Due to their lower costs regarding
money and time compared to performing
experiments, computer simulations grow in importance when developing
industrial separation processes. On plant scales, process simulators
are widely applied, and on particular scales, computational fluid
dynamics (CFD) calculations can support design. In this work, the
incompressible Cahn–Hilliard/Navier–Stokes equations
and the non-random two-liquid (NRTL) model were applied to perform
numerical simulations in order to investigate droplet interactions
of extraction systems. In contrast to other CFD approaches, no assumptions
regarding the evolution of drop size distributions are required. The
impact of the influence parameter and mobility coefficient within
this framework was studied for the first time. While the mobility
coefficients show a low impact on the flow field, different values
of the influence parameter can lead to completely different behavior,
with low influence parameters causing small morphologies and requiring
larger grid resolutions in the simulation. A method is proposed to
incorporate various thermodynamic data like phase equilibrium, interfacial
tension, and diffusion coefficients into CFD simulation. Especially,
the interfacial tension is not a direct parameter but rather determines
the density gradient theory (DGT) influence parameter and therefore
enables us to consider the variation of interfacial tensions in a
system with different temperatures or compositions.