Abstract
This study numerically simulates optimal thermal convection and entropy production minimization in a steady magnetohydrodynamic micropolar hybrid nanofluid (Ag–Al2O3/H2O) flow through an annulus region bounded between an elliptical cylinder (inner) and a square cylinder (outer) with partially insulated and partially heated walls. Four different configurations with heater locations were considered when the heater was placed continuously or discretely at different locations along the annulus’ boundaries. The governing equations were derived from the Navier–Stokes equations along with the angular momentum equation of microrotation. The flow domain, bounded between two dissimilar geometrical surfaces, was transformed into a computational domain. The modeled set of equations was solved using an in-house developed MATLAB program code based on the finite difference method with the succesive over relaxation, succesive under relaxation, and Gauss–Seidel iteration techniques. The impacts of the Hartmann number, Rayleigh number, volume fraction of nanoparticles, and vortex viscosity parameter on the streamlines, isotherms, average Nusselt number, average Bejan number, and entropy generation number were computed to analyze the flow dynamics and convective heat transfer mechanism. The average Nusselt number increased linearly with ϕhnf, higher for the inner elliptic cylinder. As K0 rises, heat convection declines. In contrast to Cases II and I, Cases III and IV exhibit a greater attenuation of heat convection at the inner elliptical cylinder. The Nuo declines rapidly for Cases I and III compared to Cases II and IV. Increasing the concentration of nanoparticles improved heat convection. Both Nui and Nuo increase linearly with ϕhnf, but the rise is more pronounced from the inner elliptical cylinder than the outer square cylinder. It is found that Cases II and III have the highest and lowest Beavg values, while Cases III and I have the highest and lowest Ns values. Beavg diminishes and the total entropy generation Ns increases with Ha, Ra, and ϕhnf, while reverse effect of vortex viscosity Ko.
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Abbreviations
- CVFEM:
-
Control volume finite element method
- EG:
-
Entropy generation
- EGM:
-
Entropy generation minimization
- FDM:
-
Finite difference method
- MFs:
-
Micropolar fluids
- MHD:
-
Magnetohydrodynamic
- SOR:
-
Successive over relaxation
- SUR:
-
Successive under relaxation
- B 0 :
-
Strength of the magnetic field
- Be:
-
Bejan number
- C p :
-
Specific heat at constant pressure (J kg–1 K–1)
- g :
-
Gravitational acceleration (m s–2)
- H :
-
Cavity size (m)
- Ha:
-
Hartmann number
- j :
-
Micro-inertial density (m–2)
- k :
-
Thermal conductivity (W m–1 K–1)
- K o :
-
Dimensionless vortex viscosity
- \(\overline{n}\) :
-
Microrotation vector (s–1)
- N :
-
Dimensionless microrotation vector
- N s :
-
Total entropy generation number
- Nu:
-
Average Nusselt number
- NuL :
-
Local Nusselt number
- p :
-
Pressure (Pa)
- P :
-
Non-dimensional pressure
- Pr:
-
Prandtl number
- r i :
-
Parameter for inner elliptic cylinder
- r o :
-
Parameter for outer square cylinder
- Ra:
-
Rayleigh number
- S gen :
-
Local total entropy generation
- S lht :
-
Local entropy generation due to heat transfer
- S lff :
-
Local entropy generation due to fluid flow
- S lHa :
-
Local entropy generation due to magnetic field
- T :
-
Temperature (K)
- u, v :
-
Velocity along x, y-axis (m s–1)
- U, V :
-
Non-dimensional velocity along x- and y- axis
- x, y :
-
Dimensional Cartesian coordinates (m)
- X, Y :
-
Non-dimensional Cartesian coordinates
- α :
-
Heat diffusivity (m2 s–1)
- β :
-
Heat expansion coefficient (K–1)
- γ :
-
Spin-gradient viscosity
- θ :
-
Dimensionless temperature
- κ :
-
Vortex viscosity (kg m–1 s–1)
- μ :
-
Dynamic viscosity (kg m–1 s–1)
- ν :
-
Kinematic viscosity (m2 s–1)
- ρ :
-
Density (kg m–3)
- σ :
-
Electrical conductivity (Ω–1 m–1)
- Φ:
-
Irreversibility parameter
- ϕ :
-
Nanoparticles volume fraction
- ϕ 1 :
-
Volume fraction of Ag
- ϕ 2 :
-
Volume fraction of Al2O3
- χ :
-
Material parameter
- ψ :
-
Dimensionless stream function
- ω :
-
Dimensionless vorticity
- ξ, η :
-
Computational plane axis
- Ag:
-
Silver nanoparticles
- Al2O3 :
-
Aluminum oxide
- avg:
-
Average
- c :
-
Cooled
- f :
-
Base fluid
- hnf :
-
Hybrid nanofluid
- h :
-
Heated
- i :
-
Inner elliptic cylinder
- l :
-
Local
- o :
-
Outer square cylinder
- ξ, η :
-
Derivative w.r.t. ξ, η
- *:
-
Parameters for computational domain
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Acknowledgements
Anil Ahlawat is thankful to the Council of Scientific & Industrial Research (CSIR), New Delhi for SRF, Letter No. 09/752(0073)/2017-EMR-I.
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Appendix-A (for reviewer’s response, not to include in publication)
Appendix-A (for reviewer’s response, not to include in publication)
The governing Eqs. (1)–(4) with corresponding boundary conditions in physical domain are solved numerically by using Gauss–Seidel method followed by successive over-relaxation and successive under-relaxation techniques. The current investigation takes place within a fluid flow domain that is confined by two dissimilar geometric surfaces. As a result, it was not possible to generate a rectangular grid directly over the annulus. Hence, it is suitable to use a body-fitted coordinate system (BFCS) for transforming the whole set of governing equations into curvilinear coordinates (ξ, η), which will be the computational domain for the problem. Therefore, for this particular geometry, the following defined transforming function is used
Here \(r_{{\text{i}}} = b_{{\text{i}}} \left[ {\left( {\frac{{b_{{\text{i}}} }}{{a_{{\text{i}}} }}} \right)^{2} \sin^{2} \left( {2\pi \xi } \right) + \cos^{2} \left( {2\pi \xi } \right)} \right]^{ - 0.5}\) and \(r_{0} = \left[ {\cos^{200} \left( {2\pi \xi } \right) + \sin^{200} \left( {2\pi \xi } \right)} \right]^{ - 0.005}\). Where ai and bi are the lengths of semi-major and semi-minor axes of inner elliptic cross section, respectively. Applying these transformations as mentioned in Roy [35], the first-order derivatives become like as follows:
, where \(J = \frac{\partial y}{{\partial \eta }}\frac{\partial x}{{\partial \xi }} - \frac{\partial y}{{\partial \xi }}\frac{\partial x}{{\partial \eta }}\).
By using the transformation given in Roy [35], the physical region of the problem was changed into a computational domain bounded in the region, 0 ≤ ξ ≤ 1 and 0 ≤ η ≤ 1 and now the orthogonal grids are possible. Equations (1)–(4) in computational domain can be written as given in Eqs. (23)–(26) along with the boundary conditions given in Eqs. (27)–(31). The diffusion and convection terms in Eqs. (23)–(31) were discretized employing the second-order central and upwind difference schemes, respectively, and then in-house MATLAB codes are designed for the computation of ψ, ω, N and θ from the system of discretized equations. Convergence criteria for ψ, ω, N and θ are given by \(\frac{{\sum\nolimits_{{{\text{ij}}}} {\left| {\Phi_{{{\text{ij}}}}^\text{k + 1} - \Phi_{{{\text{ij}}}}^\text{k} } \right|} }}{{\sum\nolimits_{{{\text{ij}}}} {\left| {\Phi_{{{\text{ij}}}}^\text{k + 1} } \right|} }} \le 10^{ - 6}\), where Φ demonstrates any of the computed magnitudes of ψ, ω, N and θ.
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Ahlawat, A., Sharma, M.K., Rashidi, M.M. et al. Entropy production minimization and heat transfer enhancement in a cavity filled with micropolar hybrid nanofluid under an influence of discrete heaters and uniform magnetic field. J Therm Anal Calorim 148, 10803–10820 (2023). https://doi.org/10.1007/s10973-023-12415-7
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DOI: https://doi.org/10.1007/s10973-023-12415-7