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Heat transfer in laminar flow in a uniformly porous channel with an applied transverse magnetic field
Authors:G M Shrestha
Institution:(1) Department of Mathematics, University, Dundee, Scotland, UK;(2) Present address: Dept. of Mathematics, Florida State Un., Tallahassee, Fla., USA
Abstract:Summary The steady laminar flow of an incompressible, viscous, and electrically conducting fluid between two parallel porous plates with equal permeability has been discussed by Terrill and Shrestha 6]. In this paper, using the solution of 6] for the velocity field, the heat transfer problems of (i) uniform wall temperature and (ii) uniform heat flux at wall are solved.For small suction Reynolds numbers we find that the Nusselt number, with increasing Reynolds number, increases for case (i) and decreases for (ii).Nomenclature psgr stream function - 2h channel width - x, y distances measured parallel, perpendicular to the channel walls - U velocity of fluid in the x direction at x=0 - V constant velocity of suction at the wall - lambda nondimensional distance, y/h - xgr nondimensional distance, x/h - f(lambda) function defined in (1) - rgr density - ngr coefficient of kinematic viscosity - R suction Reynolds number, V h/ngr - Re channel Reynolds number, 4U h/ngr - B 0 magnetic induction - sgr electrical conductivity - M Hartmann number, B 0 h(sgr/rgrngr)1/2 - K constant defined in (3) - A constant defined in (5) - beta 4R/Re - q local heat flux per unit area at the wall - k thermal conductivity - T temperature of the fluid - X –1/beta ln(1–betaxgr) - C p specific heat at constant pressure - j current density - Pr Prandtl number, mgrC p/k - P mass transfer Péclet number, R Pr - Pe mass transfer Péclet number, P/beta - T 0 temperature at x=0 - T H(lambda) temperature in the fully developed region - T h(X, lambda) temperature in the entrance region - Y n (lambda) eigenfunctions, uniform wall temperature - gamma n eigenvalues - e(lambda) function defined by (24) - B n 2/3gamma n 2 - A n constants defined by (28) - aprime 2m constants defined by (30) - F n (lambda) eigenfunctions, uniform wall heat flux - a n , b n , c n , d n , e n constants defined by (45) and (48) - S a parameter, mgrU 2/q - h 1 heat transfer coefficient - T m mean temperature - Nu Nusselt number - Nu T Nusselt number, uniform wall temperature - Nu q Nusselt number, uniform wall heat flux
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