| - 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 [-] |