1. Introduction
Electrophoresis describes the motion of a charged particle suspended in an electrolyte under an applied electric field (Hunter Reference Hunter1993). For moderately charged particles with an electrical double layer (EDL) much thinner than the particle size, the electrophoretic velocity is given by the Helmholtz–Smoluchowski relation,
$\boldsymbol {U}_{\!{ep}} = (\varepsilon \zeta _0/\eta )\,\boldsymbol {E}$
, where
$\varepsilon$
is the electrolyte permittivity,
$\zeta _0$
is the particle zeta potential,
$\eta$
represents the dynamic viscosity of the fluid and
$\boldsymbol {E}$
is the imposed electric field (von Smoluchowski Reference von Smoluchowski1903). The EDL consists of the surface charge and the surrounding diffuse ionic cloud that screens it electrostatically (Hunter Reference Hunter1993).
Electrophoresis has found widespread applications, from biomolecular separation by gel electrophoresis (Zhu et al. Reference Zhu, Lu and Liu2012) to transport and flow control in microfluidic devices (Stone et al. Reference Stone, Stroock and Ajdari2004). More recently, experiments have examined its interplay with pressure-driven flows in microchannels (Vishwanathan & Juarez Reference Vishwanathan and Juarez2023; Abdorahimzadeh et al. Reference Abdorahimzadeh, Pratiwi, Vainio, Liimatainen and Elbuken2023, Reference Abdorahimzadeh, Bölükkaya, Vainio, Liimatainen and Elbuken2024; Li & Xuan Reference Li and Xuan2018), revealing lateral migration of micro- and nanoparticles perpendicular to both the electric field and the mean flow. Depending on the operating conditions, particles migrate either toward the channel centreline or the walls, offering a promising mechanism for particle focusing, enrichment and fractionation.
Despite its potential for particle manipulation and separation, the physical origin of this cross-stream migration remains unclear. Although lateral migration in microchannels is commonly attributed to fluid inertia (Di Carlo et al. Reference Di Carlo, Irimia, Tompkins and Toner2007), the effect considered here arises only from the combination of pressure-driven flow and an applied electric field. Recent studies (Choudhary et al. Reference Choudhary, Renganathan and Pushpavanam2019; Khair & Kabarowski Reference Khair and Kabarowski2020) examined inertial migration under simultaneous shear and electrophoresis. In particular, Khair & Kabarowski (Reference Khair and Kabarowski2020) predicted lateral velocities that are too small under typical experimental conditions, indicating that inertia alone cannot explain the experimentally observed migration.
(a) The colour map shows the concentration polarisation around a spherical particle suspended in a quiescent electrolyte. The ionic concentration increases on one side of the particle (
$\delta c \gt 0$
) and decreases on the opposite side (
$\delta c \lt 0$
). (b) Concentration polarisation around a spherical particle subjected to a linear shear flow. Advection of ions by the flow perturbs the concentration field, thereby breaking the symmetry with respect to the YZ plane. (c) Schematic representation of the problem: a spherical particle is simultaneously subjected to a uniform electric field and a linear shear rate.

In this work, we investigate concentration polarisation (CP) around a colloidal particle subjected to an external electric field (Dukhin & Shilov Reference Dukhin and Shilov1974). Concentration polarisation is the formation of ionic concentration gradients around the particle, which is caused by surface conduction within the EDL: electromigration of counterions depletes ions on one side of the particle and enriches them on the other. Figure 1(a) illustrates this asymmetric concentration field, which results from the balance between surface electromigration and diffusive transport. Here
$\delta c=c-c_0$
, where
$c$
is the salt concentration at a given point and
$c_0$
is the background electrolyte concentration.
We consider a particle subjected to simultaneous electric and flow fields. Although pressure-driven microchannel flows are Poiseuille-like, the local flow is well approximated by a linear shear when the particle is much smaller than the channel dimensions. Shear enters the convection–diffusion equation governing the ionic concentration and, through ion advection, breaks the symmetry of the concentration field with respect to the YZ plane, as illustrated in figure 1(b). This symmetry breaking induces an electrophoretic velocity with a component perpendicular to the applied electric field.
2. Problem formulation
We consider a dielectric sphere with negative surface charge density
$q_s$
, suspended in a binary electrolyte with ionic diffusivities
$D_+$
and
$D_-$
, and subjected to a DC electric field and a linear shear flow (figure 1
c). Our goal is to determine its electrophoretic velocity. To this end, we adopt the electrokinetic framework developed by Schnitzer and Yariv for large zeta potentials (Schnitzer & Yariv Reference Schnitzer and Yariv2012) (hereafter, the SY model), which has been successfully applied to electrophoresis (Schnitzer et al. Reference Schnitzer, Zeyde, Yavneh and Yariv2013; Schnitzer & Yariv Reference Schnitzer and Yariv2014) and CP electroosmotic flows (Calero et al. Reference Calero, Fernández-Mateo, Morgan, García-Sánchez and Ramos2021; Fernández-Mateo et al. Reference Fernández-Mateo, García-Sánchez, Calero, Morgan and Ramos2021). The SY model provides the governing equations for the electric potential
$\phi$
, ionic concentration
$c$
and fluid velocity
$\boldsymbol {u}$
in the bulk electrolyte under the thin EDL approximation, appropriate for the experiments mentioned above where microscopic particles are dispersed in electrolytes with typical values of the Debye length in the range 10–100 nm.
We adopt a reference frame fixed at the centre of mass of the particle, and express the governing equations in non-dimensional form using the following characteristic scales: the particle radius
$a$
as the length scale; the bulk ionic concentration
$c_0$
as the concentration scale; and the thermal voltage for the electric potential,
$V_{{th}}=k_{{B}} T/{ze}$
, where
$T$
is the absolute temperature,
$k_{ B}$
is the Boltzmann constant,
$z$
is the ionic valence and
$e$
is the elementary charge. For a
$1:1$
electrolyte at room temperature, the thermal voltage is
$V_{{th}}\approx 25\,\mathrm{mV}$
. Velocities are scaled by
$\varepsilon V_{{th}}^2/(a\eta )$
, which in turn defines the characteristic time scale as
$a^2\eta /(\varepsilon V_{{th}}^2)$
. Consequently, diffusion coefficients are scaled by
$\varepsilon V^2_{{th}}/\eta$
. The dimensionless ambipolar diffusion coefficient is
$D=2D_+D_-/(D_++D_-)$
. The non-dimensional governing equations are
Equation (2.1) is the convection–diffusion equation for the ion concentration, while the equation for the electric potential (2.2) corresponds to the continuity of the electrical current with
$\alpha \equiv(D_+^{-1}-D_-^{-1})/2$
. Equations (2.3) are the Stokes equations for the fluid velocity
${\boldsymbol{u}}$
and pressure
$p$
(negligible Reynolds number) including a body force term of electrical origin.
The SY model also establishes the boundary conditions (BCs) at the particle surface. The model assumes that the particle zeta potential is much larger than the thermal voltage, i.e.
$\zeta _0 \gg 25\,\mathrm{mV}$
, an assumption that is well satisfied in the experiments described above involving carboxylate microspheres. Under these conditions, co-ions are effectively excluded from the diffuse layer, while the counter-ion flux normal to the surface is balanced by the surface current within the EDL. As a result, the following BCs are obtained:
where
$\boldsymbol{\nabla} _s$
denotes the surface gradient operator tangent to the particle, and
${\textit{Du}}$
is the dimensionless Dukhin number, which quantifies the relative contribution of surface to bulk currents (Delgado et al. Reference Delgado, Gonzalez-Caballero, Hunter, Koopal and Lyklema2005).
Concerning the fluid velocity at the particle surface, the SY model prescribes the following slip BC, which coincides with the expression derived in (Prieve et al. Reference Prieve, Anderson, Ebel and Lowell1984) in the context of diffusiophoresis:
where the non-dimensional zeta potential
$\zeta$
is related to the non-dimensional surface charge density,
$q_s$
, and ion concentration through the Gouy–Chapman equation
$q_s=2\sqrt {c}\sinh {(\zeta /2)}$
(Hunter Reference Hunter1993). The BC for the fluid velocity at the particle surface is
where
$\boldsymbol{\varOmega }$
is the angular velocity of the spherical particle.
In the far field (
$\boldsymbol{r}\rightarrow \infty$
), the electric potential and ionic concentration approach their imposed values,
$\phi =-\beta z$
and
$c=1$
, with
$\beta =E_0(a/V_{{th}})$
. Since the reference frame is attached to the particle, the fluid velocity approaches
$\boldsymbol{u}=\Gamma x\hat {\boldsymbol{z}}-\boldsymbol{U}$
far from the particle, where
$\Gamma =(\varepsilon V_{{th}}^2/a^2\eta )\dot {\gamma }$
and
$\boldsymbol{U}$
is the electrophoretic velocity. The translational and angular velocities,
$\boldsymbol{U}$
and
$\boldsymbol{\varOmega }$
, are determined by enforcing zero net hydrodynamic force and torque,
$\oint _{S} \tilde {\boldsymbol{T}}\boldsymbol{\cdot }{\rm d}\boldsymbol{S} = 0$
and
$\oint _{S} (\boldsymbol {r}\times \tilde {\boldsymbol{T}})\boldsymbol{\cdot }{\rm d}\boldsymbol{S} = 0$
, where
$\tilde {\boldsymbol{T}}$
is the hydrodynamic stress tensor and the integrals are evaluated over a closed surface enclosing the sphere and located sufficiently far from it.
Although the SY model was originally derived for a particle in a quiescent fluid, an imposed flow could, in principle, affect ion transport within the EDL and modify the BCs (2.4). Nevertheless, following the analysis in Yariv et al. (Reference Yariv, Schnitzer and Frankel2011) for the streaming potential generated by a falling sphere, the charge-advection contribution scales as
$q_s u \delta$
, with
$\delta$
the dimensionless Debye length. In the thin-EDL limit and under typical experimental conditions, this term is negligible compared with the electromigration current associated with surface conductance. Hence, the BCs (2.4) remain unchanged.
3. Problem analysis and perturbation scheme
We seek an analytical expression for the particle velocity in the limit of weak electric and shear forcing. To this end, the governing fields are expanded asymptotically in powers of the dimensionless electric-field strength,
$\beta$
, and the dimensionless shear rate,
$\Gamma$
,
where the first subscript denotes the order of the expansion in
$\Gamma$
, while the second denotes the order in
$\beta$
. The fields
$\phi _{10}$
and
$c_{10}$
are omitted here since, in the thin-EDL limit and without an applied electric field, the shear flow does not perturb the electric potential or the ionic concentration, as discussed in the previous section (Yariv et al. Reference Yariv, Schnitzer and Frankel2011). For the same reason, terms proportional to
$\Gamma ^2$
do not appear in our second-order expansion. Likewise, higher-order electric-field contributions do not affect lateral migration because the system remains axially symmetric around the sphere in the absence of shear flow. Consequently, our perturbation expansion up to second order retains only the velocity term proportional to
$\Gamma \beta$
.
3.1. Solutions at first order in the electric field and zeroth order in the shear flow
The equations for
$c_{01}$
and
$\phi _{01}$
are, respectively,
with BCs at the particle surface,
$r=1$
,
BCs far from the particle are (
$r \to \infty$
):
$c_{01} \to 0, \quad \phi _{01} \to -r \cos \theta$
.
The solutions for
$c_{01}$
and
$\phi _{01}$
are
which are coincident with the expressions in Schnitzer & Yariv (Reference Schnitzer and Yariv2012) and in Hunter (Reference Hunter1993) for a thin EDL and a highly charged surface.
The velocity field
$\boldsymbol{u}_{01}$
is governed by the equations
with BC at the particle surface:
$ \boldsymbol{u}^s_{01} = \zeta _0\boldsymbol{\nabla} _s\phi _{01} - 4\ln (\cosh (\zeta _0/4) )\boldsymbol{\nabla} _s c_{01}$
.
Far from the particle, the velocity field approaches the negative electrophoretic velocity,
$\boldsymbol{u}_{01} \to -\boldsymbol{U}_{01}$
, which is determined by the zero-net-force condition on the particle. The solution for
$\boldsymbol{U}_{01}$
is
This expression is in agreement with the results given by Schnitzer et al. (Reference Schnitzer, Zeyde, Yavneh and Yariv2013).
3.2. Solutions at zeroth order in the electric field and first order in the shear flow
At this order, the velocity field
$\boldsymbol{u}_{10}$
is the only field that remains to be solved, and it is governed by the Stokes equations
Far from the particle, the velocity approaches the undisturbed shear flow:
$ \boldsymbol{u}_{10} \to x\hat {\boldsymbol{z}}$
as
$r \to \infty$
. The following no-slip BC applies at the particle surface:
$ \boldsymbol{u}_{10} = \boldsymbol{\varOmega }\times \boldsymbol{r}$
, at
$r=1$
, where the angular velocity
$\boldsymbol{\varOmega }$
is determined by the hydrodynamic zero-net-torque condition on the particle. The solution for this velocity field is well known (Leal Reference Leal2007, ch. 8) and can be expressed as
with the particle rotation given by
$\boldsymbol{\varOmega } = -(1/2)\hat {\boldsymbol{y}}$
.
3.3. Solutions at first order in the electric field and first order in the shear flow
Equations governing
$c_{11}$
and
$\phi _{11}$
are
with BCs at the particle surface,
$r=1$
,
Far from the particle,
$r \to \infty$
:
$c_{11} \to 0$
and
$\phi _{11} \to 0$
.
Using the results from the previous sections, the source term in (3.11) can be expressed in terms of the following associated Legendre polynomials of order 1,
$P^1_1(\cos (\theta ))$
and
$P^1_3(\cos (\theta ))$
:
with
$A=({1}/{D})({3{\textit{Du}}}/{(2+4{\textit{Du}})})$
. Because the source term in (3.14) decays as
$\mathcal{O}(r^{-2})$
, the solution of (3.11) cannot satisfy the far-field BC: the general solution for
$c_{11}$
presented below does not vanish as
$r\to \infty$
where
$f(r) = A (-({1}/{5}) + ({1}/{4r^3}) - ({1}/{20r^5}) )$
,
$g(r) = A (-({1}/{30}) + ({1}/{9r^3}) + ({1}/{30r^5}) )$
and
$A_1,A_2,B_1$
and
$B_2$
are integration constants.
For (3.12), this issue can be circumvented by introducing the change of variables
$\psi _{11}=\phi _{11}-\alpha Dc_{11}$
. Consequently, (3.12) reduces to
${\nabla} ^2\psi _{11}=0$
, which ensures that
$\psi _{11}$
vanishes as
$r\to \infty$
. BCs for
$\psi _{11}$
on the particle surface are
while it vanishes far from the particle (
$\psi _{11}\to 0$
as
$r\to \infty$
).
The breakdown of the regular perturbation scheme for
$c_{11}$
is analogous to the Whitehead paradox for heat transfer from a sphere in a uniform flow, where no uniformly valid solution exists for the temperature field in the limit of
${\textit{Pe}} \to 0$
(Leal Reference Leal2007, ch. 9). Here,
${\textit{Pe}}$
denotes the Péclet number, which quantifies the ratio of convective to diffusive transport. In our problem,
${\textit{Pe}}=\Gamma /D$
when defined using the particle radius as the characteristic length scale. This paradox arises because the local Péclet number (which in our problem scales as
${\textit{Pe}}(r) = \Gamma r^2 / D$
) cannot remain arbitrarily small throughout an unbounded domain. Consequently, a proper solution for
$c_{11}$
and
$\psi _{11}$
– including the unambiguous determination of the integration constants – must be sought within the framework of a singular perturbation analysis using the method of matched asymptotic expansions, as detailed in the next section.
Before proceeding with the asymptotic matching, we present the general solution for
$\psi _{11}$
where the constants
$C_1$
and
$D_1$
are coupled to those in (3.15) via the BCs at
$r=1$
(3.16)
4. Far-field analysis and asymptotic matching
As mentioned above, the convective term in (2.1) cannot be neglected at arbitrarily large length scales, as it becomes comparable to or dominant over diffusion in regions where
$r \ge {\textit{Pe}}^{-1/2}$
. Consequently, we must seek an outer solution, denoted as
$C(\boldsymbol{r})$
, valid in this far-field domain. This solution will subsequently be matched asymptotically with the near-field (inner region) solution, which holds where
$r \ll {\textit{Pe}}^{-1/2}$
. To this end, we introduce the rescaled coordinate
$\bar {r} = r \sqrt {{\textit{Pe}}}$
. This scaling yields a distinguished limit that balances the diffusive and convective terms in the equation for
$C(\boldsymbol{r})$
as
${\textit{Pe}} \to 0$
(Leal Reference Leal2007, ch. 9.F).
Under the coordinate transformation
$\bar {r} = r \sqrt {{\textit{Pe}}}$
, the conservation equation (2.1) at order
$\beta$
becomes
By neglecting higher-order terms in the limit
${\textit{Pe}} \to 0$
, we obtain the leading-order governing equation in the outer region
The asymptotic matching condition requires that the inner limit of the outer solution matches the outer limit of the inner solution, namely,
$\lim _{\bar {r} \to 0} C_0(\bar {r}) = \lim _{r \to \infty } c(r)$
.
A general solution to (4.2) that satisfies the far-field BC (
$\lim _{\bar {r} \to \infty }C(\bar {r}) = 0$
) was derived by Elrick (Leal Reference Leal2007, ch. 9.F) in the context of the temperature distribution produced by a point heat source in a simple shear flow. This solution reads as follows:
where
$M$
is a constant and
$s$
a dummy variable of integration. In our case, given the far-field behaviour of
$c_{01}$
((3.6)) the source for
$C_0$
corresponds to a point dipole located at the origin and oriented along the
$z$
-direction. By analogy with electrostatics, where a dipole field is related to a monopole field via a directional derivative, the solution to our problem can be obtained directly from (4.3) as
$C_0(\bar {\boldsymbol{r}}) = -\partial T_0 / \partial \bar {z}$
In the limit
$r \to 0$
, the dominant contribution to the integral in (4.4) arises from the region where
$s \sim \bar r^2 \to 0$
. Consequently, the asymptotic behaviour of (4.4) near the origin can be determined analytically by expanding the integrand for small values of
$s$
. It is straightforward to show that
$C_0(\bar {\boldsymbol{r}}) \approx M ( \bar z/\bar r^3 - \bar x/4\bar r + \bar z^2\bar x/4\bar r^3)$
, where we have retained terms that, upon reverting the change of variables, yield contributions up to order
$\textit{Pe}$
. Indeed, the evaluation yields
By comparing this result with the
$c_{01}$
term of the inner solution, we obtain
$M/\textit{Pe}=\textit{DA} = ({3\textit{Du}}/{(2+4\textit{Du})})$
. Asymptotic matching up to order
$\textit{Pe}$
then requires that
$\textit{Pe}\,c_{11}|_{r \gg 1} = (C_0 - \textit{DA}\cos \theta /\bar {r}^2 )|_{\bar {r} \ll 1}$
, which implies that
$A_2 = B_2 = 0$
.
5. Results for the cross-stream migration velocity
We now evaluate the slip velocity, (2.5), on the particle surface to calculate the translation velocity
$\boldsymbol{U}$
. By applying the Lorentz reciprocal theorem for Stokes flows (Masoud & Stone Reference Masoud and Stone2019), the velocity of a force-free spherical particle is determined from the surface average of the slip velocity
where the integration is performed over the particle surface
$S_{\!p}$
. Substituting the leading-order slip velocity
$\boldsymbol{u}^s_{01}$
into (5.1) yields the standard electrophoretic velocity
$U_{01}$
, (3.8), while the
$x$
-component of the term
$\boldsymbol{u}^s_{11}$
provides the cross-stream particle velocity
$U_x$
. Substituting the constants from (3.18)–(3.21) with
$A_2=B_2=0$
leads to the explicit expression for the cross-stream particle velocity
\begin{align} \frac {U_x}{\Gamma \beta } &= -\frac {1}{4\pi }\int _{S_{\!p}}(\boldsymbol{u}^s_{11}\boldsymbol{\cdot }\hat {\boldsymbol{x}})\text{d}S =\ldots \nonumber \\ \ldots &= { \frac {\textit{Du}}{(1+2\textit{Du})^2}\left [\frac {|\zeta _0|}{4}(\textit{Du}-\alpha D(1+\textit{Du})) - \ln \left (\cosh \left (\frac {\zeta _0}{4}\right )\right ) (1+\textit{Du}(1-\alpha D))\right ]}, \end{align}
where two distinct contributions can be identified: the first term represents a purely electrophoretic effect arising from the induced electric field along the
$x$
-direction, whereas the second stems from diffusiophoresis driven by the asymmetric ionic concentration gradients. Figures 2(a) and 2(b) illustrate these mechanisms for a binary electrolyte with equal diffusivities (
$\alpha =0$
). The value of
$\Gamma$
is artificially high to clearly visualise the underlying physical mechanisms.
(a) Electrophoretic velocity,
$\boldsymbol {U}_{\!{ep}}$
, resulting from the combination of the applied electric field and the field induced by CP (as perturbed by the shear flow),
$\boldsymbol {E}=-\beta (\boldsymbol{\nabla }\phi _{01}+\Gamma \boldsymbol{\nabla }\phi _{11})$
. (b) Diffusiophoretic velocity,
$\boldsymbol {U}_{{dp}}$
, arising from CP
$\delta c=\beta (c_{01}+\Gamma c_{11})$
. (c) Dimensionless cross-stream migration velocity as a function of the Dukhin number for an electrolyte with equal diffusivities (
$\alpha =0$
) and three representative values of
$\zeta _0$
.

Figure 2(c) shows
$U_x$
as a function of Dukhin number for the case with equal diffusivities and for three representative values of the dimensionless zeta potential. Positive values of
$U_x$
indicate cross-stream migration toward regions with a higher fluid velocity along the direction of the applied electric field. In microchannel experiments, this implies that particles migrate toward the channel centre when the electric field is aligned with the fluid flow. Remarkably,
$U_x$
reverses its sign as the Dukhin number increases.
Figure 3(a) shows
$U_x$
as a function of the Dukhin number for several binary electrolytes commonly used in experiments, with
$\zeta _0=-3$
. Remarkably, for the electrolyte with the largest diffusivity contrast (HCl), the electrophoretic contribution dominates over the entire range of
$Du$
. Figure 3(b) shows the cross-stream migration velocity (in
${\unicode{x03BC}} \mathrm{m\,s}^{-1}$
) as a function of the particle radius for three typical experimental conductivities:
$\sigma = 0.1$
,
$1$
and
$10\ \mathrm{mS\,m}^{-1}$
. The physical parameters are chosen to match the Newtonian fluid experiments by Li & Xuan (Reference Li and Xuan2018), namely
$E_0 = 30\ \mathrm{kV\,m}^{-1}$
,
$\dot {\gamma } = 55.6\ \mathrm{s^{-1}}$
,
$D_0 = 1.6 \times 10^{-9}\ \mathrm{m^2\,s}^{-1}$
and
$\alpha = 1.26 \times 10^{8}\ \mathrm{s\,m}^{-2}$
(corresponding to NaCl in water). Here, the Dukhin number is estimated as
${\textit{Du}} = K_s / (a\sigma )$
, where
$K_s$
denotes the surface conductance, typically of the order of
$1\ \mathrm{nS}$
for colloids (Ermolina & Morgan Reference Ermolina and Morgan2005), and a representative zeta potential of
$-50\ \mathrm{mV}$
is assumed. For comparison, we have also plotted the prediction by Khair & Kabarowski (Reference Khair and Kabarowski2020) for the inertial electrophoretic lift. For particles with a radius of around
$1\ {\unicode{x03BC}} \mathrm{m}$
, this inertial effect remains much smaller than the velocity induced by CP.
(a) Dimensionless cross-stream migration velocity versus the Dukhin number for several binary electrolytes commonly used in experiments at
$\zeta _0=-3$
. (b) Cross-stream migration velocity as a function of particle radius for three electrolyte conductivities:
$\sigma = 0.1$
,
$1$
and
$10\ \mathrm{mS\,m}^{-1}$
. The remaining physical parameters are
$\zeta = -50\ \mathrm{mV}$
,
$D_0 = 1.6 \times 10^{-9}\ \mathrm{m^2\,s}^{-1}$
,
$\alpha = 1.26 \times 10^{8}\ \mathrm{s\,m}^{-2}$
,
$E_0 = 30\ \mathrm{kV\,m}^{-1}$
,
$\dot {\gamma } = 55.6\ \mathrm{s^{-1}}$
and
$K_s = 1\ \mathrm{nS}$
. The theoretical prediction for the inertial electrophoretic lift by Khair & Kabarowski (Reference Khair and Kabarowski2020) is also plotted for comparison.

Figure 3. Long description
Panel A: A line graph shows the dimensionless cross-stream migration velocity as a function of the Dukhin number for several binary electrolytes. The x-axis represents the Dukhin number on a logarithmic scale, and the y-axis represents the dimensionless cross-stream migration velocity. Different colored lines represent different electrolytes: KCl, NaCl, KOH, and HCl. The graph includes a legend indicating the diffusivities and alpha values for each electrolyte. The lines show varying trends, with some increasing and others decreasing as the Dukhin number increases. Panel B: Another line graph illustrates the cross-stream migration velocity as a function of particle radius for three different electrolyte conductivities. The x-axis represents the particle radius in micrometers on a logarithmic scale, and the y-axis represents the absolute value of the cross-stream migration velocity in micrometers per second on a logarithmic scale. Different colored lines represent different electrolyte conductivities: 0.1 mS/m, 1 mS/m, and 10 mS/m. The graph includes a legend and annotations indicating regions where the velocity is positive or negative. A dashed line represents the theoretical prediction for inertial electrophoretic lift by Khair & Kabarowski.
6. Conclusions
We have employed the macroscale model derived by Schnitzer and Yariv for thin EDLs to investigate the effect of an imposed shear flow on the CP around a spherical particle. Within this framework, we have derived an analytical expression (5.2) for the cross-stream particle velocity in the limit of weak electric fields and small shear rates, which – together with the thin-EDL assumption – constitute the core approximations of our theoretical analysis. We have shown that, as a consequence of the combined action of electric and shear flow fields, the particle undergoes electrophoretic migration perpendicular to both driving fields.
We have considered a binary electrolyte with unequal ionic diffusivities, which give rise to induced charges within the diffusion layer of surface-conducting particles. Although these charges significantly influence the electrophoretic mobility, they cannot break the lateral symmetry around the sphere in the absence of flow; thus, no cross-stream motion occurs regardless of the diffusivity contrast. Imposing a shear flow changes this completely: it distorts the ionic CP cloud and breaks symmetry – even for equal diffusivities (figure 1b ). Consequently, shear flow is essential to trigger lateral migration, while its magnitude is strongly governed by the difference in ionic diffusivities.
The model predicts velocities of the order of
${\unicode{x03BC}} \mathrm{m\,s}^{-1}$
for particles with radii around
$1 \ {\unicode{x03BC}} \mathrm{m}$
, which aligns well with experimental observations in microchannels. In these experiments, particles migrate across the channel cross-section over time scales of a few seconds, yielding an estimated cross-stream velocity in the range of a few micrometres per second or below. We emphasise that, at present, only order-of-magnitude estimates are possible because existing experimental studies using DC electric fields do not directly measure lateral velocity. Nevertheless, it is worth mentioning that Vishwanathan & Juarez (Reference Vishwanathan and Juarez2023) reported direct measurements of cross-stream velocity in the range of
$1{-}3\,{\unicode{x03BC}} \mathrm{m\,s}^{-1}$
, albeit under AC electric fields. Remarkably, the theory also predicts a reversal in the sign of the cross-stream migration velocity with increasing Dukhin number (
${\textit{Du}}$
). Specifically, in microchannel experiments where the electric field and fluid flow are aligned, particles migrate toward the walls at low
${\textit{Du}}$
, whereas migration occurs toward the centre at higher values. This behaviour is qualitatively consistent with the experimental observations reported by Abdorahimzadeh et al. (Reference Abdorahimzadeh, Bölükkaya, Vainio, Liimatainen and Elbuken2024), who observed this reversal in migration direction upon increasing the electrolyte conductivity.
Future work will focus on systematic experiments for a rigorous quantitative comparison with the theory. In this context, accounting for wall effects in microchannel geometries will be essential; notably, wall repulsion induced by CP electroosmosis (Fernández-Mateo et al. Reference Fernández-Mateo, Calero, Morgan, García-Sánchez and Ramos2022) may play a significant role at high electric-field strengths. In addition, future studies should explore non-spherical particle shapes – which can strongly influence lateral migration – as well as nanocolloids, where the thin EDL approximation no longer holds.
Funding
The authors acknowledge the financial support from MICIU/AEI/10.13039/501100011033/FEDER, UE (Grant No. PID2022-138890NB-I00). A.R.G. acknowledges support from a predoctoral contract funded by Junta de Andalucía, Spain (Grant No. DGP_PRED_2024_01162). R.F.M. acknowledges funding from the European Union’s Horizon Europe research and innovation programme under the Marie Sklodowska-Curie (Grant No. 101149570).
Declaration of interests
The authors report no conflict of interest.


δc>0
δc<0
Uep
E=−β(∇ϕ01+Γ∇ϕ11)
Udp
δc=β(c01+Γc11)
α=0
ζ0
ζ0=−3
σ=0.1
1
10 mSm−1
ζ=−50 mV
D0=1.6×10−9 m2s−1
α=1.26×108 sm−2
E0=30 kVm−1
γ˙=55.6 s−1
Ks=1 nS