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Numerical Study of Laminar Mixed Convection Heat Transfer of Power-Law Non-Newtonian Fluids in Square Enclosures by Finite Volume Method

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Numerical Study of Laminar Mixed Convection Heat Transfer of Power-Law Non-Newtonian Fluids in Square Enclosures by Finite Volume Method
International Journal of the Physical Sciences Vol. 6(33), pp. 7456 - 7470, 9 December, 2011 Available online at http://www.academicjournals.org/IJPS DOI: 10.5897/IJPS11.1092 ISSN 1992 - 1950 © 2011 Academic Journals

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Numerical study of laminar mixed convection heat transfer of power-law non-Newtonian fluids in square enclosures by finite volume method
Mohammad Reza Safaei1*, Behnam Rahmanian2 and Marjan Goodarzi3
1

Young Researchers Club and Department of Mechanical Engineering, Mashhad Branch, Islamic Azad University, Mashhad, Iran. 2 Department of Mechanical Engineering, Mashhad Branch, Islamic Azad University, Mashhad, Iran. 3 Department of Computer Engineering, Mashhad Branch, Islamic Azad University, Mashhad, Iran.
Accepted 23 October, 2011

In this study, we have numerically considered mixed convection heat transfer in a square enclosure with cold left and right walls, insulated moving upper wall and hot fixed lower wall. The governing flows of two reliable articles were initially modeled and after validating calculations, the given flow of the study was solved by finite volume method. To examine the effects of different factors, such as Prandtl, Reynolds and Rayleigh numbers on heat transfer in a square enclosure, the laminar flow of Newtonian fluids was approximated and then laminar flow of non-Newtonian fluids, such as carboxy methyl cellulose (CMC) and carboxy poly methylene (Carbopol) water solutions were studied for different Richardson numbers. It was found from the results obtained in the present study that when Ri is less than 1, governing heat transfer inside the enclosure is forced convection for non-Newtonian fluids similar to Newtonian ones. When Ri increases, the effect of forced convection is reduced and natural convection heat transfer increases. It was also found that in constant Grashof numbers, if n decreases, the dimensionless temperature increases. Also, if n is constant, any increase in Grashof



References: Basak T, Roy S, Sharma PK, Pop I (2009). Analysis of mixed convection flows within a square cavity with uniform and non-uniform heating of bottom wall. Int. J. Therm. Sci., 48(5): 891-912. Chhabra RP (2007). Bubbles, drops and particles in non-Newtonian fluids. second edition, CRC Press, Taylor & Francis Group. Demir H, Akyoldoz FT (2000). Unsteady thermal convection of a nonNewtonian fluid. Int. J. Eng. Sci., 38: 1923-1938. Goshayeshi HR, Safaei MR, Maghmoumi Y (2009). Numerical simulation of unsteady turbulent and laminar mixed convection in rectangular enclosure with hot upper moving wall by finite volume method. The 6th Int. Chem. Eng. Cong. and Exhib. (IChEC 2009), Kish Island, Iran. Kim GB, Hyun JM, Kwak HS (2003). Transient buoyant convection of a power-law non-Newtonian fluid in an enclosure. Int. J. Heat Mass Trans., 46: 3605-3617. Lamsaadi M, Naimi M, Hasnaoui M (2006). Natural convection heat transfer in shallow horizontal rectangular enclosures uniformly heated from the side and filled with non-Newtonian power law fluids, Energy Convers. Manag., 47: 2535–2551. Maghmoumi Y (2008). Numerical investigation of steady non-Newtonian flow on a flat plate. M. Sc. thesis, IAUM, Iran (in Farsi Language). Maghmoumi Y, Alavi SMA, Safaei MR (2008). Numerical analysis of steady non-newtonian flow over a flat plate. Maj. J. Mech. Eng., 4: 21-33 (in Farsi Language). Turan O, Chakraborty N, Poole RJ (2010). Laminar natural convection of Bingham fluids in a square enclosure with differentially heated sidewalls. J. Non-Newtonian Fluid Mech., 165: 901–913. Oztop HF, Dagtekin I (2004). Mixed convection in two-sided lid-drive differentially heated square cavity, Int. J. Heat Mass Trans., 47: 17611769. Patankar SV (1980). Numerical heat transfer and fluid flow. Hemisphere Washington. Safaei MR (2009). The study of turbulence mixed convection heat transfer in Newtonian and non-Newtonian fluids inside rectangular enclosures in different Richardson numbers. M. Sc. thesis, IAUM, Iran (in Farsi Language). Safaei MR, Goshayeshi HR (2010). Numerical simulation of laminar and turbulence flow of air: natural & mechanical ventilation inside a room 10th REHVA world cong. Clima 2010 Sust. Energy Use in Build., Antalya, Turkey. Turan O, Chakraborty N, Poole RJ (2010). Laminar natural convection of Bingham fluids in a square enclosure with differentially heated sidewalls. J. Non-Newtonian Fluid Mech., 165: 901–913. Conclusions In the present study, laminar mixed convection heat transfer inside a square enclosure for power-law nonNewtonian fluids like CMC and Carbopol was solved by 4 finite volume method. Grashof number is constant (10 ) and Ri changes between 0.01 to 100. Prandtl, Grashof and Reynolds numbers have been calculated in compliance with the equations of non-Newtonian fluids. Dimensionless temperature and shear stress diagrams have been illustrated for better comparison of different fluids. According to what has been considered in this study, it can be said that: 1. In Richardson numbers less than 1, the fluid behavior into the enclosures is forced convection, and the more the Richardson number, the more powerful the heat transfer by natural convection. 2. In governing natural convection, the isothermal lines are nearly symmetric and through transiting to forced convection, these lines become asymmetric. 3. In constant Gr, increase in Re causes the enhancement of the fluid recirculation power. 4. In constant Gr, non dimensional temperature increases by decreasing n.

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