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A model for the electric field-driven flow and deformation of a drop or vesicle in strong electrolyte solutions

Published online by Cambridge University Press:  20 June 2022

Manman Ma
Affiliation:
School of Mathematical Sciences, Tongji University, Shanghai 200092, PR China
Michael R. Booty*
Affiliation:
Department of Mathematical Sciences and Center for Applied Mathematics and Statistics, New Jersey Institute of Technology, Newark, NJ 07102, USA
Michael Siegel
Affiliation:
Department of Mathematical Sciences and Center for Applied Mathematics and Statistics, New Jersey Institute of Technology, Newark, NJ 07102, USA
*
†Email address for correspondence: michael.r.booty@njit.edu

Abstract

A model is constructed to describe the flow field and arbitrary deformation of a drop or vesicle that contains and is embedded in an electrolyte solution, where the flow and deformation are caused by an applied electric field. The applied field produces an electrokinetic flow, which is set up on the charge-up time scale $\tau _{*c}=\lambda _{*} a_{*}/D_{*}$, where $\lambda _{*}$ is the Debye screening length, $a_{*}$ is the inclusion length scale and $D_{*}$ is an ion diffusion constant. The model is based on the Poisson–Nernst–Planck and Stokes equations. These are reduced or simplified by forming the limit of strong electrolytes, for which dissolved salts are completely ionised in solution, together with the limit of thin Debye layers. Debye layers of opposite polarity form on either side of the drop interface or vesicle membrane, together forming an electrical double layer. Two formulations of the model are given. One utilises an integral equation for the velocity field on the interface or membrane surface together with a pair of integral equations for the electrostatic potential on the outer faces of the double layer. The other utilises a form of the stress-balance boundary condition that incorporates the double layer structure into relations between the dependent variables on the layers’ outer faces. This constitutes an interfacial boundary condition that drives an otherwise unforced Stokes flow outside the double layer. For both formulations relations derived from the transport of ions in each Debye layer give additional boundary conditions for the potential and ion concentrations outside the double layer.

Information

Type
JFM Papers
Copyright
© The Author(s), 2022. Published by Cambridge University Press
Figure 0

Figure 1.An interior phase $\varOmega _{in}$ with boundary $\partial \varOmega _{in}$ and an exterior phase $\varOmega _{ex}$ with boundary $\partial \varOmega _{ex}$ are separated by the interface $S$ of a drop or a vesicle membrane that is either impervious or nearly impervious to the passage of ions. An electric field with strength $\boldsymbol {E}$ induces a flow of ions that charges up a pair of Debye layers of opposite polarity. The outer edges of the Debye layers are denoted by $S_{+}$ in the exterior phase and $S_{-}$ in the interior phase and the induced flow velocity of the host solvent is denoted by $\boldsymbol {u}$.

Figure 1

Table 1.Variables are made non-dimensional by the quantities shown.

Figure 2

Figure 2.Sketch of characteristics or particle paths $\boldsymbol {x}$ such that ${{\rm d}\kern0.06em \boldsymbol {x}}/{{\rm d}t}=\boldsymbol {u_{0}}$ showing inflow and outflow regions for the Debye layer in the exterior domain $\varOmega _{ex}$. The inflow and outflow regions are separated by the location of the marker ($\bullet$), which is such that $\partial _{n}v_{p}|_{S}=0$ as explained in § 5.4. An impression is given of the deformation of a Lagrangian fluid volume as it enters and leaves the Debye layer. The counterpart in $\varOmega _{in}$ is not shown.

Figure 3

Table 2.Order of magnitude estimate for the terms in the Stokes equation. The estimate for the normal component of the viscous force is revised after considering the tangential component, as explained in the text.

Figure 4

Table 3.Representative scales and dimensionless groups.

Figure 5

Figure 3.Numerical simulation of the electrokinetic flow induced in and around a drop by a uniform applied field with potential $\phi _{\infty }=-\varPsi z$ and dimensionless strength $\varPsi = 5$. (a) The geometry is axisymmetric about the $z$-axis, with the flow magnitude and direction indicated by arrows, at time $t=2.0$. (b) The $\zeta$-potential in the exterior Debye layer $\zeta _{+}$ versus normalised arc length $\bar {s}$ along the interface in a meridional plane. This is shown from drop pole to pole with $\bar {s} \in [0, 1]$ at a sequence of times from $t=0.5$ to $t=2.0$. (c) The tangential fluid velocity $u_{s}$ on the drop interface versus normalised arc length $\bar {s}$ at the same sequence of times.

Figure 6

Figure 4.The data here are analogous to those shown in figure 3 but at increased applied field strength $\varPsi = 10$. (a) The axisymmetric, quadrupolar flow field at time $t=2.0$. (b) The exterior $\zeta$-potential $\zeta _{+}$ and (c) the tangential fluid velocity $u_{s}$ on the interface, both shown versus the normalised pole-to-pole arc length $\bar {s}$, at times from $t=0.5$ to $t=2.0$ as indicated.