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Article

Heat Transfer Analysis on Peristaltic Transport of a Jeffery Fluid in an Inclined Elastic Tube with Porous Walls

by
G. Manjunatha
1,
C. Rajashekhar
2,
Hanumesh Vaidya
3,*,
K. V. Prasad
3,
Saraswati
3 and
B. B. Divya
1
1
Department of Mathematics, Manipal Institute of Technology, Manipal Academy of Higher Education, Manipal-576104, Karnataka, India
2
Bhaskaracharya Study Chair, Karnataka State Akkamahadevi Women’s University, Vijayapura-586108, Karnataka India
3
Department of Mathematics, Vijayanagara Sri Krishnadevaraya University, Jnana Sagara Campus,Vinayaka Nagar, Ballari-583 105, Karnataka, India
*
Author to whom correspondence should be addressed.
Int. J. Thermofluid Sci. Technol. 2020, 7(1), 070101; https://doi.org/10.36963/IJTST.20070101
Submission received: 30 July 2020 / Revised: 10 December 2020 / Accepted: 20 December 2020 / Published: 10 January 2020

Abstract

This article analyses the effects of heat transfer and thermal conductivity on the peristaltic transport of Jeffery fluid through an inclined elastic tube with porous walls. The velocity slip and convective boundary conditions are taken into account. The modeled governing equations are solved analytically by considering the long wavelength and small Reynolds number approximations. The closed-form solutions are obtained for velocity, flow rate, and the theoretical determination of flow rate is calculated with the help of equilibrium condition given by Rubinow and Keller. A parametric analysis has been presented to study the effects of Jeffery parameter, thermal conductivity, Darcy number, the angle of inclination, velocity slip, Biot number, amplitude ratio, Prandtl number, and Eckert number on velocity, flow rate, and temperature are scrutinized. The streamlines show that the bolus moves with the same speed as that of the wave and further the study reveals that an increase in the Biot number reduces the magnitude of the temperature.

1. Introduction

The investigation of heat transfer effects along with slip conditions on peristalsis has bought the attention of researchers in past decades due to their extensive application in sanitary fluid transport, heart-lung machines, laser therapy, hypothermia treatment, transport of corrosive fluids and coldness cryosurgery (Jaggy et al., 2000). The examination of heat transfer is concerned with temperature and the flow of heat. Where temperature decides the amount of thermal energy available while heat flow indicates the movement of thermal energy from one place to another. In general, the heat transfer can happen in three unique classes: conduction, convection, and radiation. Among the three classifications, the convective method of heat transfer assumes an indispensable part in numerous applications. Mainly, it is utilized as a part of oxygenation and hemodialysis. Keeping this in mind, numerous scientists have explored the fluid characteristics by taking convective boundary conditions alongside variable thermal conductivity (Hayat et al., 2013; Alsaedi et al., 2013; Abbasi et al., 2015; Hayat et al., 2016; Sayed et al., 2016; Abdul, 2017; Srinivasa, 2017; Prasad et al., 2018(a)). The initial studies on the peristaltic transport of a Newtonian/non-Newtonian fluid has been carried out by many researchers by taking different assumptions and configuration (Latham, 1966; Burns and Parkes, 1967; Raju and Devanathan, 1972; Vajravelu et al., (2016)(a); Vajraveluet al., (2016)(b); Prasad et al., 2017; Manjunatha and Rajashekhar, 2018; Prasad et al., 2018(b); Vaidya et al., 2019 (a-d)). Among the several non-Newtonian models, the Jeffery model is more significant in describing the flow of blood in arteries. The studies on the use of the Jeffery model was carried out by Hayat et al. (2007) to investigate the peristaltic transport in a circular tube. Nadeem and Akram (2010) analyzed the peristaltic transport in a rectangular duct and obtained the exact solutions for pressure rise and pressure gradient. Further, several authors used the Jeffery model for investigating the peristaltic transport with different geometries and assumptions to represent the specific living situation (Vajravelu et al., 2011; Bhatti and Abbas, 2016; Selvi et al., 2017).
The flow of biological fluids through porous media plays a vital role in understanding the various mechanism in gallbladder, lungs, blood vessel movement, etc. These applications of porous media in biofluid dynamics and biomechanics have attracted researchers in recent times. In the human body, a large part of the tissues, like, muscles, ligaments, and bones form a deformable porous media. In such conditions, the presence of slip on the boundary because of the permeability of the walls has a necessary effect in reviewing the biological fluids. Thus, slip effects are more verbalized for fluids going through geometries which have flexible property, like blood vessels. This slip flow of fluids is used in the polishing of the internal cavities and artificial heart valves. The exploratory examinations on non-Newtonian fluids revealed the centrality of slip at the walls. The peristaltic flow of blood through a tube can be idealized better by considering slip and permeability. Studies on the utilization of porous walls on peristaltic transport have been initially explored by Elshehawey et al. (1999). Later, various researchers examined the impact of slip velocity on the peristaltic mechanism by using different models under different assumptions and geometries (Nadeem and Akram, 2011; Tripathi and Beg, 2012; El-Koumy et al., 2012; Manjunatha et al., 2019(a-c)).
It is important to note that, the Poiseuille's law shows that for a fluid which is incompressible, the flux in the tube is a linear function of the pressure difference between the ends of the rigid tube through which it flows. Hence, the non-Newtonian fluids obey Poiseuille’s law in most of the theoretical as well as experimental studies. The nonlinearity in vascular beds of warm-blooded creatures is ascribed to the flexible idea of veins and their immense distensibility. This elastic property of veins was first perceived by Young (1968). Further, Rubinow and Keller (1972) showed that the scope of the tube could be controlled by the strain in the dividers and the transmural weight contrast by accepting that the Poiseuille law holds locally. Consequently, there is a necessity for the subjective speculation of blood flow through elastic tubes. The stream designs bought by the models with a rigid tube can't clarify the flow of blood in narrow arteries completely. Henceforth, it becomes important to consider the elasticity in the present model.
To the best of the authors' knowledge, no attempts have been made in the literature to investigate the role of variable thermal conductivity, convective boundary conditions and inclination on peristaltic transport of Jeffery fluid in an axisymmetric elastic tube with porous walls. The present investigation helps to fill the gap in this direction. The resulting modeled equations are solved analytically under the proper slip boundary conditions. The influence of pertinent parameters on velocity, flow rate, temperature, and streamlines are presented graphically. The outcomes of the present model help in understanding the complex physiological behavior of blood in the circumstances mentioned above, which intern helps medical people to investigate the blood flow in arteries a much better way than the earlier and, helps in modeling the heart-lung and dialysis machines.

2. Mathematical Formulation

The flow is considered to be laminar, steady, incompressible, fully-developed, axisymmetric and exhibiting peristalsis in an elastic tube with porous walls (See Figure 1). The fluid is characterized by the Jeffery model and facilitates the choice of the cylindrical coordinate system to study the problem. The wall deformation due to the propagation of an infinite sinusoidal wave train of peristaltic waves is represented by
Ijtst 07 070101 i001
Consider the constitutive equations on the peristaltic transport of incompressible viscous Jeffery fluid represented by the following expressions
Ijtst 07 070101 i002
Ijtst 07 070101 i035
where Ijtst 07 070101 i003 is the Cauchy’s stress tensor, Ijtst 07 070101 i004 is the extra tensor, Ijtst 07 070101 i005 is the identity tensor, λ1 is the ratio of relaxation to retardation time, λ2 is the retardation time and γ is the shear rate and dots over the quantities indicate differentiation with respect to time.
The flow becomes steady in the wave frame (r, θ, z) moving with velocity c away from the fixed frame (R,Θ, Z) given by
Ijtst 07 070101 i006
where p and P are pressures, ψ and Ψ are stream functions, in the wave and fixed frames of references, respectively.
The pressure p remains constant at any axial station of the tube under the assumption of long wavelength approximation. Using the following nondimensional variables
Ijtst 07 070101 i007
The non-dimensional equations of motion and energy in the wave frame of reference, moving with speed c, under the lubrication approach is as follows:
Ijtst 07 070101 i008
where u and w are the radial and axial velocities, Re is the Reynolds number, θ is temperature, δ is wave number, Pr is the Prandtl number, Ec is the Eckert number, r is radial coordinate, τrr is shear stress in radial coordinates τzr is shear stress in axial and radial coordinates, τzz is shear stress in axial coordinate and τrz is the shear stress along radial and axial coordinates.
Under the assumption of long wavelength and small Reynolds number, Equations (5)–(7) takes the form
Ijtst 07 070101 i009
Ijtst 07 070101 i036
The corresponding non-dimensional boundary conditions are (Saffman, 1971; Abbasi et al., 2015)
Ijtst 07 070101 i010
where Da is the porous parameter (Darcy number), α is the velocity slip parameter, ϕ is the thermal conductivity, k(θ) = 1 + ϕθ, ϕ << 1, Ijtst 07 070101 i011 is the Biot number and l is the heat transfer coefficient of the wall and θ is the temperature.
The closed-form solutions are obtained for the velocity expression (8) and (9) satisfying the boundary conditions (11) and (12), we obtain the velocity as
Ijtst 07 070101 i012
where Ijtst 07 070101 i013 and Ijtst 07 070101 i014 Using Equation (10) together with the boundary conditions (11) and (12), we obtain an expression for temperature as
Ijtst 07 070101 i015

2.1. Theoretical Determination of flux: Application to Flow Through an Artery

A theoretical calculation of the flux Q is carried out for an incompressible Jeffery fluid through an elastic tube of radius h(z, t) = h'(z, t) + h''(z). The fluid is assumed to enter the tube with pressure p1 and leave the tube with pressure p2, while the pressure outside the tube is p0. If z denotes the distance along the tube from the inlet end, then the pressure p(z) in the fluid at z diminishes from p(0) = p1 to p(λ) = p2 . The tube may contract or expand due to the difference in the pressure of the fluid p(z) − p0. Subsequently, the cross-section of the tube may have a deformation due to the elastic property of the walls. Thus, the difference in pressure influences the conductivity σ1 of the tube at z . We consider the conductivity σ1 = σ1[ p(z) − p0] to be a known function of the pressure difference (p(z) − p0). This conductivity is assumed to be the same as that of a uniform tube having an identical cross-section at z . The relation between Q and the pressure gradient is given by
Ijtst 07 070101 i016
Under the considerations of peristaltic motion and the elastic property of the tube wall, Equation (15) can be written as,
Ijtst 07 070101 i017
where Ijtst 07 070101 i018 and h″ is the change in radius of the tube due to elasticity and is a function of pressure p − p0 at each cross-section due to the Poiseuille flow. Equation (15) with the inlet condition p(0) = p1 gives
Ijtst 07 070101 i019
where p ' = p(z) − p0 . Equation (17) gives p(z) in terms of z and Q by setting z = 1 and p(1) = p2 we get Q as,
Now, using Equation (17) in Equation (18), we have
Ijtst 07 070101 i020
Equation (19) can be solved if we explicitly know the function h''( p − p0). If h'' is known as a function of the tension T(h'') or stress, then h''( p') can be determined from the equilibrium condition (Rubinow and Keller, 1972) given by
Ijtst 07 070101 i021
Rubinow and Keller (1972) carried out experimental investigations by controlling the static pressure-volume connection of a 4-cm long piece of a human iliac artery and gave an expression for tension in an elastic tube as:
Ijtst 07 070101 i022
Using Equation (21) with t1 = 13 and t2 = 300, Equation (20) takes the following form
Ijtst 07 070101 i023
Using Equation (22), Equation (19) can be written as
Ijtst 07 070101 i024
Letting p = p1 and p = p2 in Equation (20) the solutions are obtained for Ijtst 07 070101 i025 respectively.
Equation (23) can be rewritten as
Ijtst 07 070101 i026
where,
Ijtst 07 070101 i027

3. Results and Discussion

The present paper emphasizes on the combined effects of slip and heat transfer on the peristaltic transport of Jeffery fluid in an inclined elastic tube with porous walls. Figure 2, Figure 3, Figure 4, Figure 5, Figure 6, Figure 7, Figure 8 and Figure 9 are plotted to observe the effects of Jeffery parameter (λ1), the angle of inclination (β), porous parameter (Da), velocity slip parameter (α), amplitude ratio (ε), elastic parameters (t1,t2), inlet and outlet elastic radius (h", h"), Brinkmann number (Br), thermal conductivity (ϕ) and Biot number (Bi) on velocity (w), flow rate (Q), streamlines (ψ) and temperature (θ). MATLAB programming is used to plot these effects of physiological parameters.
Velocity profiles are plotted in Figure 2 for different values λ1, Da, ε, β and α. It is noticed that the velocity profiles are parabolic in nature with the maximum velocity at the center of the tube. From Figure 2a–d it is observed that for a larger value of λ1, Da, ε and β the magnitude of the velocity increases. Whereas, an increase in the value of α decreases the magnitude of the velocity. Figure 3 and Figure 4 are plotted to examine the effects of Ijtst 07 070101 i028 on flow rate. Figure 3(a) depicts the variation of λ1 on flow rate. It is observed from the figure that an increase in the values of λ1 enhances the flow rate in an elastic tube. Figure 3(b) shows the variation of Da on flow rate. It is noticed that an increase in the values of Da increases the volume of flow rate.
The influence of α on flow rate shows the opposite behavior as that of Da (See Figure 3(c)). Figure 3(d) portrays the variation of β on flux. It is observed that the impact of increase in the angle β increases the volume of flow rate. The variation of ε on flow rate is illustrated in Figure 3(e). It is clear from the figure that an increase in the value of ε increases the volume of flow rate. Since ε is the amplitude ratio, an increase in the value of ε results in an increase in the wave height which in turn increases the flux. Figure 4(a and b) are drawn to study the effects of t1 and t2 on Q respectively. We see from these figures that an increase in the values of t1 and t2 enhances the flow rate. Further, the variation of inlet and outlet elastic radius Ijtst 07 070101 i029 and Ijtst 07 070101 i030 on Q are plotted in Figure 4(c and d). For a fixed value of Ijtst 07 070101 i031, the effect of increasing values of Ijtst 07 070101 i032 makes flow rate to decrease (See Figure 4(c)). However, Fig.4(d) exhibits the opposite behavior when we fix Ijtst 07 070101 i033 and vary Ijtst 07 070101 i034.
The effects of λ1, ε, Da, ϕ, Bi and Br on temperature are plotted in Figure 5. The temperature profiles are non-parabolic and show the dual nature. The role of λ1 on temperature is shown in Figure 5(a). The temperature decreases with increasing values of λ1 . Finally, the behavior of ε on temperature shows the opposite trend as that of λ1 (Figure 5(b)). The role of Da on temperature is examined in Figure 5(c). It is observed that the increasing values of Da decrease the temperature near the axis of the tube and opposite behavior is observed near the walls. The effect of ϕ plays a vital role in the determination of temperature. It means that a larger value of ϕ increases temperature near the axis of the tube and the effect is negligible near the walls (See Figure 5(d)). This is because of an increase in the value of ϕ allows the fluid to dissipate or absorb heat to its surroundings. Hence, an increase in ϕ decreases the temperature near the walls of the tube. Figure 5(e) depicts the variation of temperature due to the influence of Bi. An increase in the value of Bi results in the reduction of temperature. Figure 5(f) illustrates the effect of Br on temperature. It is found that an increase in the value of Br increases temperature. Since Ec occurs due to the viscous dissipation effects and it enhances temperature. Further, an increase in the value of Pr decrease thermal conductivity and thereby increases temperature.
The essential part of peristalsis is trapping. It is by and large the arrangement of the inside flowing bolus. These trapped boluses push ahead alongside the sinusoidal movement of the peristaltic wave. This phenomenon is particularly useful in bloodstream issues, for example, the arrangement of thrombus and transport of food bolus in the gastrointestinal tract. Figure 6, Figure 7 and Figure 8 shows that the size of trapped bolus decreases as we increase the value of λ1, Da and ε and hence it increases the number of bolus formations. Whereas it increases with an increase in the value of α and thereby, it vanishes the trapped bolus for larger values of α which is observed in Figure 9. From these figures, one can observe that the bolus moves at the same speed as that of the wave.

4. Conclusions

It is worth noticing that, from the current model, one can deduce the results of a Newtonian model by taking λ1 = 0. The present study provides a satisfactory outcome that represents some of the natural phenomena, especially the flow of blood in narrow arteries, which can be handled and processed in case of dysfunction. The conclusions can be summarized as follows:
The axial velocity increases with an expansion in the estimation of the porous parameter, and it diminishes for a larger value of velocity slip parameter.
The flow rate in an incline elastic tube increases with an expansion in the porous parameter, and it diminishes with an increment in the slip parameter.
The influence of the Jeffery parameter and angle of inclination enhances the flow rate.
The effects of elastic parameters, outlet elastic radius and amplitude ratio increases the flow rate while the inlet elastic parameter decreases the flow rate.
The magnitude of temperature diminishes with an expansion in the Biot number and the temperature depended thermal conductivity increases the temperature close to the axis and the impact is irrelevant close to the walls.
The volume of tapered bolus diminishes with expanding porous parameter, and it increments for larger values of the velocity slip parameter.

Acknowledgments

The authors appreciate the constructive comments of the reviewers which led to definite improvement in the paper.

References

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Figure 1. Geometrical representation of Peristaltic waves in an elastic tube.
Figure 1. Geometrical representation of Peristaltic waves in an elastic tube.
Ijtst 07 070101 g001
Figure 2. w v/s r with varying (a) Jeffery parameter (λ1), (b) porous parameter (Da), (c) amplitude ratio (ε), (d) angle of inclination (β and (e) velocity slip parameter (α).
Figure 2. w v/s r with varying (a) Jeffery parameter (λ1), (b) porous parameter (Da), (c) amplitude ratio (ε), (d) angle of inclination (β and (e) velocity slip parameter (α).
Ijtst 07 070101 g002
Figure 3. Q v/s z with varying (a) Jeffery parameter (λ1), (b) porous parameter (Da), (c) velocity slip parameter (α), (d) angle of inclination (β) and (e) amplitude ratio (ε).
Figure 3. Q v/s z with varying (a) Jeffery parameter (λ1), (b) porous parameter (Da), (c) velocity slip parameter (α), (d) angle of inclination (β) and (e) amplitude ratio (ε).
Ijtst 07 070101 g003
Figure 4. Q v/s z with varying (a) elastic parameter (t1), (b) elastic parameter (t2), (c) inlet elastic radius (Ijtst 07 070101 i037) and (d) outlet elastic radius (Ijtst 07 070101 i038).
Figure 4. Q v/s z with varying (a) elastic parameter (t1), (b) elastic parameter (t2), (c) inlet elastic radius (Ijtst 07 070101 i037) and (d) outlet elastic radius (Ijtst 07 070101 i038).
Ijtst 07 070101 g004
Figure 5. θ v/s r with varying(a) Jeffery parameter (λ1), (b) varyingamplitude ratio (ε), (c) porous parameter (Da), (d) thermal conductivity (ϕ), (e) Biot number (Bi) and (f) Brinkmann number (Br).
Figure 5. θ v/s r with varying(a) Jeffery parameter (λ1), (b) varyingamplitude ratio (ε), (c) porous parameter (Da), (d) thermal conductivity (ϕ), (e) Biot number (Bi) and (f) Brinkmann number (Br).
Ijtst 07 070101 g005
Figure 6. Streamlines for varying (a)λ1 = 0 , (b) λ1 = 0.2 , (c) λ1 = 0.4 and (d) λ1 = 0.6.
Figure 6. Streamlines for varying (a)λ1 = 0 , (b) λ1 = 0.2 , (c) λ1 = 0.4 and (d) λ1 = 0.6.
Ijtst 07 070101 g006
Figure 7. Streamlines for varying (a)Da = 0.01, (b) Da = 0.02, (c) Da = 0.03 and (d) Da = 0.04.
Figure 7. Streamlines for varying (a)Da = 0.01, (b) Da = 0.02, (c) Da = 0.03 and (d) Da = 0.04.
Ijtst 07 070101 g007
Figure 8. Streamlines for varying (a)ε = 0.3, (b) ε = 0.4, (c) ε = 0.5 and (d) ε = 0.6.
Figure 8. Streamlines for varying (a)ε = 0.3, (b) ε = 0.4, (c) ε = 0.5 and (d) ε = 0.6.
Ijtst 07 070101 g008
Figure 9. Streamlines for varying (a)α = 0.1, (b) α = 0.2, (c) α = 0.3 and (d) α = 0.4.
Figure 9. Streamlines for varying (a)α = 0.1, (b) α = 0.2, (c) α = 0.3 and (d) α = 0.4.
Ijtst 07 070101 g009

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Manjunatha, G.; Rajashekhar, C.; Vaidya, H.; Prasad, K.V.; Saraswati; Divya, B.B. Heat Transfer Analysis on Peristaltic Transport of a Jeffery Fluid in an Inclined Elastic Tube with Porous Walls. Int. J. Thermofluid Sci. Technol. 2020, 7, 070101. https://doi.org/10.36963/IJTST.20070101

AMA Style

Manjunatha G, Rajashekhar C, Vaidya H, Prasad KV, Saraswati, Divya BB. Heat Transfer Analysis on Peristaltic Transport of a Jeffery Fluid in an Inclined Elastic Tube with Porous Walls. International Journal of Thermofluid Science and Technology. 2020; 7(1):070101. https://doi.org/10.36963/IJTST.20070101

Chicago/Turabian Style

Manjunatha, G., C. Rajashekhar, Hanumesh Vaidya, K. V. Prasad, Saraswati, and B. B. Divya. 2020. "Heat Transfer Analysis on Peristaltic Transport of a Jeffery Fluid in an Inclined Elastic Tube with Porous Walls" International Journal of Thermofluid Science and Technology 7, no. 1: 070101. https://doi.org/10.36963/IJTST.20070101

APA Style

Manjunatha, G., Rajashekhar, C., Vaidya, H., Prasad, K. V., Saraswati, & Divya, B. B. (2020). Heat Transfer Analysis on Peristaltic Transport of a Jeffery Fluid in an Inclined Elastic Tube with Porous Walls. International Journal of Thermofluid Science and Technology, 7(1), 070101. https://doi.org/10.36963/IJTST.20070101

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