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Flow and heat transfer analysis of EyringPowell fluid over stratified sheet with mixed convection
Journal of the Egyptian Mathematical Society volumeÂ 28, ArticleÂ number:Â 40 (2020)
Abstract
This article presents the study of heat transfer under the influence of mixed convective flow of EyringPowell fluid over a stratified stretching sheet. The impact of heat generation/absorption is also discussed. The fluid is considered to be a viscous, incompressible, two dimensional, and laminar. Transformation, based on the similarity variables, is used for the alteration of modeled governing partial differential equations (PDEs) into ordinary differential equations (ODEs). The shooting approach is introduced to accomplish the mathematical solution of governing equations. RungeKutta method of order four is used for the integration purpose and Newtonâ€™s method helps to refine initial guesses. All the programming is done on MATLAB. The effects of emerging parameters on temperature and velocity profiles are discussed through graphs. The related physical properties of flow, i.e., the skin friction coefficient and Nusselt number are described graphically for various parameters. Numerical values for the Nusselt number and skin friction coefficient are tabulated for the various parameters. It is noted that increment in thermal stratification parameter yields fall in both velocity and temperature of fluid and a reverse relation is observed for the heat generation parameter.
Introduction
Heat transfer is a mechanism through which internal energy is transferred from one material to another. It is one of the key point for the researchers, physicists, engineers, and mathematicians. It is extremely important to study the impact of heat transfer in various materials and boundary layer flows over stretching sheet due to their considerable applications in various biological phenomena, engineering processes, and industrial units like paper production, metal extrusion, fermentation, and bubble absorption [1â€“13]. The basic concern of heat transfer study is to prevent the heat loss in important industrial processes. The heat loss has one of the disadvantage that it increases the cost of product due to extra consumption of heat as well as it may cause the malfunctioning of the products. Heat transfer occur in three ways known as conduction, convection, and radiation. Heat transfer through physical contact, through motion of fluid, or through radiation is called conduction, convection, and radiation respectively. In general terms when we talk about convection, the heat transfer occurs between some sorts of fluid and fixed or moving surface. The process of convection is divided into three sub categories, free convection or natural convection, forced convection, and mixed convection. The basic principle dealing with the natural or free convection is through continuous transfer of the heat flow between two surfaces or materials when there is considerable force of buoyancy. When we talk about forced convection, there is some sort of external force that causes to transfer the heat between the two materials. Chen [14] provided an analysis of mixed convection in boundary layers flow on a vertical and constantly stretching sheet. He used finite difference method to solve the problem. Ali [15] researched numerically the impact of temperaturedependent viscosity on the laminar mixed convection flow over a continually moving vertical surface. He found the critical values of mixed convection for which variable viscosity assists or oppose the flow. Hayat et al. [16] provided an analysis for the twodimensional mixed convection boundary layer flow on MHD stagnation point through a porous medium bounded by a vertical stretching plate, taking into account the radiation effect. Ali and Yousef [17] analyzed the boundary layer flow due to buoyancy forces through a uniformly moving vertical surface with suction or injection. The plate when placed vertically affects the heat flow and the buoyancy factor. Khan et al. [18] investigated the important aspects of magnetic nanofluids and stratification process under the linear convection. Shooting method is applied for the nonlinear stretching sheet to analyze the impact of viscosity effects and understand the different behaviors of Willamson nanofluid. Hayat et al. [19] examined the MHD effect with Joule heating for heat and mass transfer through the double stratified sheet. The various physiochemical parameters of heat flow are analyzed both numerically and graphically. The results shows the subsequent reduction of mean absorption coefficient with increase in temperature profiles. Heat and fluid flow passing over a rotating disk was considered by Hayat et al. [20]. The magnetohydrodynamics flow of nanofluid using the double stratification impact is analyzed analytically. The analytical solutions were calculated after the use of boundary layer approximation. The results depict that the Prandtl number has direct relation with heat flow and indirect with the temperature of the fluid.
Fluid flow analysis along stretching/shrinking sheet is a major concern for researchers. The maximum composition of our cellular mass is consisting of fluids, air, and water, and there are subsequent amount of essential body fluids in correct proportion that aids to lead a healthy life. The fluid flow over a stretched surface has many applications in industrial processes and engineering, liquid films in condensation process, paper production, drawing of plastic wires and films, crystal glowing, glass blowing, food industries, coatings, drug delivery system, paints, ceramics, manufacturing of rubber sheets, etc. Sakiadis [21, 22] was the first to examine the boundary layer flow on a continuous flat and cylindrical surfaces moving at a coherent velocity. Dandapat and Gupta [23] analyzed the heat transfer flow in the viscoelastic fluid along the stretching sheet. The boundary layer flow was analyzed in depth over a continuous solid surface and contrasted with the moving surface of finite length. Erickson et al. [24] considered the boundary layer flow with suction and injection and numerically resolved the energy and the diffusion equation. Flow produced by stretching sheet is discussed by Crane [25]. Anderson et al. [26] examined the powerlaw fluid flow under the effect of magnetic forces, over a linearly stretched surface. An OldyroydB fluid flow with the influence of heat generation/absorption is depicted by Hayat et al. [27]. Fluid flow over curved stretching surface using curvilinear coordinate was first investigated by Sajid et al. [28].
Scientists nowadays are trying to investigate the effects of shear stress and fluid flow of nonNewtonian fluids due to their industrial need. The nature of the nonNewtonian fluids is diverse and cannot be explained by a single reference equation. The nonNewtonian fluids exhibit a nonlinear correlation between stress and strain. The preference is given to EyringPowell fluid over the other nonNewtonian fluids due to the fact that it is based on kinetic molecular model of liquids not on the empirical relation. The key role of various fluids in industries draws the attention of investigators to look and find their usage and hurdles caused by various heat flow phenomenon. Ibrahim et al. [29] investigated the magnetohydrodynamics (MHD) boundary layer flow of EyringPowell nanofluid by using the CattaneoChristov heat flux model. The purpose of this study was to discuss the strong correlation between the influx of heat transfer, characterization for the conservation of mass, energy, and momentum. Eldabe et al. [30] tried to focus on magnetohydrodynamics effect on nonNewtonian, unsteady and incompressible fluid when subjected to the extreme stress in combination with outlying electric field. The mathematical model of EyringPowell fluid was solved by applying the computational tools on nonlinear partial differential equations. Both the firstorder and secondorder approximation were being calculated by the finite difference technique. Malik et al. [31] tried to investigate the mixed convection flow over the stretching plate for MHD EyringPowell fluid and numerically solved the problem by applying shooting method. The results indicate significant decrease in heat and mass transfer by enhancing EyringPowell material parameter. A study is being carried by Ogunseye et al. [32] that focuses the thermal properties and characteristics of EyringPowell nanofluid for minimum entropy loss. A recent study of Prand et al. [33] discusses the boundary layer flow of EyringPowell fluid with thermal and physiochemical aspects of heat and fluid flow. Saleh et al. [34] investigated comprehensively the transferal of heat and the uniform, steady boundary layer flow of EyringPowell fluid by Newtonian heating model. They have implemented the finitedifference method to solve the nonlinear differential equations.
After carefully reviewing the above cited research, it is feel that the EyringPowell fluid model with mixed convection boundary layer flow over a stratified stretching sheet with heat generation/absorption is still missing in the literature. The model includes an energy equation to analyze the temperature flow over the stratified stretching sheet. By using the boundary layer approximation and implementing appropriate similarity transformations, the governing partial differential equations together with the boundary conditions are changed to dimensionless form. Numerical scheme based primarily on shooting technique is implemented for ODEs system. Graphs and tables are used to discuss the impacts of distinct physical parameters. Numerical outcomes for the Nusselt number and skin friction are also calculated. At the end of this article, we will be able to answer the folliwng questions: What is the impact of EyringPowell fluid parameter on the velocity profile? Does the mixed convection parameter have any effect on the velocity of the fluid? How does the stratified sheet help to boost the temperature of the fluid? Is the impact of heat generation and heat absorption the same?
Mathematical formulation
A twodimensional steady mixed convection flow of an incompressible EyringPowell fluid through stratified stretching sheet has been considered as given in Fig.Â 1. Sheet is stretching at constant speed U_{w}=ax in vertical direction along the xâˆ’axis. T_{w} and T_{âˆž} are respectively the fluid temperature at wall and far away from the wall. The free stream velocity of the fluid is 0. Further, the effect of heat generation absorption is reviewed in the energy equation. In the problem, we have ignored the suction/injection and viscous dissipation effects.
The boundary layer approximation reduces the equation of continuity and the equation of momentum into the following form [35]:
where Î² and C are the dimensional EyringPowell fluid material parameters, Î¼ represents the kinematic viscosity of fluid, and g denotes the gravitational acceleration. Under boundary layer approximation, the energy equations takes the form:
where k denotes thermal conductivity, C_{p} is the specific heat at constant pressure, and Q is the heat generation/absorption coefficient. The boundary conditions for the present flow problem is given by
where u and v represent the horizontal and vertical components of fluid velocity. Also, T_{0} is used to denote the stretching sheet reference temperature and b_{1} and b_{2} are positive dimensional constants. The simultaneous PDEs with the corresponding boundary conditions are reduced to ODEs using similarity transformation. In this case, the equation of continuity is identically satisfied while the momentum and energy equations are reduced to nondimensional ODEs. The following stream function is defined
now using the recommended similarity transformation as
where Ï† is stream function, f(Î·) is dimensionless stream function, and Î· presents similarity variable, also
So, the final dimensionless form of the present problemâ€™s mathematical model is
with boundary conditions
different parameters used in the above equations have the following formulations:
skin friction coefficient and Nusselt number is given as
Ï„_{w} is shear stress and q_{w}=âˆ’k(âˆ‚T/âˆ‚y)_{y=0} is heat flux at the surface. The dimensionless form of skin friction coefficient and Nusselt number is
where Re_{x} represents local Reynolds number and is defined as
Solution methodology
The governing problem is solved numerically by shooting method which is a very well known numerical technique [36â€“40]. For the transition of equations, first rewrite them again in the following form
The problems with the boundary value can not be analytically solved readily because these ODEs are nonlinear and coupled. The technique of shooting was therefore regarded for the sake of numerical solutions. The fourthorder Runge Kutta and Newtonâ€™s method are the main features in the shooting method for solving the nonlinear differential equations. Now, let us use the following notations to convert them into the first order ODEs.
the system obtained as:
the initial conditions take the following form:
For the sake of numerical solution of the above system of equations, take the bounded domain [0,Î·_{âˆž}].Î·_{âˆž} is finite real number. Here, c and d are supposed initial conditions. Selection criteria of missing initial equations is
initially c=c_{0},d=d_{0} is chosen as the missing condition. To refine these initial conditions, the Newtonâ€™s method is utilized, which has the following iterative scheme
Initial value problem is solved by RungKutta method of order four with c_{0} and d_{0} as the supposed initial conditions. Iterative process kept on working until the stopping criteria is obtained. The stopping criteria is given by
where Îµ is a positive number and is fixed as Îµ=10^{âˆ’6}.
Result and discussion
In this section, the results are given in tabular and graphical form. FigureÂ 2 shows the effect of Îµ (material parameter) on dimensionless velocity of the fluid. The parameter Îµ is inversely proportional to the nonNewtonian fluidâ€™s dynamic viscosity. Increase in Îµ will result in lower the flow resistance. This decrement in flow resistant will increase the velocity of the fluid. FigureÂ 3 shows the effect of Îµ on temperature of the fluid. As stated above, increase in Îµ decreases the viscosity of the fluid that contributes for the temperature reduction.
FigureÂ 4 shows the impact of material parameter Ïƒ on fluid velocity. We see from the graph that the velocity of fluid increases with an increase in Ïƒ. As Ïƒ is directly related with the velocity of the sheet, and due to higher stretching speed, the velocity of the fluid will also enhances. FigureÂ 5 shows the impact of Ïƒ on temperature of the fluid. It is evident from the graph that the temperature of fluid decreases with an increase in Ïƒ. FigureÂ 6 is drawn to see the influence of mixed convection parameter Î» on velocity profile. Graph depicts that enhancing Î» brings growth in fluid velocity. The reason behind this increment is the thermal buoyancy force. Due to higher buoyancy force, the momentum boundary layer thickness gets enlarged. FigureÂ 7 shows the effect of mixed convection parameter Î» on temperature of the fluid. It is witnessed from the graph that boosting value of Î» causes a reduction in thermal buoyancy force which reduces the temperature of fluid. FigureÂ 8 shows the influence of Prandtl number on velocity profile f^{â€²}(Î·). Pr has direct relationship with viscosity of the fluid. Increase in Pr makes the fluid more dense, which causes a decrease in the velocity profile. FigureÂ 9 gives the Prandtl number Pr effect on temperature profile. This dimensionless number is reversely associated with thermal conductivity k and implies that the fluids with greater Prandtl number Pr holds weak energy diffusion. So, upgrading in Prandtl number Pr creates a strong reduction in temperature of the fluid which results in thinner thermal boundary layer. The impact of thermal stratification parameter e_{1} is shown in Fig.Â 10. It is witnessed through the graph that magnifier thermal stratification declines the motion of the fluid. This effect is noted because of the reduction of the convective potential between sheet surface and ambient temperature. The temperature Î¸(Î·) of the moving fluid decreases for the higher stratification parameter. The temperature difference between the ambient fluid and the fluid on the surface declines with respect to e_{1} which resultantly reduces the temperature as shown in Fig.Â 11. Impact of Î³ is displayed through Fig.Â 12. Increasing heat generation parameter Î³ gives rise to the velocity of fluid over stretching sheet. The temperature of fluid increases with increasing the heat generation parameter Î³ as shown in Fig.Â 13.
TableÂ 1 shows the impact of material parameters Ïƒ and Îµ, Prandtl number Pr, mixed convection parameter Î», thermal stratification parameter e_{1}, and chemical reaction parameter Î³ on skin friction coefficient and Nusselt number. Material parameters Îµ and Ïƒ, mixed convection parameter Î», and heat generation parameter Î³ have a direct relation with skin friction. Increase in these parameters shows an increment in skin friction while increase in Prandtl number and thermal stratification parameter causes a reduction in the skin friction coefficient. Heat generation parameter Î³ and fluid material parameter Ïƒ shows a direct relation with Nusselt number âˆ’Î¸^{â€²}(0). Increasing these parameters causes a rise in the value of Nusselt number whereas increasing Îµ, mixed convection parameter Î», Prandtl number Pr, and thermal stratification parameter e_{1} shows a decrease in the value of Nusselt number.
Summary
In this article, we have explored the mixed convection boundary layer flow of EyringPowell fluid through the stratified stretching sheet. The fluidâ€™s characteristics such as viscosity and thermal conductivity are taken independent of temperature. The dimensionless velocity and dimensionless temperature are investigated and displayed in the form of graphs and tables. For different values of the specific physical parameters, the Nusselt number and skin friction are provided in the tabular form. From the present investigation, we can draw the following conclusions:

Increase in EyringPowell fluid material parameter Îµ give rise to the velocity and temperature of fluid drops over stretching sheet.

Increasing the EyringPowell material parameter Ïƒ shows a rise in temperature but decline of velocity profile.

When mixed convection parameter Î» is increased, the velocity of fluid increases; however, temperature falls.

With increase in Prandtl number Pr, the velocity and temperature of fluid show reduction behavior.

The strength of the thermal stratification parameter e_{1} can help to control the velocity and temperature of fluid.

By increasing the values of heat generation parameter Î³, we get the increment in both velocity and temperature profiles.
Availability of data and materials
All the data generated and materials during this study are included in this research article.
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M. Bilal carried out the problem design, code validation, methodology, reading, and correction. S. Ashbar did the computation, draft preparation, and writing. The authors read and approved the final manuscript.
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Bilal, M., Ashbar, S. Flow and heat transfer analysis of EyringPowell fluid over stratified sheet with mixed convection. J Egypt Math Soc 28, 40 (2020). https://doi.org/10.1186/s42787020001036
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DOI: https://doi.org/10.1186/s42787020001036