Combined Free and Forced Convection in Porous Media

1971 ◽  
Vol 11 (04) ◽  
pp. 399-405 ◽  
Author(s):  
Michel A. Combarnous ◽  
Paul Bia

Abstract An experimental study of thermal convection in a horizontal porous layer bounded by isothermal planes has been performed with and without a mean flow of the saturating fluid phase. The temperature distribution and heat transfer resulting from convection have been determined. The theoretical criterion for the onset of convection (Rayleigh number NRa > 4p2) has been verified. For low values of NRa (< 260) a regular pattern of convective cells has been observed which may be motionless or moving depending on the experimental conditions. For NRa values higher than 260, another convective state has been found that is mainly unstable. Numerical computations have been worked out that confirm the experimental results on the heat transfer and size of convective cells. INTRODUCTION Thermal convective currents may exist in a porous medium when the vertical component of the temperature gradient runs in the same direction as the gravity vector. Such a configuration is possible in some cases during a real in-situ combustion test4 or during hot fluid injection. A general understanding of convection is also of interest for analyzing the abnormal temperature gradients sometimes observed in oil and gas reservoirs.22 From the phenomenological standpoint a distinction must be made between the natural or free convection occurring in a closed volume and the mixed or combined free and forced convection arising when there is a mean flow of the fluid phase. Natural convection in porous media has been the subject of numerous experimental attempts to determine a convection criterion, e.g., by using a linear theory,1,2,9 and to measure the mean heat transfer.3,7 Numerical studies8,10,15,19,20 have also been made, and their results are not always in good agreement with experimental observations. However, no thorough study of mixed convection has been made except for a theoretical analysis of the convection onset criterion5 and some qualitative experimental observations.4 This paper presents some findings concerning both the natural and mixed convection of an incompressible fluid in a homogeneous horizontal porous layer bounded by two parallel impervious isothermal surfaces. The temperature for the cooler upper surface is T1 and that of the lower surface is T2=T1+?T. THEORETICAL ANALYSIS The effect of pressure on specific gravity is assumed to be negligible with regard to the effect of thermal expansion. So the relationship between density and temperature may be expressed as:Equation 1 In addition to complying with equations for motion and continuity, velocity and temperature distributions obey the heat transfer equation:Equation 2 By taking into account the additivity property of enthalpy, M may be expressed asEquation 3 On the contrary, khR is not just a simple function of khj and khs and must be measured or calculated with different kinds of models.6

2009 ◽  
Vol 132 (1) ◽  
Author(s):  
V. V. Sobha ◽  
R. Y. Vasudeva ◽  
K. Ramakrishna ◽  
K. Hema Latha

Thermal dispersion due to local flows is significant in heat transfer with forced convection in porous media. The effects of parametrized melting (M), thermal dispersion (D), inertia (F), and mixed convection (Ra/Pe) on the velocity distribution, temperature, and Nusselt number on non-Darcy, mixed convective heat transfer from an infinite vertical plate embedded in a saturated porous medium are examined. It is observed that the Nusselt number decreases with increase in melting parameter and increases with increase in thermal dispersion.


1981 ◽  
Vol 103 (2) ◽  
pp. 242-248 ◽  
Author(s):  
Y. T. Chan ◽  
S. Banerjee

Transient multidimensional natural convection in porous media has been studied using a numerical method based on the simplified marker and cell technique with local cancellation of low order, diffusional truncation errors. The conservation equations and boundary conditions were phrased in terms of the primitive variables, velocity and temperature. Differences in temperature between the fluid and the solid matrix are considered. Heat transfer between the solid and liquid phases was modelled by representing the porous medium as an assemblage of spherical particles, and solving the conduction problem within the spheres at every time step. Nusselt numbers at walls were calculated from the temperature and velocity profiles. Numerical results for heat transfer through fluid saturated porous media heated from below are in good agreement with published experiments. Consideration of heat transfer between the solid and fluid phase leads to Nusselt numbers that vary with the thermophysical properties of the solid material, even when the Rayleigh number and fluid thermophysical properties are kept constant. This is also observed in experiments. The calculations also show convective instabilities of the right period at high Rayleigh numbers.


2018 ◽  
Vol 22 (1 Part B) ◽  
pp. 467-475 ◽  
Author(s):  
Habib-Olah Sayehvand ◽  
Sakene Yari ◽  
Parsa Basiri

Staggered arrangement is one of the common configurations in heat exchangers that make better mixing of flow and heat transfer augmentation than other arrangements. In this paper forced convection heat transfer over three isothermal circular cylinders in staggered configuration in isotropic packed bed was investigated. In this work laminar 2-D incompressible steady-state equations of momentum and energy were solved numerically by finite volume method. Simulation was done in three Reynolds numbers of 80, 120, and 200. The results indicate that, using porous medium the Nusselt number enhanced considerably for any of cylinders and it presents thin temperature contours for them. Also is shown that by increasing Reynolds number, the heat transfer increased in both channel but the growth rate of it in porous media is larger. In addition, results of simulation in porous channel show that with increasing Peclet number, heat transfer increased logarithmically.


Sign in / Sign up

Export Citation Format

Share Document