1. Introduction
Suspended bubbles or liquid droplets deform in fluid flows and in doing so demonstrate a host of phenomena with high industrial importance. For instance, in petroleum industry, there is a major need to accurately drive and control the demulsification process of crude oil [
1,
2]. In doing so, conventional experimental techniques, such as heat treatment, electrical field, and membrane separation, require complex and expensive setups to enable significant insight into these complex multi-physics problems [
3]. In terms of physical modelling, the simulations of the dynamics of bubble rising including deformation and possible merging or break-down, require a correct treatment of the sharp liquid-gas interfaces with a fine modeling of the surface tension that can lead to large deformations of the interfaces. In this article, we focus on the numerical study of a single bubble deformation under different flow conditions. Since the numerical simulation of two-phase flows is inherently a multi-scale problem that needs sophisticated strategies for time and space integration schemes, both small and large scale deformations should be treated simultaneously. Moreover, in a two phase system of leaky dielectric fluids inclusion of the temperature response to electric and hydrodynamic response of the system requires special treatment. The application of an external electric field to a droplet can result in large topology and velocity changes with possible break-down and coalescence. Understanding of the underlying principles of Electrodynamics (EHD) can be applied to better control and predict the motion and deformation of droplets.
From a fundamental point of view, most of the simplest multi-physics models cannot be theoretically solved in their closed form, hence the interest in numerical solution arises [
4,
5]. The classical methods such as Finite Difference [
6], Finite Element [
7], Finite Volume [
8], Level Set Method [
9], and combined methods [
10] cover the majority of the mesh-based numerical strategies in which the accuracy of the results is highly dependent on the numerical aspects (i.e., numerical methods, time step size and mesh refinement) [
11]. Numerical methods can be classified with regards to their modeling approach. In the Eulerian multi-fluid approach, each phase is considered as an interpenetrating continua from which an ensemble averaging of the multi-phase Navier–Stokes equations is calculated [
12]. On the other hand, the Lagrangian mesh-free methods notably Smoothed Particle Hydrodynamics (SPH) [
13] offers a promising and flexible framework in modeling complex coupled multi-phase fluid problems. As listed in reference [
14], among several mesh-free methods, SPH inherently provide notable efficiency in calculating partial derivatives [
15] by considering particles which remove the necessity for mesh generation and refinement.
From physical point of view, thermocapillary instability (TC) is caused by inhomogenities in interfacial tension in multi-phase systems. This in-homogeneity is a result of a thermal gradient at the interface introduced by surfactants or temperature variations. Here, we consider the variation of temperature on the surface of the micro-droplet. Temperature variation creates a non-uniform surface tension, which results in interruption in the balance of forces and the introduction of a new shear stress on the surface of the droplet. The imposed strains by the continuous phase alter the structure of the particles of the disperse phase. In particular, coupling the temperature gradient with an electric field leads to a bubble destabilization and deformation. The electrostatic pressure enhances the instability since the electrostatic force on the droplet surface is higher than the capillary pressure. On the other hand, the capillary pressure affects the fluctuations of the free surface, which lead to diminishing instabilities. The instability grows when the electrostatic pressure is larger than the capillary pressure. As a result, the bubble starts to deform or migrate.
There are few experimental and theoretical studies available in the literature of EHD-TC coupled problem. In principle, a droplet in such system evolves in order to reduce the total free energy of the system. The total energy is defined as the sum of internal and the kinetic energies. At steady state, the final shape of the droplet is reached at the lowest interfacial energy level. The linear stability analysis shows a negative correlation between the temperature and the interfacial tension. Regarding the one-dimension thin liquid films, the EHD-TC forces lead to the creation of smaller structures (eddies) [
16,
17]. Nevertheless, some inconsistencies between the experimental and theoritical approaches are reported because of the electric breakdown effects, when a sufficiently high voltage is applied [
18]. Therefore, the current paper concerns the study of complex flow physics including thermocapillary phenomena (Marangoni forces) and electrohydrodynamics by means of SPH simulation. The current work is an extension of our previous numerical study in which an electric field is coupled [
19].
This article is organised as follows; the governing equations of a multi-phase system with thermal gradient and electric field are first presented, before introducing the SPH method and the associated space and time discretization schemes. Afterwards, numerical convergence studies are presented. Then we discuss the surface tension, the electrohydrodynamics and the thermo-capillary effects, separately. Finally, the results for electrohydrodynamics-thermo-capillary bubble deformations are presented.
4. Results and Discussion
This section presents the results of the SPH model implemented in the 2D studies. First, in order to verify the SPH model in the pressure prediction, a Young-Laplace problem is solved with SPH model in a 2D simulation domain. Second, a linear thermal profile is imposed on a 2D simulation domain to verify the SPH model against analytical solution of the Marangoni force in the static case followed by a dynamic case to validate the 2D thermoacapillary bubble rising and comparison of the SPH results with direct numerical simulation results. Third, the effects of EHD on a single droplet immersed in continues phase are calculated with SPH model and compared with analytical results. This includes the flow orientation inside and outside of the droplet, the bubble deformation and the velocity compared with analytical results. In the last section, the SPH model for two-phase flow subject to coupled EHD and thermocapillary forces is presented and the evolution of a 2D droplet is predicted for multiple fluid properties.
Validation of the interfacial forces begins with the investigation of a static pressure jump. Initially, a quiescent system with a velocity field equal to zero is assumed. Since all time derivatives are zero, the mass is conserved. Young-Laplace law relates the droplet curvature and the pressure gradient at the interface. Based on this law, the pressure gradient at the interface of two phases would be equal to the product of the mean curvature of the interface and the surface tension such as
where
and
are the radii of the curvature of a curved surface. Note that in case of a circle
resulting in
. The pressure jump at phase boundary follows the Young-Laplace equation, which describes the relationship between the pressure, the surface tension and the radius of the droplet. The schematic of the pressure inside and outside of the bubble are shown in
Figure 2-left. To investigate the accuracy of the numerical results compared to analytical results when droplet radius
R are taken 0.25 [m], 0.3125 [m], 0.375 [m] and 0.625 [m]. The
ratio is set to 8 in these simulations so that the same confinement effect will be applied for all. It is shown in
Figure 2-right that as expected, a linear relationship between
and
is observed. The slope of each straight ling indicates the surface tension and are equal to
and
. This indicates that the simulation results obtained from SPH multiphase model confirm well with Young-Laplace law. According to Equation (
26), surface tension tends to minimize the surface, whereas the pressure difference tends to increase the surface curvature. When considering free-surface flows and based on the geometry, the fluid-fluid interface is flat while in the problems stated here, one phase is fully surrounded by the other and is under full tension from all directions, leading to droplet circular shape (when no external forces are applied).
To study the effect of particle resolution, the simulation setup is designed with the domain size of 4 [cm], sufficiently low confinement effects with
and a surface tension of
[N/m]. The following relative error norms are defined.
Table 1 shows that when the particle resolutions increase, both
and
norms decrease. We can conclude that the pressure gradient inside the bubble converges to the analytical solution
[Pa].
Next, we validate the Marangoni force separately and investigate convergence of the numerical method. First, the static capillary stress tangential to the interface under thermocapillary effect at three grid resolutions is studied. A linear thermal profile is imposed on a two-layer square (5.76 [mm] × 5.76 [mm]) domain where droplet is characterised by
[kg/m
3],
[m
2/s] and the background fluid by
[kg/m
3],
[m
2/s] for density and thermal conductivity, respectively. The surface tension evolves based on the Equation (
28) showing a linear relationship between the surface tension and the temperature,
where
and
are the reference values of the surface tension and the temperature, respectively. The negative surface tension coefficient
[N/mK] implies the decrease of the surface tension
with respect to the temperature. The linear thermal gradient 200 [K/m] is imposed from bottom wall
towards the upper wall
. According to the dependence of the surface tension to the temperature with
[N/mK], the Marangoni force acts vertically on the interface. Note that the lateral walls are adiabatic while the top and the bottom walls are subject to
K and
[K].
Figure 3 shows the profile of interfacial Marangoni force along a horizontal line at the center of the simulation domain, at three different particle spacing. The values form SPH model are the normal component of the Marangoni force perpendicular to the fluid-fluid interface which are calculated based on the Continuum Surface Force (CSF) method and as a consequence are volumetric force calculated per particle volume. Lower particle spacing correspond to sharper interface. If an infinite resolution was possible numerically, the Marangoni force profile would tend to Dirac function where its magnitude is equal to Marangoni force. From
Figure 3 one can also observe that the magnitude of the Marangoni force increases with particle resolution augmentation. Since the
[N/mK], the interfacial Marangoni force direction is downwards. To compare the magnitude numerical results with exact solution (
[N/m
2] ). For the numerical case, magnitude of the Marangoni force predicted by SPH method is computed by integrating the Marangoni force part of the surface tension (not the CSF part). The comparative table of the results in shown in
Table 2. The gravity and the heat dissipation are neglected, therefore the only acting force is the Marangoni force for which the sampled profile along the horizontal line is depicted and one can observe that the higher the particle spacing, the wider the range of volumetric Marangoni force at the interface. These results are in agreement with results reported in [
19,
40].
In thermocapillary droplet motion, having that surface tension depends on temperature, assuming hot wall temperature
and cold wall temperature
on parallel boundaries (
>
) leads to the introduction of a surface tension gradient along the interface. Thermocapillarity consists of applying a temperature gradient along an interface to induce a surface tension gradient. If
and
denote the temperature and the surface gradient operator, respectively, the thermocapillary tangential stress writes as
The surface tension gradients (i.e., Marangoni effect) can be used to control the dynamics of the bubble. To this end, a square box (5.76 [mm] × 5.76 [mm]) is discretized using 32 particles in each direction. The droplet is initially placed at the center of the domain and has a radius
[mm]. The velocity boundary conditions are set to be free slip at the lateral walls, and no-slip at the top and bottom walls. Neumann Pressure boundary conditions are used on all walls except for the left wall, where a Dirichlet Pressure boundary condition is used due to bootstrap condition of the Pressure Poisson Equation. The temperature is fixed at 290 [K] at the bottom wall and linearly increases to 291.15 [K] at the top wall. Assuming that both droplet and the ambient fluid are initially at the stationary state with
[kg/m
3] and
[Pa·s] for the droplet and
[kg/m
3] and
[Pa·s]) for the background fluid, we consider that the heat conductivity of the droplet (1.2 × 10
−6 [W/mK]) is half of the background fluid. With constant surface tension
[N/m] and the rate of the change of the surface tension with temperature
[N/mK] in Equation (
28),
Figure 4 shows the time evolution of the droplet migration velocity subject to Marangoni force compared to results obtained by Ma and Bothe [
41]. The dimensionless velocity
where the characteristic velocity
and the dimensionless time
.
Marangoni stress that is the tangential component of the surface tension gradient acts in opposition of the surface motion and hence results in less flexibility of the interface and droplet mobility restriction if no additional force is applied. As time passes, the time-evolution of the non-dimensional droplet velocity which, and after some oscillations, meets the velocity associated direct numerical simulation Ma and Bothe [
41], hence the initial unsteady leading to a steady droplet motion.
Hereafter, the EHD solver is validated by setting up a similar test to first part of the
Section 4. The direction of these streamlines is determined as the mutual relationship between the electrical conductivity and electrical permitivity ratios of the phases. They are defined as
and
for the electrical permitivity and electrical conductivity ratios, respectively. Note that the subscript
d and
b refer to the droplet and bulk fluid properties.
The recirculation zones of the fluid inside and outside of the droplet are theoretically predicted by Taylor et al. [
42] as depicted in
Figure 5 with Pole-to-Equator and Equator-to-Pole flow directions. A specific numerical simulation for the case
with
and
for
from
Table 3 are compared with Taylor’s results in
Figure 6.
A qualitative agreement of the flow orientation inside and outside of the droplet is found between the theoretical prediction and the SPH capability in correctly capturing the direction of the recirculation zones. For
, the streamlines start from the equator towards the pole, while
situation, the opposite direction is observed.
Figure 7 depicts the velocity profile on the right-half and the pressure distribution on the left-half. Note that the recirculation zones of velocity streamlines inside (in blue) and outside (in red) of the droplet are clearly visible.
Investigation of circular droplet deformation given small deformations subject to electric field is presented here using two theories from literature. Taylor [
42] estimates the droplet deformation
as
where
is the discriminating function evaluated as
For the same problem, Feng [
44] suggests the following relation
where
is estimated from
In Equations (
30) and (
32),
R is the initial droplet radius before its deformation and
is the electric field magnitude in the vertical direction deduced from the electric potential difference
, with
h being the height of the domain. Numerically, the droplet deformation parameter
D can be defined based on the droplet’s deviation from the circular shape,
where
A and
B are the elliptic droplet diameters at the steady-state condition, parallel and perpendicular to the direction of the external electric field, respectively. When
, the droplet is at its initial circular shape. On the other hand, more deviation from zero indicates more deformation from its initial shape. Positive and negative values of
refer to deformation in the direction and perpendicular to the electric field direction, respectively. For our study, we consider a circular droplet with
[m] placed at the center of a squared domain of
[m]. The domain contains 240 particles per direction. The droplet properties are
[kg/m
3] and
[Pa·s] while the bulk fluid has identical density and viscosity. All four boundaries are set to no-slip velocity and Neumann pressure boundary conditions except for the top wall where a Dirichlet pressure boundary condition is used. An electrical field is imposed on the system by
[V/m] resulting in unique electric force value directed towards the bottom wall.
Table 3 summarizes different EHD test cases and
Table 4 represents the obtained along with the theoretical values of Feng and Taylor, and the droplet deformed shape at the steady-state. These setups are selected from the simulations proposed by Shadloo et al. [
43] and show good agreement with this study.
Feng [
44] has also proposed an analytical solution for the droplet velocity subject to DC electric field, assuming that the droplet deformation is negligible, i.e., the final shape of the droplet is assumed circular. The velocities inside and outside the droplet can be theoretically calculated as
where
r is the radial position,
and
are the tangential velocity and the radial velocity, respectively. The characteristic velocity
U can be evaluated as
Our numerical results are in agreement with the analytical solutions for both the velocity
and
at which one of the velocity components is maximized as shown in
Figure 8. As can be observed in this figure, theoretical velocity profile for tangential and radial components are shown with dashed-lines and solid lines in the given order. The simulation data for tangential and radial velocity components are respectively depicted with filled circles and unfilled circles. The simulation input parameters correspond to
as shown in
Table 3 with (
[m],
[V/m]). When the droplet deformation is sufficiently large such that the terminal shape can no longer be assumed as circular in two dimension, the conformity of the numerical and analytical results tends to reduce. Based on the Equations (
35) and (
37) the radial velocity needs to be zero at the droplet interface (
). However, because of the small deformation of the droplet (
) and causes small deviation between the numerical and analytical results. Based on the equations of tangential components (
36) and (
38), having (
) leading to
[m/s] and maximum values of
that is in agreement with the observations in
Figure 8.
In this section the simultaneous effects of thermocapillarity and electrohydrodynamics on a single suspended droplet are studied. When a multiphase system is solely subject to electric field, the motion of the dispersed phase is forced by the electric field and damped by the viscous forces. The instabilities caused by EHD-driven flows will occur when the viscous drag force is much smaller than the electric force. Hence, the droplet losses its balance and starts to migrate and/or deform. The electric force is more sensitive to the droplet size than the viscous counterpart, augmenting more instability for larger ratios, where R is the initial droplet radius and L is the size of the domain.
As mentioned before, the Marangoni effect roots into the tangential component of the surface tension gradient which if aligned with the tangential component of the electric force, drives the flow to a more unstable configuration. Subsequently, in the next section we will discuss the scaling parameters that lead to observation of both convective Marangoni effects and electrohydrodynamic effects. To capture electrohydrodynamics driven droplet deformations at the equilibrium state, the electric and the hydrodynamic time scales should match properly based on the geometry of the system namely the droplet radius and the channel width. The EHD time scale can be characterised by Maxwell-Wagner polarization time . It is worth reminding that electric charge accumulation at the fluid-fluid interface happens when each phase has a different charge relaxation time where and are electric permittivity and electric conductivity. This accumulation of the bulk free charges at the phase boundaries will further result in creation of dipoles on the droplet. The electric field acting on these induced free charges, will generate shear stress at the fluid-fluid interface that can be balanced by shear viscous stress and, if thermal gradient is applied, the tangential component of the surface tension gradient. Another aspect to take into account regarding the instability of an EHD-TC multiphase system, is the difference between prolate and oblate droplet deformation. Assuming a vertical potential difference across the domain, and given that weakly conductive droplets embedded in the weakly conductive fluids tend to flip such that the dipole aligns with the direction of the electric field, one can expect that the oblate deformations are more prone to potential instabilities as their dipole is in the opposite direction of the electric field.
The coupled EHD-TC problem setup consists of a square domain of size
[m] with
where
R is the radius of the centralised droplet at
[m] and
[m] with
particle resolution in x and y directions, respectively. An electric potential of
[V] is imposed on the top boundary while other boundaries are set to
[V]. A linear thermal profile is imposed on the top and bottom walls with respective temperatures of
[K] and
[K] while the reference temperature and the initial temperature are also kept at 290 [K] throughout the simulation. The velocity boundary conditions are set to be free slip at the lateral walls, and no slip at the top and bottom walls. Also, pressure boundary conditions are set to be Dirichlet with a constant value at top wall and Neumann for the other three boundaries (
) where
is the normal direction to the given boundary. The density and viscosity of are chosen to be
[kg/m
3],
[Pa·s] for the bubble and
[kg/m
3],
[Pa·s] for the bulk phase. Both phases are set to have stationary conditions at initial time step. The fluid electrical properties of the three cases are given in
Table 5. The time evolution of the droplet subject to thermocapillary flow and EHD forces is illustrated in
Figure 9.
Based on the results shown in
Figure 9, a combination of
and
ratios and the direction of thermal and electric potential gradients affect the deformation and migration of the droplet.Thermocapillary induced motion due to surface tension gradient can be decomposed into two components.The perpendicular temperature gradient component to the fluid layer that generates Benard-Marangoni circulations inside the droplet. The tangential temperature gradient component generate surface tension gradient along the surface of the fluid and induce surface flow towards the regions with higher surface tension. In our simulation, we combine these two components to obtain surface force. Furthermore, when a droplet is suspended in an imposed flow field generated by the EHD forces, which itself depends on the
and
relation as explained in the EHD section; both surface force and the imposed EHD force are responsible for the deformation and migration of the droplet. For the case 1 (top row) and case 2 (middle row), vertical and horizontal electric field are applied, respectively, while the thermal gradient is kept vertical in both cases. All the other parameters are kept the same. In case 1, where the electric field is oriented the same as thermal gradient, in the vertical direction, it is observed that the droplet forms a prolate shape. Because the viscosity of the droplet (
[Pa·s]) is chosen close to continues phase viscosity (
[Pa·s]), similar to those in the thermocapillary induced motion cases, the resistance due to the presence of the droplet is relatively low. However, the non-uniform distribution of the electric charges on the surface of the droplet, generates a shear force (from equator-to-pole since
) which, in addition to the Marangoni stress caused by the variation of surface tension on the droplet surface, deforms the droplet. This deformation modifies the effective viscosity of the droplet compared to its initial state with respect to the continues field. Because the surface tension coefficient is negative
[N/m], the droplet tends to move in the opposite direction of the thermal gradient, that is from top to bottom. But the effective viscosity modification, retards this migration. The top side of the droplet, closer to hot wall, has lower surface tension, and it is as a result more prone to strong deformation caused by both internal EHD-induced circulations and surface-force-induced circulations. In the case 2, where horizontal electric field in applied with higher electric potential set to be at the right side of the setup, our results show a symmetric elongation along the electric field direction while the droplet is moving downwards. Finally, case 3 (bottom row) shows the evolution of the droplet towards a break-up when a vertical electric field is applied taking
. As can be observed, the droplet starts to deform from its center while keeping symmetrical oblate structure thought the break-up process. Comparison between case 3 in coupled EHD-TC cases and case 4 in
Table 4 where both systems are characterised by
, we observe a different orientation for the droplet due to the presence of Marangoni force. It is important to take into account the difference between the scale of effectiveness in EHD phenomena and Marangoni flows due to thermal gradient. The former has a really small time scale and therefor affects the system much faster than the Marangoni flows. This highlights the reason for-which numerical simulation of coupled physics require many trials as time-scale and length scale are not in the same order for each physics involved.