 | - mass fraction concentration [-] |
 | - mean skin friction coefficient over the turbulent area of [-] |
 | - mean drag resistance coefficient in the REV [-] |
 | - mean form resistance coefficient in the REV [-] |
 | - mean skin friction coefficient on the REV laminar region [-] |
 | - drag resistance coefficient upon single sphere [-] |
 | - specific heat [J/(kgK)] |
 | - interface differential area in porous medium [m2] |
 | - character pore size in the cross section [m] |
 | - molecular diffusion coefficient [m2/s] |
 | - capillary morphology characteristic pore diameter [m] |
 | - diameter [m] of i-th pore [m] |
 | - mean diameter of medium's pores [m] |
 | - particle diameter [m] |
 | -porous medium Euler number [-] |
 | -Fanning friction factor [-] |
 | -gravitational constant [m2/s] |
 | - pore scale microroughness layer thickness [m] |
 | - internal surface in the REV [m2] |
 | - permeability [m2] |
 | - turbulent diffusion coefficient [m2/s] |
 | - analytic longitudinal diffusion coefficient [m2/s] |
 | - absorption equilibrium constant [-] |
 | - turbulent eddy viscosity [m2/s] |
 | - porous medium general scale [m] |
 | - averaged porosity [-] |
 | - number of pores [-] |
 | - number of pores with diameter of type i [-] |
 | - pressure [Pa] |
 | - ={U}f Lpor/D , porous medium Peclet number [-] |
 | - particle radius Peclet number [-] |
 | - , Prandtl number [-] |
 | - ={U}f Lpor/ , porous medium Reynolds number [-] |
 | - ={U}f dm / , mean Reynolds number based on mean pore diameter [-] |
 | - cross sectional flow area [m2] |
 | - source or sink in diffusion equation [s-1] |
 | - total cross sectional area available to flow [m2] |
 | - projected obstacle area on the cross perpendicular pore surface [m2] |
 | - specific surface of a porous medium [1/m] |
 | - = [1/m] |
 | - cross flow projected area of obstacles [m2] |
 | - time interval for averaging of turbulent variable [s] |
 | - velocity fluctuation [m/s] |
 | - dimensionless porous medium interstitial velocity [-] |
 | - characteristic velocity in porous medium, equals to laminar regime velocity in dh tube, [m/s] |
 | - square friction velocity at the upper boundary hr of averaged over surface [m2/s2] |
 | - averaged mass transfer coefficient over [m/s] |
 | - heat transfer coefficient in control volume [W/(m2K)] |
 | - averaged heat transfer coefficient over [W/(m2K)] |
 | - mean heat transfer coefficient across the layer [W/(m2K)] |
 | - = , characteristic heat transfer coefficient in the layer [W/(m2K)] |
 | - volumetric thermal expansion coefficient [1/K] |
 | - smooth wall boundary layer thickness [m] |
 | - representative elementary volume (REV) [m3] |
 | - turbulence dissipation rate [m2/s3] |
 | - Darcy friction coefficient in tubes [-] |
 | - dynamic viscosity [kg/(m s)] or [Pa s] |
 | - kinematic viscosity [m2/s] |
 | - density [kg/m3] |
 | - turbulent dissipation rate coefficient exchange ratio [-] |
 | - porous medium turbulent kinetic energy coefficient exchange ratio [-] |
 | - conventional turbulent kinetic energy coefficient exchange ratio [-] |
 | - porous medium fluid non-local temperature turbulent coefficient exchange ratio [-] |
 | - turbulent friction stress tensor [kg/(m s2)] |
 | - wall shear stress [N/m2] |
 | - roughness element slope angle [°] |
 | - scalar field variable [-] |