We
investigated asphaltene adsorption behaviors at the oil–water
interface, focusing on the effect of oil solvents, by molecular dynamics
simulations. Heptane, toluene, and their mixtures with ratios of heptane
to toluene of 25:75, 50:50, and 75:25 by volume (namely, heptol25,
heptol50, and heptol75) were used as the oil models. Two asphaltene
models with essentially the same structure were employed: one contains
a basic pyridine-type nitrogen heteroatom; another contains no heteroatoms.
The asphaltene adsorption Gibbs free energy at the oil–water
interface was evaluated by potential of mean force (PMF) calculations
using the umbrella sampling method. The results show that the oil
solvent not only affects the adsorption Gibbs free energy but also
the adsorption structure as revealed by PMF minimum numbers, locations,
and asphaltene orientation angles. For nitrogen-containing asphaltene,
the adsorption Gibbs free energy increases linearly with the heptane
volume fraction. Noteworthily, the adsorption Gibbs free energy value
of this nitrogen-containing asphaltene is high enough to adsorb at
the toluene–water interface. It implies that solely adding
solvent (such as toluene) may not be enough for solving the emulsion
problems induced by interface-active asphaltenes. For the asphaltene
without heteroatoms, the asphaltene prefers to be solvated in the
oil phase, and there is no well-defined adsorption state when the
heptane volume fraction is less than half. For heptol75–water
and heptane–water interface systems, the asphaltene adsorption
minima can be detected. This clearly indicates that the oil solvent
can influence the surface activity of asphaltenes. The study highlights
the importance of subtle balances of different noncovalent interactions
between asphaltenes, water, and oil components in the oil solvent.
The detailed understanding of the asphaltene adsorption behaviors
presented in this study will be helpful to solve oil–water
emulsion problems and understand the effect of water cut to asphaltene
deposition in crude oil production.