Numerical Modelling of Non-similar Mixed Convection Heat and Species Transfer along an Inclined Solar Energy Collector Surface with Cross Diffusion Effects
Osman Anwar Bég, Ahmed Bakier, Ramachandra Prasad, Swapan Kumar Ghosh
.
DOI: 10.4236/wjm.2011.14024   PDF    HTML   XML   5,352 Downloads   11,689 Views   Citations

Abstract

An analysis is performed to study thermo-diffusion and diffusion-thermo effects on mixed convection heat and mass transfer boundary layer flow along an inclined (solar collector) plate. The resulting governing equations are transformed and then solved numerically using the local nonsimilarity method and Runge-Kutta shooting quadrature. A parametric study illustrating the influence of thermal buoyancy parameter (ζ), Prandtl number (Pr), Schmidt number (Sc), Soret number (Sr), Dufour number (Du) and concentration-to- thermal-buoyancy ratio parameter, N, on the fluid velocity, temperature and concentration profiles as well as on local skin-friction, Nusselt and Sherwood numbers is conducted. For positive inclination angle of the plate (γ = 70 degrees), flow velocity (f') is strongly increased i.e. accelerated, with thermal buoyancy force parameter (ζ), in particular closer to the plate surface; further into the boundary layer, ζ has a much reduced effect. Conversely temperature (θ) and concentration (ψ) is decreased with increasing thermal buoyancy parameter, ζ. For negative plate inclination, the flow is accelerated whereas for positive inclination it is decelerated i.e. velocity is reduced. Conversely with negative plate inclination both the temperature and concentration in the boundary layer is reduced with the opposite apparent for positive inclination. Increasing Prandtl number strongly reduces temperature in the regime whereas an increase in Schmidt number boosts temperatures with temperature overshoots near the plate surface for Sc = 3 and 5 (i.e. for Sc > 1). Concentration is reduced continuously throughout the boundary layer, however, with increasing Schmidt number. A positive increase in concentration-to-thermal-buoyancy ratio parameter, N, significantly accelerates the flow in the domain, whereas negative N causes a deceleration. A velocity overshoot is also identified for N = 20, at intermediate distance from the plate surface. Negative N (thermal and concentration buoyancy forces oppose each other) induces a slight increase in both fluid temperature and concentration, with the reverse observed for positive N (thermal and concentration buoyancy forces assisting each other). Increasing Dufour number respectively causes a rise in temperature and a decrease in concentration, whereas an increase in Soret number cools the fluid i.e. reduces temperature and enhances concentration values. In the absence of Soret and Dufour effects, positive N causes a monotonic increase in local Nusselt number, NuxRex-1/2 with ζ Cos γ, for N = -1 the local Nusselt number remains constant for all values of parameter, ζ Cos γ. Local Sherwood number, ShxRex-1/2 is boosted considerably with higher Schmidt numbers and also with positive N values. The computations in the absence of Soret and Dufour effects correlate accurately with the earlier study by Chen et al. (1980).

Share and Cite:

O. Bég, A. Bakier, R. Prasad and S. Ghosh, "Numerical Modelling of Non-similar Mixed Convection Heat and Species Transfer along an Inclined Solar Energy Collector Surface with Cross Diffusion Effects," World Journal of Mechanics, Vol. 1 No. 4, 2011, pp. 185-196. doi: 10.4236/wjm.2011.14024.

Conflicts of Interest

The authors declare no conflicts of interest.

References

[1] W. T. Kierkus, “An Analysis of Laminar Free Convection Flow and Heat Transfer about an Inclined Isothermal Plate,” International Journal of Heat and Mass Transfer, Vol. 11, No. 2, 1968, pp. 241-252. HUdoi:org/10.1016/0017-9310(68)90153-1U
[2] T. Fujii and H. Imura, “Natural-Convection Heat Transfer from a Plate with Arbitrary Inclination,” International Journal of Heat and Mass Transfer, Vol. 15, No. 4, 1972, pp. 755-764. Hdoi:org/10.1016/0017-9310(72)90118-4
[3] T. S. Chen, C. F. Yuh and A. Moustsoglou, “Combined Heat and Mass Transfer in Mixed Convection along Vertical and Inclined Plates,” International Journal of Heat and Mass Transfer, Vol. 23, No. 4, 1980, pp. 527- 537. Hdoi:org/10.1016/0017-9310(80)90094-0
[4] B. F. Armaly, T. S. Chen and N. Ramachandran, “Correlations for Laminar Mixed Convection on Vertical, Inclined and Horizontal Flat Plates with Uniform Surface Heat Flux,” International Journal of Heat and Mass Transfer, Vol. 30, No. 2, 1987, pp. 405-408. Hdoi:org/10.1016/0017-9310(87)90129-3
[5] S. L. Lee and K. Hsu, “Interaction of Surface Suction/Blowing with Buoyancy Force on Mixed Convection Flow Adjacent to an Inclined Flat Plate,” International Journal of Heat and Mass Transfer, Vol. 32, No. 10, 1989, pp. 1989-1991. Hdoi:org/10.1016/0017-9310(89)90167-1
[6] G. Wickern, “Mixed Convection from an arbitrarily Inclined Semi-Infinite Flat Plate—I. The Influence of the Inclination Angle,” International Journal of Heat and Mass Transfer, Vol. 34, No. 8, 1991, pp. 1935-1945. Hdoi:org/10.1016/0017-9310(91)90205-S
[7] W. M. Yan, and C. Y. Soong, “Convective Heat and Mass Transfer along an Inclined Heated Plate with Film Evaporation,” International Journal of Heat and Mass Transfer, Vol. 38, No. 7, 1995, pp. 1261-1269. Hdoi:org/10.1016/0017-9310(94)00241-M
[8] W. J. Sheu and M. C. Lin, “Thermal Ignition in Buoyancy-Driven Boundary Layer Flows along Inclined Hot Plates,” International Journal of Heat and Mass Transfer, Vol. 39, No. 10, 1996, pp. 2187-2190. Hdoi:org/10.1016/0017-9310(95)00283-9
[9] C. Ludwig, “Diffusion Zwichen Unfleigh Erwarmten Orten Gleich Zusammengesetz Losungen,” Sitzungbsber. Kaiser. Akad. Wiss. (Mathem.-Naturwiss. Cl.), Wien, Vol. 65, 1856, pp. 539.
[10] C. Soret, “Sur l’état d’équilibre que prend, du point de vue de sa concentration, une dissolution saline primitivement homogène, dont duex parties sort portèes à des temperatures différentes,” C. R. Arch. Sci. Phys. Natur., Genève, Vol. 2, 1879, pp. 48-61.
[11] J. Platten and J. C. Legros, “Convection in Liquids,” Springer, Berlin, 1984.
[12] A. Mojtabi and M. C. Charrier-Mojtabi, “Double-Diffusive Convection in Porous Media,” Handbook of Porous Media, Marcel Dekker, New York, 2000, pp. 559-603.
[13] O. E. Tewfik and J. W. Yang, “The Thermodynamic Coupling between Heat and Mass Transfer in Free Convection with Helium Injection,” International Journal of Heat and Mass Transfer, Vol. 6, No. 10, 1963, pp. 915-923. Hdoi:org/10.1016/0017-9310(63)90082-6
[14] E. M. Sparrow, W. J. Minkowycz and E. R. G. Eckert, “Effects of Diffusion Thermo and Thermal Diffusion on Heat Transfer, Flow and Mass Transfer for the Helium-Air Boundary Layer in Stagnation Flow,” ASME Journal of Heat Transfer, Vol. 86C, 1964, p. 508.
[15] E. M. Sparrow, C. J. Scott, R. J. Frostron and W. A. Ebert, “Experiments on the Diffusion Thermo Effect in a Binary Boundary Layer with Injection of Various Gases,” ASME Journal of Heat Transfer, Vol. 87, 1965, pp. 321-327.
[16] C. R. A. Abreu, M. F. Alfradique and A. S. Telles, “Boundary Layer Flows with Dufour and Soret Effects. I: Forced and Natural Convection,” Chemical Engineering Science, Vol. 61, No. 13, 2006, pp. 4282-4289. Hdoi:org/10.1016/j.ces.2005.10.030
[17] W. Hort, S. J. Linz and M. Lucke, “Onset of Convection In Binary Gas Mixtures: Role of the Dufour Effect,” Physical Review A, Vol. 45, No. 6, 1992, pp. 3737-3748. Hdoi:org/10.1103/PhysRevA.45.3737
[18] R. M. L. Coelho and A. Silva-Telles, “Extended Graetz Problem Accompanied by Dufour and Soret Effects,” International Journal of Heat and Mass Transfer, Vol. 45, No. 15, 2002, pp. 3101-3110. Hdoi:org/10.1016/S0017-9310(02)00043-1
[19] A. Weaver and R. Viskanta, “Natural Convection Due to Horizontal Temperature and concentration Gradients: 2- Species Interdiffusion, Soret and Dufour Effects,” International Journal of Heat and Mass Transfer, Vol. 34, No. 12, 1991, pp. 3121-3133. Hdoi:org/10.1016/0017-9310(91)90081-O
[20] N. G. Kafoussias and E. M. Williams, “Thermal-Diffu- sion and Diffusion-Thermo Effects on Mixed Free-Forced Convective and Mass Transfer Boundary Layer Flow with Temperature Dependent Viscosity,” International Journal of Engineering Science, 1995, pp. 1369-1384.
[21] M. Anghel, H. S. Takhar and I. Pop, “Dufour and Soret Effects on Free Convection Boundary Layer over a Vertical Surface Embedded in a Porous Medium,” Studia University Babes-Bolyai Mathematica, Vol. XLV, No. 4, 2000, pp. 11-21.
[22] A. Postelnicu, “Influence of Chemical Reaction on Heat and Mass Transfer by Natural Convection form Vertical Surfaces in Porous Media Considering Soret and Dufour Effects,” Heat and Mass Transfer, Vol. 43, No. 6, 2007, pp. 595-602. Hdoi:org/10.1007/s00231-006-0132-8
[23] B. O. Anwar, R. Bhargava, S. Rawat and E. Kahya, “Numerical Study of Micropolar Convective Heat and Mass Transfer in a Non-darcian Porous Regime with Soret/Dufour Diffusion Effects,” Emirates Journal of Engineering Research, Vol. 13, No. 2, 2008, pp. 51-66.
[24] B. O. Anwar, A. B. Tasveer, A. Y. Bakier and V. Prasad, “Chemically-Reacting Mixed Convective Heat and Mass Transfer along Inclined and Vertical Plates with Soret and Dufour Effects: Numerical Solutions,” International Journal of Applied Mathematics and Mechanics, Vol. 5, No. 2, 2009, pp. 39-57.
[25] O. Anwar Bég, A. Y. Bakier and V. R. Prasad, “Numerical Study of Free Convection Magnetohydrodynamic Heat and Mass Transfer from a Stretching Surface to a Saturated Porous Medium with Soret and Dufour Effects,” Computational Materials Science, Vol. 46, No. 1, 2009, pp. 57-65. Hdoi:org/10.1016/j.commatsci.2009.02.004
[26] R. Bhargava, R. Sharma and O. Anwar Bég, “Oscillatory Chemically-Reacting MHD Free Convection Heat and Mass Transfer in a Porous Medium with Soret and Dufour Effects: Finite Element Modeling,” International Journal of Applied Mathematics and Mechanics, Vol. 5, No. 6, 2009, pp. 15-37.
[27] S. Rawat and R. Bhargava, “Finite Element Study of Natural Convective Heat and Mass Transfer in a Micropolar Fluid-Saturated Porous Regime with Soret/Dufour Effects,” International Journal of Applied Mathematics and Mechanics, Vol. 5, No. 2, 2009, pp. 58-71.
[28] O. Anwar Bég, V. R. Prasad, B. Vasu, N. Bhaskar Reddy, Q. Li and R. Bhargava, “Free Convection Heat and Mass Transfer from an Isothermal Sphere to a Micropolar Regime with Soret/Dufour Effects, International Journal of Heat and Mass Transfer, Vol. 54, 2011, pp. 9-18. Hdoi:org/10.1016/j.ijheatmasstransfer.2010.10.005
[29] E. Osalusi, J. Side and R. Harris, “Thermal-Diffusion and Diffuse-Thermal Effects on Combined Heat and Mass Transfer of a Steady MHD Convective and Slip Flow Due to a Rotating Disk with Viscous Dissipation and Ohmic Heating,” International Communications in Heat Mass and Transfer, Vol. 35, No. 8, 2008, pp. 908-918. HUdoi:org/10.1016/j.icheatmasstransfer.2008.04.011U
[30] R. S. Miller, S. Palle and C. Nolan, “Effects of Soret and Dufour Diffusion on Laminar Diffusion Flames at Large Pressures,” 56th Annual Meeting of Fluid Dynamics Division, American Physical Society, Meadowlands, New Jersey, November 23-25, 2003.
[31] M. K. Partha, P. V. S. N. Murthy and G. P. Raja-Sekhar, “Soret and Dufour Effects in a Non-Darcy Porous Medium,” ASME Journal of Heat Transfer, Vol. 128, No. 6, 2006, pp. 605-610. Hdoi:org/10.1115/1.2188512H
[32] N. OKong’o and J. Bellan, “Real-Gas Effects on Mean Flow and Temporal Stability of Binary Species Mixing Layers,” AIAA Journal, Vol. 41, No. 12, 2003, pp. 2429-2443. Hdoi:org/10.2514/2.6842
[33] E. M. Sparrow, H. Quack and J. Boerner, “Local Nonsimilarity Boundary Layer Solutions,” AIAA Journal, Vol. 8, No. 11, 1970, pp. 1936-1942. Hdoi:org/10.2514/3.6029
[34] O. A. Bég, A. Y. Bakier, V. R. Prasad and S. K. Ghosh, “Nonsimilar, Laminar, Steady, Electrically-Conducting Forced Convection Liquid Metal Boundary Layer Flow with Induced Magnetic Field Effects,” International Journal of Thermal Sciences, Vol. 48, No. 8, 2009, pp. 1596-1606. Hdoi:org/10.1016/j.ijthermalsci.2008.12.007
[35] T-B. Chang, A. Mehmood, O. Anwar Bég, M. Narahari, M. N. Islam and F. Ameen, “Numerical Study of Transient Free Convective Mass Transfer in a Walters-B Viscoelastic Flow with Wall Suction,” Communications in Nonlinear Science and Numerical Simulation, Vol. 16, No. 1, 2010, pp. 216-225. Hdoi:org/10.1016/j.cnsns.2010.02.018H
[36] O. A. Bég, J. Zueco and T. B. Chang, “Numerical Analysis of Hydromagnetic Gravity-Driven Thin Film Micropolar Flow along an inclined Plane,” Chemical Engineering Communications, Vol. 198, No. 3, 2011, pp. 312-331.
[37] O. Anwar Bég and O. D. Makinde, “Viscoelastic Flow and Species Transfer in a Darcian High-Permeability Channel,” Journal of Petroleum Science and Engineering, Vol. 76, No. 3-4, 2011, pp. 93-99. Hdoi:org/10.1016/j.petrol.2011.01.008
[38] M. M. Rashidi and O. Anwar Bég, “DTM-Padé Modeling of Natural Convective Boundary Layer Flow of a Nanofluid Past a Vertical Surface,” International Journal of Thermal and Environmental Engineering, Vol. 4, 2012, pp. 13-24.
[39] B. Gebhart, et al., “Buoyancy-Induced Flows and Transport,” Hemisphere, New York, 1988.
[40] O. Anwar Bég, J. Zueco and L. M. López-Ochoa, “Network Numerical Analysis of Optically-Thick Hydromagnetic Slip Flow from a Porous Spinning Disk with Radiation Flux, Variable Thermophysical Properties and Surface Injection Effects,” Chemical Engineering Communications, Vol. 198, No. 3, 2011, pp. 360-384.
[41] J. Zueco, P. Eguía, E. Granada, J. Míguez and O. Anwar Bég, “An Electrical Network for the Numerical Solution of Transient MHD Couette Flow of a Dusty Fluid: Effects of Variable Properties and Hall Current,” International Communications in Heat and Mass Transfer, Vol. 37, No. 10, 2010, pp. 1432-1439. Hdoi:org/10.1016/j.icheatmasstransfer.2010.07.025H
[42] M. M. Rashidi, M. Rastegari and O. Anwar Bég, “A Study of Non-Newtonian Flow and Heat Transfer over a Non-isother-mal Wedge Using the Homotopy Analysis Method,” Chemical Engineering Communications, 2011.

Copyright © 2024 by authors and Scientific Research Publishing Inc.

Creative Commons License

This work and the related PDF file are licensed under a Creative Commons Attribution 4.0 International License.