Analysis of reliability index $\mathfrak{R} = P(Y < X)$ for newly extended xgamma progressively first-failure censored samples with applications

Nomenclature

1.   Introduction

For the past few years, there have been some noteworthy advancements in the field of fluid mechanics that are focused on structures inside fluids. The classical theory has been demonstrated to be insufficient for describing their behaviour. The earliest theory to take structured fluids into account is the theory of micropolar fluids, given by Eringen ^[1]. The mathematical representation of micropolar fluid allows us to discuss several physical phenomena resulting from the micro-motions and local structure of the particles. It provides a more accurate description of the behaviour of various real fluids, such as animal blood, liquid crystals, polymeric suspensions, and muddy fluids, than the classical representation of Navier-Stokes, particularly whenever the typical flow dimensions, such as the pipe diameter, shrink to a small size. It aligns closely with our assumptions that the greater the effect of the fluid's internal structure, the smaller the typical dimensions of the flow. There have been numerous studies on micropolar fluid flow in applications related to engineering ^[2,3,4] and industry ^[5,6,7].

At low Reynolds numbers, in cell/cavity models, the movement of a viscous/micropolar incompressible fluid on rigid particles or fluid droplets of different shapes is a topic of interest for researchers in biomedical, chemical, and environmental engineering and science. In many real-life situations, the area where fluids flow over groups of particles is important. This is true for sedimentation, fluidisation, the rheology of suspensions, the movement of blood cells found in veins or arteries, centrifugation, and micro-fluidics. As a result, it is crucial to ascertain whether the existence of nearby boundaries or particles affects the movement of a specific droplet or particle. The unit cavity/cell model is a notable and effective method that has been used to predict how the concentration of particles will affect the rate at which particles sediment ^[8].

The representation of the cell/cavity model includes the idea that a randomly assembled collection of droplets/particles may be separated into an identical number of cells/cavities, each containing a single droplet/particle that is typically spherical or elliptical. The fluid cell's volume is selected to ensure that the assemblage's solid volume fraction aligns with the cell's solid volume fraction. Therefore, each particle (droplet) causes the entire disruption by being restricted inside the fluid's cell it is linked to. The boundary value problem is simplified by considering only one droplet/particle and its surrounding envelope. The representation of the unit cell is commonly employed to analyse and address the boundary value problem in solid/fluid particles that are moving within concentrated cells/cavities, disregarding the influence of the container cell (cavity), such as ^[9,10,11].

The Stokes flow issue, which involves an incompressible fluid with a different viscosity surrounding a fluid sphere, has received a lot of attention in analytical and numerical discussions. This model is widely used in modern engineering applications. Hadamard ^[12] and Rybczynski ^[13] independently expanded the Stokes issue to study the translational movement of a fluid sphere droplet in another non-miscible fluid. They calculated the drag force that the surrounding fluid would exert on the fluid sphere by assuming that the shearing tension and tangential velocity at the interface between the two fluid phases are continuous. In real Stokes flow scenarios, droplets or particles are typically not in isolation and are surrounded by a fluid that is confined by solid cavities (walls). It is crucial to examine if the existence of nearby boundaries has a substantial impact on the movement of the droplet/particle. Using bipolar spherical coordinate systems, Bart ^[14] studied the movement of a spherical fluid droplet as it settled perpendicular to a planar interface, seperating between two immiscible newtonian fluid phases. Meanwhile, Salem et al. ^[15] studied the thermocapillary Stokes movement of a fluid sphere droplet in the presence of a planar interface. Hetsroni and Haber ^[16] investigated the issus of a solitary fluid sphere droplet immerged in an unlimited Newtonian fluid of varying viscosity. Also, some have studied examined the wall impacts on a spherical fluid droplet flowing along the centreline of a circular tube utilising a reciprocal theorem ^[17] and an approximate technique ^[18]; on the other hand, some studies the interface impacts on a spherical fluid droplet utilising the volume of fluid method ^[19,20,21]. Moreover, Lee et al. ^[22] showed the motion of a fluid droplet inside a non-concentric spherical cavity.

Every result mentioned above concerns viscous fluids. According to micropolar fluids, Ramkissoon ^[23,24] has discussed the Stokesian flow of a non-Newtonian fluid past a Newtonian fluid sphere and spheroid. Niefer and Kaloni ^[25] studied two interconnected issues involving the movement of a Newtonian fluid past a spherical fluid containing a non-Newtonian fluid, and, additionally, the movement of a non-Newtonian fluid past a Newtonian fluid droplet with a boundary condition for non-zero slip/spin. Hayakawa ^[26] examined the issues associated with the slow, axisymmetric Newtonian flow of a non-Newtonian fluid past a stationary sphere and cylinder; they explicitly analysed and determined the normalised drag force for each scenario, other studies, see ^[27,28].

The movement depends strongly on the interfacial area, which is a function of the size and shape of the particle, as well as the overall fluid motion. At the interface between a particle and the ambient fluid, for particle stability, a balance between the normal force, the shear force, and the surface tension force must be maintained. This balance governs the shape of the particle. The size would also be influenced, particularly if there is phase change. Accordingly, the encircling medium and the fluid particle is separated by a well-defined interface. In certain instances, such as a soap bubble, the separating interface can be a thin liquid film. There are many complex instances, consisting of pairs of bubbles and drops in contact, or a fluid particle entirely inside a drop. These systems are referred to as compound drops. The fluid medium surrounding drops and bubbles is one of the following phases ^[29]: $(i)$ drop inside liquid; $(ii)$ gas bubble inside liquid; $(iii)$ soap bubble (gas inside gas); $(iv)$ compound drop-two interfaces (liquid or gas inside liquid inside liquid or gas); and $(v)$ compound drop-three interfaces (at least two of the phases are liquid).

The aim of this study is to investigate the issue of a compound drop's mobility when two interfaces separating three immiscible liquid regions are present; the micropolar fluid is also one of the three fluid phases. The movement of a spherical viscous droplet in a micropolar fluid with an interface has not been investigated before. Thus, in this paper, we generalise the problem of Salem ^[30] to consider the translational movement of a spherical viscous droplet inside a spherical micropolar/viscous interface with concentric positions. The viscous sphere droplet is either immersed in viscous fluid or in micropolar fluid.

2.   Mathematical equations

The equations describing the incompressible micropolar fluid in steady motion with negligible external forces and couplings, based on Stokes' assumption, are provided by ^[1]:

where $\vec{q}$ refers to the velocity vector; $\vec{\nu}$ refers to the microrotation vector; $p$ refers to the fluid pressure at any point; $\mu$ refers to the dynamic viscosity coefficient; and $(k, \alpha, \beta, \gamma)$ are the micropolar viscosity parameters. These coefficients follow standard inequality rules:

The constitutive equations, respectively, for the stress tensor, $\vec{ \rm{I}}$, and the couple stress tensor, $\vec{ \rm{m}}$, are:

where $\vec{ \rm{I}}$ is the unit dyadic, $\vec{\epsilon}$ is the unit triadic, $\vec{\omega} = {\frac{1}{2}}(\nabla\wedge\vec{q})$ is the vorticity vector, and $(\cdot)^T$ denotes a dyadic transposition. When $k = 0$, the Eqs (1)–(5) reduce to Navier-Stokes' classical model ^[31].

3.   Mathematical formulation

Assume a spherical interface separating two non-mixable fluids; one of them is bounded and the other is semi-unbounded. The fluid outside is a Newtonian fluid, whereas the fluid inside is a non-Newtonian fluid. A viscous sphere droplet of radius $a$ is embedded in a micropolar fluid, at which its centre coincides with the spherical interface centre, and the spherical interface of radius $b(b > a)$. The viscous droplet sphere is moving with a uniform velocity $\vec{U} = U\vec{e}_{ \rm{z}}$; the drop's centre is instantaneously located at the centre of the interface, which is to be at rest; see Figure 1. Geometrically, to describe the viscous sphere droplet and the spherical interface, it is appropriate to define the unit vectors $(\vec{e}_{r}, \vec{e}_{\theta}, \vec{e}_{\phi})$ that correspond to the spherical coordinates $(r, \theta, \phi)$, and consider that the viscous droplet centre serves as the origin of this coordinate system. The gyro-inertial and inertial factors in the field equations may be ignored since it is assumed that the Reynolds numbers for the flow of the micropolar fluid are small enough. Therefore, we take the Stokesian approximation into consideration. The motion is generated by the movement of the viscous droplet in both fluid regions. All dynamical variables in this motion are independent of $\phi$, and it is axially symmetric. Thus, for the three fluid phases, our approach involves utilising spherical coordinates to represent the velocity and microrotation components ^[3,31]:

Let $\psi^{(1)}$, $\psi^{(2)}$, and $\psi^{(3)}$ refer to, respectively, the three stream functions for the three flow areas inside the viscous drop, between the surface of the drop and the micropolar-viscous interface, and outside the micropolar-viscous interface. Therefore, using the conservation of mass equation (1), in terms of stream functions, the velocity components in the three fluid areas may be expressed as

where $\zeta = \cos\theta$. Using the field Eqs (1)–(3) and the formulaes (6)–(8) with the velocity components (9)–(11), it is found that the following systems of equations exist in the three fluid regions:

For the viscous fluid in the domain $(r < a)$:

and for the micropolar fluid in the domain $(a\leq\, r\leq\, b)$:

and for the viscous fluid in the domain $(r > b)$:

where $\mu_{1}$, $\mu_{2}$, and $\mu_{3}$ are the viscosity coefficients for the viscous fluid inside the drop, between the surface of the drop and the micropolar-viscous interface, and outside the micropolar-viscous interface, respectively, and the axisymmetric Stokesian operator is defined by

Now, after removing the formulaes $p^{(1)}$, $p^{(2)}$, $p^{(3)}$, and $\nu_{\phi}^{(2)}$ from Eqs (12)–(18), we find that three differential equations are satisfied by the three stream functions, which are as follows:

Also, we may obtain the component of the microrotation $\nu_{\phi}^{(2)}$ for the micropolar fluid from the following relation:

where $m_{2} = (\mu_{2}+k_{2})/k_{2}$, $\psi^{(2)} = \psi_{1}+\psi_{2}$, $E^{4}\psi_{1} = 0$, and $E^{2}\psi_{2} = \ell_{2}^{2}\psi_{2}$.

Also, we may obtain the vorticity components $\omega_{\phi}^{(1)}(\vec{\omega}^{(1)} = \omega_{\phi}^{(1)}(r, \theta)\vec{e}_{\phi})$ and $\omega_{\phi}^{(3)}(\vec{\omega}^{(3)} = \omega_{\phi}^{(3)}(r, \theta)\vec{e}_{\phi})$, for the viscous fluid phases from the relations

It is also essential to specify the boundary circumstances in order to solve the differential equations (19)–(21).

As stated before, the droplet surface and the micropolar-viscous interface are presumed to be stationary spherical interfaces. This assumption is physically valid since the interface stays spherical due to the surface tension at the interface, which separates two non-miscible fluids, even when subjected to shearing stresses that deform it. In the beginning, at least, the droplet will be approximately spherical if the motion is sufficiently slow ^[31]. Therefore, in this study, we assume that the deformation of the droplet surface and the micropolar-viscous interface are neglected and that the interfaces keep their spherical shapes permanently. Therefore, because there is no mass transfer across the two separating interfaces, the components of the normal velocity on the two sides at the two separating surfaces ought to disappear, and both the tangential stresses and the tangential velocity components are continuous. Since the micropolar fluid phase contains a microstructure, there is also a condition on the microrotation component. Moreover, under these circumstances, the convenient physical one is that the microrotation for the micropolar fluid on the drop's surface and at the micropolar-viscous interface is in proportion to the vorticity for the viscous fluid ^[25]. Here, the proportionality coefficient, $s$, could be known as the spin parameter. The range of this parameter, which is zero to one, is presumed to depend only on the nature of the fluids on both sides of the interface. First value: When the micro-elements near a stiff boundary are incapable of rotating, the situation is represented by $s = 0$ (no spin). Second value: When the microrotation of the micro-elements equals the vorticity of the viscous fluid at the boundary, the situation is represented by $s = 1$. Moreover, for away from the external interface, the velocity and microrotation components must vanish, and at the centre of the internal interface sphere, the velocity components must exist.

The physical boundary conditions mentioned above have the following mathematical formulation:

where $s_{1}$ and $s_{3}$ are the spin parameters inside the viscous drop and outside the micropolar-viscous interface, respectively. $t_{r\theta}^{(1)}$, $t_{r\theta}^{(2)}$, and $t_{r\theta}^{(3)}$ are the shear stresses for the flow inside the droplet, between the surface of the drop and the micropolar-viscous interface, and outside the micropolar-viscous interface, respectively.

The solutions of Eqs (19)–(21) suitable for satisfying boundary conditions (25)–(35) for the stream functions are respectively presented by:

where $I_{\frac{3}{2}}(\cdot)$ and $K_{\frac{3}{2}}(\cdot)$ are respectively the first and second kind for modified Bessel functions of order ${\frac{3}{2}}$, and $A_{1}$, $B_{1}$, $A_{2}$, $B_{2}$, $C_{2}$, $D_{2}$, $E_{2}$, $F_{2}$, $A_{3}$, and $B_{3}$ are unknown constants.

To satisfy the boundary conditions (28) and (33), the following formulaes, in spherical coordinates, for the shear stresses $t_{r\theta}^{(1)}$, $t_{r\theta}^{(2)}$, and $t_{r\theta}^{(3)}$ are given by:

Therefore, the formulaes for the velocity components, the shear stresses, the vorticity components, and the microrotation component in the three fluid regions are given by

Inserting formulations (42)–(53) into conditions (25)–(29) and (31)–(34), we can derive a finite set of ten linear equations for figuring out the unknown constants $A_{1}$, $B_{1}$, $A_{2}$, $B_{2}$, $C_{2}$, $D_{2}$, $E_{2}$, $F_{2}$, $A_{3}$, and $B_{3}$:

where $\lambda_{12} = 2\mu_{12}/(2+k_{2}/\mu_{2})$ and $\lambda_{32} = 2\mu_{32}/(2+k_{2}/\mu_{2})$ with $\mu_{12} = \mu_{1}/\mu_{2}$ and $\mu_{32} = \mu_{3}/\mu_{2}$. Here, $\mu_{12}$ represents the ratio of dynamic viscosity coefficients between the outer and inner fluids to the droplet, and $\mu_{32}$ represents the ratio of dynamic viscosity coefficients between the inner and outer fluids to the micropolar-viscous interface. As $\mu_{12}\to\infty$, the droplet becomes a solid sphere, whereas as $\mu_{12}\to\, 0$, the droplet becomes a gas bubble; on the other hand, as $\mu_{32}\to\infty$, the micropolar-viscous interface becomes a cavity wall (solid wall), whereas as $\mu_{32}\to\, 0$, the fluid outside the micropolar-viscous interface becomes a gas (air), see Figure 2.

The normalised hydrodynamic drag force $F_{z}$ made by the micropolar fluid on the viscous droplet's surface in the presence of the micropolar-viscous interface is shown to be ^[23,32]

Here, the expression (64) demonstrates that the normalised hydrodynamic drag force applied to the viscous sphere droplet relies solely on the coefficient $D_{2}$, which can be obtained by solving the system of ten Eqs (54)–(63) using the Gaussian elimination method. To provide some comparison, the normalised hydrodynamic drag force $F_{z\infty}$ made by an infinite micropolar fluid on the viscous droplet's surface is found to be ^[30]

The micropolar-viscous interface correction factor $K$, with the aid of Eqs (64) and (65), is defined as

4.   The case for the effect of a viscous-micropolar interface on a viscous sphere droplet

Here, in this segment, we suppose the opposite scenario (see Figure 3), that is, a viscous sphere droplet is submerged in a viscous fluid of viscosity $\hat{\mu}_{2}$. Let $\hat{\mu}_{1}$ and $\hat{\mu}_{3}$ represent the viscosity coefficients of the viscous inside the drop and the micropolar outside the viscous-micropolar interface, respectively. Therefore, the stream functions of the fluids in the three regions satisfy the differential equations, as follows:

The following are the general solutions to Eqs (67)–(69):

where $\hat{A}_{1}$, $\hat{B}_{1}$, $\hat{A}_{2}$, $\hat{B}_{2}$, $\hat{C}_{2}$, $\hat{D}_{2}$, $\hat{A}_{3}$, $\hat{B}_{3}$, and $\hat{C}_{3}$ are unknown constants.

In this case, the boundary conditions roughly take the same form as the boundary conditions (25)–(35), as follows:

where $s_{2}$ is the spin parameter for the viscous fluid outside the droplet's surface and inside the viscous-micropolar interface.

Therefore, the formulaes for the velocity components, the shear stresses, the vorticity component, and the microrotation component in the three fluid regions are given by

where $m_{3} = (\hat{\mu}_{3}+k_{3})/k_{3}$.

Again, inserting formulaes (83)–(93) into conditions (73)–(76) and (78)–(81), we can derive a finite set of nine linear equations for figuring out the unknown constants $\hat{A}_{1}$, $\hat{B}_{1}$, $\hat{}A_{2}$, $\hat{B}_{2}$, $\hat{C}_{2}$, $\hat{D}_{2}$, $\hat{A}_{3}$, $\hat{B}_{3}$, and $\hat{C}_{3}$:

where $\lambda_{23} = 2\mu_{23}/(2+k_{3}/\hat{\mu}_{3})$ with $\mu_{23} = \hat{\mu}_{2}/\hat{\mu}_{3}$ and $\mu_{21} = \hat{\mu}_{2}/\hat{\mu}_{1}$. Here, $\mu_{23}$ represents the ratio of dynamic viscosity coefficients between the inner and outer fluids to the viscous-micropolar interface, and $\mu_{21}$ represents the ratio of dynamic viscosity coefficients between the outer and inner fluids to the droplet. As $\mu_{23}\to\infty$, the fluid outside the viscous-micropolar interface becomes a gas (air), while as $\mu_{23}\to\, 0$, the viscous-micropolar interface becomes a cavity wall (solid wall); on the other hand, as $\mu_{21}\to\infty$, the droplet becomes a gas bubble, while as $\mu_{21}\to\, 0$, the droplet becomes a solid sphere, see Figure 4.

The normalised hydrodynamic drag force $\hat{F}_{z}$ made by the viscous fluid on the viscous droplet's surface in the presence of the viscous-micropolar interface is shown to be ^[31]

Here, the expression (103) demonstrates that the normalised hydrodynamic drag force applied to the viscous sphere droplet relies solely on the coefficient $\hat{D}_{2}$, which can be obtained by solving the system of nine Eqs (94)–(102) using the Gaussian elimination method. To provide some comparison, the normalised hydrodynamic drag force $\hat{F}_{z\infty}$ made by an infinite viscous fluid on the viscous droplet's surface is found to be

The viscous-micropolar interface correction factor $\hat{K}$, with the aid of equations (103) and (104), is defined as

5.   Numerical outcomes and discussion

In this segment, we indicate the numerical outcomes of the factors $K$ and $\hat{K}$ that operate on a viscous sphere drop embedded in a micropolar or viscous fluid. These outcomes are exhibited in Figures 5–8 and Tables 1–5 for a set of values: The spacing ratio $a/b$, the viscosity ratios $(\mu_{12}, \mu_{32}, \mu_{21}, \mu_{23})$, the spin parameters $(s_{1}, s_{2}, s_{3})$, the micropolarity parameters $(k_{2}/\mu_{2}, k_{3}/\hat{\mu}_{3})$, and the parameters $(\gamma_{2}/\mu_{2}a^{2}, \gamma_{3}/\hat{\mu}_{3}a^{2})$. The method of Gaussian elimination is utilised to solve the set of linear Eqs (54)–(63) and (94)–(102) to get the desired unkowns, after utilising the suitable non-dimensional quantities. Thus, the drag force $K$ and $\hat{K}$ can be calculated.

Figures 2 and 4 indicate the difference between the viscosity ratios in the two problems. Also, we test the accuracy of our results in some special cases by comparing them with the solutions of Salem ^[30] and Happel et al. ^[31]; see Tables 1 and 2, respectively. We can also use the CFD (Computional Fluid Dynamics) method (VOF model) to solve this problem and compare it with our analytical results.

Figures 5(a), (b) and 6(a), (b) show that the results for the interface correction factors exerted on a solid sphere and a gas sphere bubble, respectively, moving inside a spherical interface between micropolar/viscous fluids against the spacing ratio $a/b$ at some values of $\mu_{32}$ and $\mu_{23}$. Figures 5(a) and 6(a) indicate the motion of a solid sphere $(\mu_{12}\to\infty)$ and a gas bubble $(\mu_{12}\to\, 0)$, respectively, moving inside a micropolar fluid in the presence of a cavity wall $(\mu_{32}\to\infty)$, coalescence $(\mu_{32} = 1)$, and gas/liquid interface (free surface) $(\mu_{32}\to\, 0)$, while Figures 5(b) and 6(b) indicate the motion of a solid sphere $(\mu_{21}\to\, 0)$ and a gas bubble $(\mu_{21}\to\infty)$, respectively, moving inside a viscous fluid with a cavity wall present $(\mu_{23}\to\, 0)$, coalescence $(\mu_{23} = 1)$, and gas/liquid interface (free surface) $(\mu_{23}\to\infty)$. Figures 5(a), (b) and 6(a), (b) indicate that $K$ and $\hat{K}$ increase monotonically with an increase in the spacing ratio $a/b$ and will grow into infinity when $a/b\to\, 1$ for any certain value of the remaining parameters. For a fixed value of $a/b$ and keeping the other parameters fixed, Figures 5(a) and 6(a) show that $K$ increases with the increase of the viscosity ratio $\mu_{32}$, while Figures 5(b) and 6(b) show that $\hat{K}$ increases with a decrease in the viscosity coefficient $\mu_{23}$, with the minimum and maximum impacts when there is an atmospheric air interface and a solid wall, respectively; this is also shown in Table 3. Clearly, in the case of a solid or gas sphere, the effect of the outer-on-inner interface in the case of a cavity wall is larger than in the case of atmospheric air. Additionally, the values of the drag forces are getting closer to agreement in the case of a solid sphere; while they are getting closer and closer to agreement in the case of a gas sphere, when moving from cavity to air case. Moreover, the drag force on a viscous droplet when it is immersed in micropolar fluid is greater than when it is immersed in viscous fluid; with the minimum and maximum effects in the cases of free atmospheric air interface and solid wall, respectively. Also, these forces depend on both the properties of the object and the properties of the fluid. Its also shown that the values of the drag force on a viscous droplet immersed in a viscous fluid are the largest when compared with those in a micropolar fluid.

Figure 7(a), (b) shows that the results for the interface correction factors $K$ and $\hat{K}$ exerted on a viscous sphere droplet moving inside a spherical interface between micropolar/viscous fluids against the spacing ratio $a/b$ at some values of $k_{2}/\mu_{2}$ and $k_{3}/\hat{\mu}_{3}$. Both indicate that $K$ and $\hat{K}$ increase monotonously with the increase of the spacing coefficient $a/b$. Also, in the case of $\mu_{12} = \mu_{32} = \mu_{21} = \mu_{23} = 1$, for a fixed value of $a/b$, $K$ increases with a decrease in the micropolarity parameter $k_{2}/\mu_{2}$, while $\hat{K}$ increases with an increase in the micropolarity parameter $k_{3}/\hat{\mu}_{3}$, holding constant the other parameters.

Figure 8(a), (b) shows the factors $K$ and $\hat{K}$ against the ratios $\mu_{32}$ and $\mu_{23}$, respectively, for various coefficients. In regard to the complete range of spin parameters $s_{1}$ and $s_{2}$, Figure 8(a) shows that $K$ monotonously increases as $\mu_{32}$ increases; while Figure 8(b) shows that $\hat{K}$ monotonously decreases as $\mu_{23}$ increases, holding constant the other parameters. Also, plots demonstrate that, for a fixed value of $\mu_{32}$ and $\mu_{23}$, $K$ and $\hat{K}$ increase with a decrease in the spin parameters $s_{1}$ and $s_{2}$, respectively. In addition, for a given value of $k_{2}/\mu_{2}$ and $\mu_{12}$, Table 4 shows that $K$ increases as $s_{3}$ increases keeping $s_{1}$ unchanged, while $K$ decreases as $s_{1}$ increases keeping $s_{3}$ unchanged; on the other hand, $K$ increases as $k_{2}/\mu_{2}$ increases keeping $s_{1}$ and $s_{3}$ unchanged. Moreover, Table 5 shows that $\hat{K}$ increases as $k_{3}/\hat{\mu}_{3}$ increases; on the other hand, for a given value of $k_{3}/\hat{\mu}_{3}$ and $\mu_{12}$, $\hat{K}$ decreases as $s_{1}$ increases to a predetermined value of $\mu_{12}$(said $\mu_{o}$), hence it increases with an increase in $s_{2}$ for $\mu_{12} > \mu_{o}$. To illustrate, in Table 5, if $k_{3}/\hat{\mu}_{3} = 3$, $\hat{K}$ decreases with an increase in $s_{2}$ (from $0$ to $3$) up to $\mu_{o} = 4$, hence it increases with an increase in $s_{2}$. As expected, Figure 8(a) and Table 4 show that when the micro-elements of the micropolar fluid surrounding the viscous droplet are in perfect spin $(s_{1} = s_{3} = 1)$, $K$ has minimum, while for no spin $(s_{1} = s_{3} = 0)$, it has maximum, while Figure 8(b) and Table 5 show that when the micro-elements of the viscous fluid surrounding the viscous droplet are in perfect spin $(s_{2} = 1)$, $\hat{K}$ has minimum, while for no spin $(s_{2} = 0)$, it has a maximum. Clearly, for large/small values of viscosity ratios, the drag force is irrelevant with respect to the spin parameter.

6.   Conclusions

A creeping axisymmetric translational movement of a spherical viscous drop moving at a concentric instantaneous position inside a spherical micropolar-viscous interface separating finite and semi-infinite immiscible fluid phases is studied. A connected issue is also studied when a viscous-micropolar interface is present and the viscous sphere droplet is embedded in a viscous fluid. We dealt with three immiscible fluid phases in three different regions. Analytical solutions are obtained for the viscous and micropolar equations pertaining to the fluid flow field associated with these movements, and the effect of interaction between the viscous droplet and the fluid-fluid interface is stated by obtaining formulaes for the interface correction factors. Many special cases are obtained from this study, for example, the movement of a solid sphere and a gas bubble moving inside a micropolar or viscous fluid in the presence of a cavity, coalescence, and gas/liquid interface. As found, the normalised hydrodynamic drag force in general applying on the viscous droplet's surface increases as a function of the droplet-to-interface radius ratio; on the other hand, it is a decreasing and increasing function of the micropolarity parameters, the relative viscosity of the fluid-fluid interface, and the spin parameters. As found, the viscous sphere droplet encounters a maximum interface correction factor when the fluid-fluid interface is to be a cavity wall and a minimum when the fluid-fluid interface is to be a gas/liquid interface. In the two cases of a cavity wall and a gas/liquid interface, as found, the viscous sphere droplet encounters a maximum interface correction factor when the viscous sphere droplet is to be a solid sphere and a minimum when the viscous sphere droplet is to be a gas bubble. Also, at the fluid-fluid interface, as found, the interface correction factors are significantly influenced by the spin parameters. Our results for special cases are in good agreement with the solutions obtained by Salem ^[30] and Happel et al. ^[31].

Author contributions

Ahmed G. Salem: Supervision, conceptualization, software, writing-original draft, writing–review and editing; Turki D. Alharbi: Writing–review and editing; Abdulaziz H. Alharbi: Supervision, writing–review and editing; Anwar Ali Aldhafeeri: Funding acquisition, writing–review and editing. All authors have read and approved the final version of the manuscript for publication.

Acknowledgments

This work was supported by the Deanship of Scientific Research, Vice Presidency for Graduate Studies and Scientific Research, King Faisal University, Saudi Arabia [Grant No. KFU241994].

Conflict of interest

The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.