aso | Diffusivity of the ground (m2/s) | Te | Inlet temperature of the fluid in the inner tube (K) |
af | Diffusivity of the fluid (m2/s) | Tm | Mean temperature of the fluid in annular space at z and ( K) |
DH | Hydraulic diameter, DH = 2(Ri − rex). (m) | Tu | Temperature of the exchanger wall at z and t (K) |
G | Green’s function | T0 | Initial temperature field in the soil t = 0 (K) |
h | Local heat transfer coefficient at the wall (Wm−2/K) | u | Radial velocity (m/s) |
kf | Thermal conductivity of the fluid. (Wm−1/K) | v | Orthoradial velocity (m/s) |
ks | Thermal conductivity of the ground (Wm−1/K) | w | Axial velocity in annular space (m/s) |
L | Length of the exchanger. (m) | u0 | Average velocity of fluid in the annularspace (m/s) |
| Vector-position in the space | z | Axial coordinate (m) |
| Vector-position in the space where the temperature is evaluated | Greek | Symbols |
Re | Reynolds number, Re = W0DHρf/μ, dimensionless | δ | Time step (s) |
rex | Radius of the central tube. (m) | Φ | Heat flux density (W/m2) |
Ri | Radius of the exchanger (m) | ν | f cinematic viscosity of the fluid (m2/s) |
t | Time (s) | ρf | Fluid density (kg/m3) |