An overview of the molecular simulation studies of the
oil+brine
two-phase system in the presence of CO2, CH4, and their mixture at geological conditions is presented. The simulation
results agreed well with the experimental results and the density
gradient theory predictions on the basis of the cubic–plus–association
equation of state (CPA EoS) (withDebye–Hückel electrostatic
term) and the perturbed chain statistical associating fluid theory
(PC-SAFT) EoS. The interfacial tension (IFT) of the alkane+H2O system showed almost a linear increase with an increasing number
of carbon atoms in the alkane molecule. These IFTs are approximately
equal for linear, branched, and cyclic alkanes. Here, the negative
surface excess of the alkanes might explain the increase in the IFTs
with an increase in the pressure. The surface excesses of the alkanes
increased with decreasing temperature. This may explain the decrease
of the slopes in the IFT versus pressure plot with a decrease in the
temperature. The IFT behavior of the alkane+water+CH4/CO2 system was found to be similar to that observed for the alkane+water
system. The addition of CO2 had a more significant influence
on the IFT than the addition of CH4. Here, CH4 and CO2 exhibited a positive surface excess. The negative
surface excess of the salt ions probably explains the increase in
the IFTs of the alkane+brine system with increasing salt content.
The solubilities of CH4 and/or CO2 in the H2O-rich phase of the alkane+brine+CH4/CO2 system increased with decreasing salt content (salting-out effect).
The IFT of the aromatic hydrocarbon+H2O system is much
lower than that of the alkane+H2O system. The surface excess
followed the order o-xylene > ethylbenzene >
toluene
> benzene for the aromatic hydrocarbon+H2O system. This
trend has a direct correlation with the aromatic–aromatic interaction.