2.4. Charged Particles Suspended in an Evaporating Medium while subject to Nonuniform Electric Fields
In simulations and experiments presented herein, charged particles (colloidal latices with net positive surface charge density) are suspended in a nonuniform electric field which emanates from multiple metasurface apertures (see
Figure 9). When an electric field (uniform or nonuniform) is applied to charged particles in suspension, they migrate along the field lines in a predictable manner such that a relative motion between the charged particles and the suspending medium is observed [
17]. The electrostatic force on the charged particles is given as
. Such charged particles in suspension will polarize the suspending solution surrounding it, giving rise to a counter-charged ion cloud called an electric double layer. Since the induced ion cloud is oppositely charged in comparison to the particle, the overall motion of the fluid (suspension medium) will be in the opposite direction of the charged particle’s.
The opposing suspension motion tends to retard the motion of the particle in suspension as an electric force is applied to it, creating a drag-like force called Electrophoretic Retardation (
). However, charged particles within the electrolyte are still able to move with a constant velocity, called the drift velocity (
). In such an instance, the charged particle-double layer volume can be treated as a single particle, with an effective radius of the moving particle including any molecules of water or other solvent that move with it, called Stoke’s Radius (
). The impact that the electric double layer has on the kinematics of the particle are determined by the layer thickness. The thickness of the electric double layer is represented by the Debye length
, and is a characteristic distance from the charged particle in the solution, to a radial distance from the surface normal of the charged particle in which the electric potential decays to approximately
of the total surface potential [
17]. As a charged particle travels through a solution, there is a plane beyond which the oppositely charged ions do not travel along with the particle of interest: the slipping plane, which is defined by the electrical potential at the plane, and the zeta potential, which dictates the amount of repulsion between the surrounding counter-ion layer and the solution. Interestingly, this repulsion is due to the osmotic pressure created between the ionic concentration difference between the double layer and the solution [
18,
19].
However, when taking the Debye-Hückel condition,
(where
r is the Stoke’s Radius), and there is no pressure gradient within the suspension medium, there will be no flow of the suspension medium due to the electric field as there should be no other free charges present within it [
17]. This means that the polarized electric double layer is considered to be very thin, and thus, the Electrophoretic Drag can be treated as negligible. The Debye-Hückel limiting case was considered in this paper, as the surface charge density of latices is considerably small (as will be seen in
Section 2.7). This means that Stoke’s Radius can be treated as the particles radius. Furthermore, since the electric field that the particles are subjected to is non-uniform in this experiment (shown in
Figure 9,
Figure 10 and
Figure 11), the electrostatic force contribution to particulate motion in the Debye-Hückel limit can be expressed as [
17,
20,
25]:
where
q is the charge of the particle, and
E is the electric field strength.
In a nonuniform electric field, an electrically neutral body in suspension will usually move in a direction in which the electric field gradient is the steepest; a phenomenon which was coined Dielectrophoresis by Pohl in 1951 [
21]. The mechanism governing dielectrophoresis depends on the asymmetrical induction and attraction of charge densities within suspensoids, where electric dipoles are induced due to the charge asymmetry [
21,
22]. In simple dielectrophoresis (of an uncharged particle), the motion of the particle is dependent on the dielectric properties of the suspension medium and the particle.
In 1979, Pohl showed that the an effective dipole moment could be utilized in the formulation of the dielectrophoretic force [
23]. For a perfectly insulating spherical particle of radius
r with absolute permittivity
that is suspended in a medium of absolute permittivity
, the dielectrophoretic force can be shown to be:
where
is the Clausis-Mosotti factor. In Equation (
3), it is seen that the dielectrophoretic force is not explicitly dependent on any electrical charge within the medium or particles, but depends on the gradient of the nonuniform electric field and the dielectric properties of the medium and particles [
20,
21]. Upon further observation of Equation (
3), one sees that particles are attracted to regions of stronger electric field when
, and repelled when
, and in general, is not parallel to the electric field [
22,
24].
When a solution is spread across the metasurface, it will naturally evaporate over time; in fact, this is a feature of this metasurface sensing technique that must be considered since the nature of latex sedimentation is highly dependent on evaporation and the properties of the deposition surface [
9]. This phenomenon is not unique to latices or colloidal particles. For instance, in a NaCl solution (with sub-nanometer sized particles) evaporating on a hydrophilic surface, the majority of the salt crystallization during natural evaporation takes place at the liquid-air interface. This results in a ringlike crystal "coffee stain" effect, which is attributed to capillary flow from the center to the edges of the water droplet due to loss of the solvent and "pinning" of the water droplet to imperfections on the substrate surface. However, on a hydrophobic surface, the re-crystallization takes place within the bulk of the water droplet at the liquid-solid interface [
6].
For hydrophobic colloidal particles (such as latices), it has been observed that they will preferentially adsorb onto hydrophobic regions, and in regions of opposite charge. However, it is known that latex films do not dry uniformly. Instead, due to the boundary conditions at a droplets edge, latex particles are laterally transported from the fluid centre to the edge of the droplet where they will be consolidated. This means that, in the case of no external forces but that of evaporation, a high concentration of latices should be observed along the perimeter of a water droplet [
9].
In an ambient environment (
Celsius, and some air flow above the surface), it has been shown that the rate of evaporation of water can be approximated as within
[
27]. In order to test the evaporation rate of the solution as it sat on the metasurface, five single drops of the colloidal solution used in this study were placed onto the metasurface and the time to evaporation measured. The ambient temperature was
Celsius, and the 12V computer fan was turned on within the containment box. The fan was not directly pointing at the water droplets, but only allowed air to circulate within the containment box. It was found that, on average, it took approximately fifteen minutes for the water droplets to evaporate. Each of the droplets was measured to be approximately 3
in radius (radius parallel to the metasurface), with a height of approximately
. Modeling the droplet as half an oblate spheroid [
28], the rate of evaporation for the water in our controlled environment was determined using the following equation:
where
is the equatorial radius (radius of the sphere in the plane parallel to and on the metasurface),
h is the polar radius (the height of the oblate spheroid) [
28],
is the density of water, and
is the approximate average time it took for a droplet to evaporate. Given that
,
, and
s it was found that
.
Therefore, assuming that the evaporation rate of the water remains relatively constant, the change in volume of the water as a function of time can be described by the following equation:
It can be shown that this separable differential equation results in an equation for the volume of the water on a surface as a function of time,
, where
is the initial mass of the water on the surface,
is the initial volume and
is the evaporation rate. Given that the estimated total time it takes to evaporate the water will be
. Solving Equation (
5) produces the following equation:
where A is a normalization constant. Solving for
A while considering that the volume must approach zero at
, one finds
. Keeping the experimentally measured evaporation time and geometry of the droplet of water in mind, the resulting equation is:
A graph of the volume of the water on the metasurface as a function of time is given in
Figure 12. In
Figure 12, it is clear that the change in volume as a function of time is nonlinear, and therefore, the change in the radius and height of the water droplet should be nonlinear as well. Assuming that the radius of the water spot (approximated as a hemisphere) and its relative height from the surface should both reach zero at
,
, such that in the event that
and
, the radius should decrease at a rate that is two times faster than the height of the droplet at a constant evaporation rate.
Equation (
7) can be re-expressed in terms of the height of the water spot
and the radius of the water spot
. Then differentiating each with respect to time, the rate at which the height and radius of the droplet can be determined. The graphs of
and
are given in
Figure 13(a,b). This phenomenon subjects the particles to another type of force which accelerates the sedimentation process, thus altering the equation of motion [
29,
30,
31]. The exact rate of change for the radius (
) and height (
) of the water spot are given in
Figure 13c,d, respectively.
During conventional procedures of latex film deposition, it has been shown that evaporation is the driving force behind particle sedimentation. In such film deposition procedures, latex deposition is driven by the directed motion of particular influxing to evaporative regions via the convective mass transfer of water. As was previously described, the dominating sedimentation process takes place at the radial boundary of the water spot on top of the metasurface (due to convective mass transfer), directed in a downward direction at the edge due to the curvature of the water droplet. Since the total evaporation flux of the water must be equal to the bulk water flux to the boundary, it is suggested that the particle velocity due to the bulk water flux,
, can be described as [
29,
30,
31]:
where
is the radial velocity due to evaporation as a function of time, depicted in
Figure 13(c),
is the total surface area of the water spot (half of an oblate spheroid), and
is the surface area of the radial boundary at which a two-dimensional lattice of particles has settled (estimated as the surface area of a cylinder whose height is the particle diameter), and
is particle radius [
29,
30,
31]. The surface area of an oblate spheroid is defined as [
28]:
where
is the equatorial radius (radius of the sphere in the plane parallel to and on the metasurface),
is the polar radius (the height of the oblate spheroid), and
. Solving Equation (
8), one will find that:
It is suggested here that, since the latex particles within the medium are subject to the convective mass transfer of water due to evaporation, using Stoke’s law [
32], the downward force contribution that the evaporative process contributes to particle motion within the solution can be described by:
where
is the particle radius,
is the fluid viscosity,
is the particle velocity due to fluid flux,
g is the acceleration due to gravity,
is the particle density, and
is the fluid density. Furthermore, the contribution from frictional drag due to Stoke’s Law will retard the motion of the particles in directions which are not parallel to the convective mass transfer vectors. This means that, since the majority of the latice deposition takes place at the evaporative front, the force vector due to evaporation (
) contributes to the downward motion, whereas motion parallel to the metasurface is retarded in a manner predicted by Stoke’s Law. The retarding force due to frictional drag, whose vector components are parallel to the metasurface, are given by:
Finally, the net force on a charged particle in suspension subject to an nonuniform electric field during evaporation can be expressed as:
where downward acceleration due to gravity is negligible within the fluid. In the limit that the electric field goes to zero, evaporation will be the only external driving force which causes particle deposition onto the surface.
Due to the convective mass flow of the water toward the edges of a water droplet, it should be observed experimentally that the particles should aggregate in clumps near the edge, where a random, smaller distribution of particles is observed over the wider area [
9] without the presence of an externally applied electric field. Conversely, in the presence of an electric field, it should be that the latices are not so highly concentrated along the boundary of a water droplet, but instead, their bulk should become increasingly spread out over a larger surface area and concentrated near metasurface apertures in a manner proportional to the electric field strength they are subjected to.