Inertial effects on the interphase drag force and rheology of dilute suspensions of buoyant droplets at low Reynolds number

In this work, we compute the hydrodynamic force and the first and second moments of force acting on a translating spherical droplet immersed in a uniform flow using the reciprocal theorem. We consider the low but finite Reynolds number regime,

, and the dilute limit of small droplet volume fraction

phi ϕ $\phi$

. Here,

upper U U $U$

denotes the magnitude of the relative velocity between the phases,

a a $a$

the droplet radius and

rho Subscript f ρ f $\rho _{\!f}$

and

mu Subscript f μ f $\mu _{\!f}$

the density and viscosity of the continuous phase, respectively. We show that the

upper O left parenthesis italic Re right parenthesis O ( Re ) $O(\textit{Re})$

inertial corrections to the first and second moments of force scale as

upper O left parenthesis rho Subscript f Baseline phi upper U squared right parenthesis O ( ρ f ϕ U 2 ) $O(\rho _{\!f} \phi U^2)$

and

upper O left parenthesis a rho Subscript f Baseline phi upper U squared right parenthesis O ( a ρ f ϕ U 2 ) $O(a\rho _{\!f}\phi U^2)$

, respectively. Equivalently, in dimensionless form, these corrections scale as

upper O left parenthesis phi italic Re right parenthesis O ( ϕ Re ) $O(\phi \textit{Re})$

and

upper O left parenthesis left parenthesis a divided by upper R right parenthesis phi italic Re right parenthesis O ( ( a / R ) ϕ Re ) $O(({a}/{R})\phi \textit{Re})$

, where

upper R R $R$

denotes the macroscopic length scale. Moreover, the ensemble average of the drag force and the higher-order force moments over the distribution of droplet velocities introduces additional contributions proportional to the velocity variance of the dispersed phase, both in the interphase momentum exchange and in the effective stress of the continuous phase. As a consequence, in dilute emulsions of buoyant droplets, the effective stress depends quadratically on the relative velocity between the phases, on the velocity variance of the dispersed phase and on the spatial gradients of these quantities. Finally, we consider a steady-state pipe flow to examine how the force moments derived in this study affect the behaviour of the two-phase flow in this particular configuration.