| Nomenclature |
|
g
|
gravitational acceleration, [m/s2] |
|
q′″ |
heat source, [W/m3] |
|
d
|
diameter of cylinder, [m] |
|
A
|
surface area, [m2] |
|
K
|
permeability of cylinder, [m2] |
|
kf
|
thermal conductivity of fluid, [W/(m·°C)] |
|
ke
|
effective thermal conductivity, [W/(m·°C)] |
|
Rc
|
thermal conductivity ratio |
|
h
|
heat transfer coefficient, [W/(m2·°C)] |
|
x
|
dimensional horizontal coordinate, [m] |
|
y
|
dimensional vertical coordinate, [m] |
|
u
|
dimensional x-component velocity, [m/s] |
| v |
dimensional y-component velocity, [m/s] |
|
p
|
pressure, [Pa] |
|
T*
|
temperature, [°C] |
|
X
|
dimensionless horizontal coordinate |
|
Y
|
dimensionless vertical coordinate |
|
U
|
dimensionless x-component velocity |
|
V
|
dimensionless y-component velocity |
|
P
|
dimensionless pressure |
|
T
|
dimensionless temperature |
|
Lw
|
the wake length |
|
Lp
|
the penetration depth |
|
Re
|
Reynolds number |
|
Pr
|
Prandtl number |
|
Gr
|
Grashof number |
|
Ri
|
Richardson number |
|
Da
|
Darcy number |
|
Nu
|
Nusselt number |
|
Er
|
enhancement ratio |
|
n
|
the dimensionless normal direction |
| Greek symbols |
|
α
|
thermal diffusivity, [m2/s] |
|
β
|
thermal expansion coefficient, [°C−1] |
| υ |
fluid kinematic viscosity, [m2/s] |
|
ε
|
fluid kinematic viscosity porosity |
|
ρ
|
fluid density, [kg/m3] |
| δ |
the thickness of the thermal boundary layer |
|
|
a binary constant |
| Subscripts |
| ∞ |
free stream |
|
ave
|
average |