Abstract
The study presents the mixed convective boundary layer flow of Eyring–Powell fluid over a vertical plate with variable velocity and temperature distribution taking convective boundary condition into account. The transformed non-dimensional governing equations in non-similar nature are solved by employing hybrid technique: local non-similarity method in conjunction with homotopy analysis method. The convergence of homotopy series solution is obtained and presented for various order of approximations. The series solutions have been validated by comparing the results available in the literature and found good agreement. The obtained results are shown properly by graphs and discussed for various values of thermo-physical parameters. It is found that the Eyring–Powell fluid shows higher velocity than Newtonian fluid whereas lower temperature than Newtonian fluid. Furthermore as increase in fluid parameter, ratio of relaxation and retardation parameter, skin friction coefficient decreased and heat transfer coefficient increased. The study finds wide applications in the field of design of heat exchangers, process of cooling of metallic plate, extrusion of plastic sheets, in polymer and glass industries etc.
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Abbreviations
- \( A \) :
-
Cauchy stress tensor (N/m2)
- \( A_{1} \) :
-
Kinematical tensor (N/m2)
- \( C_{f} \) :
-
Local skin friction coefficient
- \( C_{p} \) :
-
Specific heat at constant pressure (J/kg K)
- \( c \) :
-
Fluid parameter (s−1)
- \( {\text{De}} \) :
-
Deborah number
- \( f \) :
-
Non-dimensional stream function velocity
- \( f_{0} \) :
-
Initial guess for non-dimensional velocity
- \( g \) :
-
Gravitational acceleration (m/s2)
- \( {\text{Gr}} \) :
-
Grashof number
- \( n \) :
-
Power index
- \( {\text{Nu}} \) :
-
Local Nusselt number
- \( P \) :
-
Pressure (Pa or N/m2)
- \( p \) :
-
Embedded parameter
- \( I \) :
-
Identity vector
- \( \Pr \) :
-
Prandtl number
- \( \text{Re} \) :
-
Reynolds number
- \( T\, \) :
-
Fluid temperature (K)
- \( V \) :
-
Velocity vector (m/s)
- \( u,v \) :
-
Dimensional velocity components (m/s)
- \( x,y \) :
-
Cartesian coordinates
- \( \alpha \) :
-
Thermal diffusivity (m2/s)
- \( \beta \) :
-
Fluid parameter
- \( \gamma \) :
-
Biot number
- \( \dot{\gamma } \) :
-
Shear rate (s−1)
- \( \tau \) :
-
Extra stress tensor (Pa or N/m2)
- \( \tau_{w} \) :
-
Shear stress (Pa or N/m2)
- \( q_{w} \) :
-
Rate of heat transfer (W/m2)
- \( \mu \) :
-
Dynamitic viscosity (Pa s)
- \( \upsilon \) :
-
Kinematic viscosity of the fluid (m2/s)
- \( \theta \) :
-
Dimensionless temperature
- \( \psi \) :
-
Stream function (m2/s)
- \( \xi \) :
-
Mixed convection parameter
- \( \eta \) :
-
Non-similarity variables
- \( \rho \) :
-
Density of fluid (kg/m3)
- \( \hbar_{i} \) :
-
Control parameter for \( f \), \( g \) and \( h \)
- \( {\mathcal{L}}_{i} \) :
-
Auxiliary linear operator
- \( {\mathcal{N}}_{i} \) :
-
Auxiliary non-linear operator
- w:
-
Wall condition
- ∞:
-
Ambient condition
- ′:
-
Prime denotes the derivative with respect to η
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Ray, A.K., Vasu, B., Murthy, P.V.S.N. et al. Non-similar Solution of Eyring–Powell Fluid Flow and Heat Transfer with Convective Boundary Condition: Homotopy Analysis Method. Int. J. Appl. Comput. Math 6, 16 (2020). https://doi.org/10.1007/s40819-019-0765-1
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DOI: https://doi.org/10.1007/s40819-019-0765-1