Abstract
The main aim of this modeling investigation is to improve the performance of the gradient theory for binary systems of methane and n-alkane. To achieve this aim, the gradient theory (GT) is combined with the volume-translated Peng-Robinson equation of state (VTPR EOS) for accurate description of phase equilibrium and surface tensions of methane/hydrocarbon systems. To improve the phase equilibrium calculations, the binary interaction parameters of VTPR EOS for methane/hydrocarbon systems have been determined based on the mole fraction of methane in liquid phase. A new correlation of the influence parameter based on the densities of bulk phases has been suggested. To make the present model predictive, the binary interaction parameters of the mixture influence parameter have been set equal to zero. The results of the model show that the predictions of the present model agree well with experimental surface tensions, especially for very low values of surface tensions (near-critical interfaces).
Highlights
The accurate determination of the physical properties for systems plays a dominant role in the petroleum industry
To improve the phase equilibrium calculations, the binary interaction parameters of volume-translated Peng–Robinson (VTPR) EOS for methane/hydrocarbon systems have been determined based on the mole fraction of methane in liquid phase
This form of influence parameter has been proposed for gradient theory
Summary
The accurate determination of the physical properties for (oil+gas) systems plays a dominant role in the petroleum industry. The gradient theory (GT) is combined with the volume-translated PengRobinson equation of state (VTPR EOS) for accurate description of phase equilibrium and surface tensions of methane/ hydrocarbon systems. The gradient theory of fluid interfaces [3,4,5] is one of the prediction models combining density (or volume) with the surface tension.
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