Abstract
The natural convection heat transfer within the enclosure is a classical problem by highlighting the real field applications such as electronic packaging industry, PCR-chips for DNA amplification, energy-efficient design of buildings rooms, operation and safety of nuclear reactors, convective heat transfer within boilers, furnaces and solar systems and thermal energy storage. Hence, the present study numerically investigates the flow and heat transfer characteristics within the square enclosure having the heated circular obstacle at the middle with an air of constant thermophysical properties is considered as working fluid. Also, the study continues after introducing winglets at different angles, i.e. 00, 300, 450, 600, 700 and 900. The detailed hydrodynamic and thermal boundary conditions that are required considered and mentioned. The influence of circular obstacle with and without winglets has been reported by comparing velocity and vorticity magnitude also estimating natural convection heat transfer from obstacles. The heat transfer of the enclosure is maximum when the winglet is placed at 450, because of the flow confinement provided and also allowing the fluid to interact more with the hot obstacle and carries more heat. In highest Rayleigh number, the following heat transfer enhancement has been achieved, circle-circle with winglet @ 450 = 10.58%.
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Abbreviations
- Th :
-
Hot wall temperature (K)
- Tc :
-
Cold wall temperature (K)
- L:
-
Characteristic length (m)
- G:
-
Gravitational pull (m s−2)
- d:
-
Diameter of the obstacle (m)
- Nu:
-
Nusselt number
- Ra:
-
Rayleigh number
- Cp :
-
Pressure coefficient
- \(p\) :
-
Static pressure at the point where pressure coefficient is being measured
- \(p_{\infty }\) :
-
Free stream static pressure
- \(p_{^\circ }\) :
-
Free stream stagnation pressure
- \(\rho_{\infty }\) :
-
Free stream fluid density
- \(V_{\infty }\) :
-
Free stream fluid velocity
- Cf :
-
Skin friction coefficient
- \(\tau_{\text{w}}\) :
-
Skin shear stress on the surface
- \({\uprho }\) :
-
Fluid density
- h:
-
Convective heat transfer coefficient (w K−1 m−2)
- k:
-
Thermal conductivity (w K−1 m−1)
- v:
-
Kinematic viscosity (m2 s−1)
- β:
-
Thermal expansion coefficient (K−1)
- α:
-
Thermal diffusivity (m2 s−1)
- T:
-
Surface temperature (K)
- T∞ :
-
Bulk mean temperature (K)
- U:
-
Average velocity magnitude (m s−1)
- U* :
-
Non-dimensional velocity
- W:
-
Vorticity magnitude (s−1)
- W* :
-
Non–dimensional vorticity
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Acknowledgements
We sincerely thank and appreciate the Mechanical Engineering Department SRMIST for giving us the chance to work in their facilities and letting us have access in the product development lab and computer Fluid Dynamics lab to the technology and modelling facility.
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Subhani, S., kumar, R.S. Natural Convection Heat Transfer Enhancement of Circular Obstacle within Square Enclosure. J Therm Anal Calorim 147, 4711–4729 (2022). https://doi.org/10.1007/s10973-021-10829-9
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DOI: https://doi.org/10.1007/s10973-021-10829-9