylene} and {propyl propanoate + p-xylene} at the temperature 298.15K and atmospheric pressure, over the whole composition range. The surface tension deviations obtained were correlated with a Redlich Kister type equation. These data were compared with five different theoretical approaches. Among them we apply the theories of Hildebrand and Scott for ideal solutions and their extension of Guggenheim s ideal solution equation, valid for systems containing molecules of significantly different size; the Brock and Bird theory, based only in the critical values of the pure compounds; the Sudgen s equation based in the parachor, which needs the knowledge of density for the whole composition in the mixture; and finally, the Prigogine s refined theory, which takes into account the critical values and the temperature dependence of surface tension.We will discuss results from those five theoretical models applied to the experimental data presented in this work, and also to other previously published data. Also, we will discuss the influence of the surface molar area parameter value on the models that need it. (C) 2005 Elsevier B.V. All rights reserved.
Compounds
# Formula Name
1 C6H12O2 propyl propanoate
2 C8H10 1,2-dimethylbenzene
3 C8H10 1,3-dimethylbenzene
4 C8H10 1,4-dimethylbenzene
Datasets
The table above is generated from the ThermoML associated json file (link above). POMD and RXND refer to PureOrMixture and Reaction Datasets. The compound numbers are included in properties, variables, and phases, if specificied; the numbers refer to the table of compounds on the left.
Type Compound-# Property Variable Constraint Phase Method #Points
  • POMD
  • 1
  • Surface tension liquid-gas, N/m ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Drop volume
  • 1
  • POMD
  • 2
  • Surface tension liquid-gas, N/m ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Drop volume
  • 1
  • POMD
  • 3
  • Surface tension liquid-gas, N/m ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Drop volume
  • 1
  • POMD
  • 4
  • Surface tension liquid-gas, N/m ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Drop volume
  • 1
  • POMD
  • 2
  • 1
  • Surface tension liquid-gas, N/m ; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Drop volume
  • 17
  • POMD
  • 1
  • 3
  • Surface tension liquid-gas, N/m ; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Drop volume
  • 12
  • POMD
  • 1
  • 4
  • Surface tension liquid-gas, N/m ; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Drop volume
  • 18