|
ρ
s
|
Density (Kg/m3) |
|
k
s
|
Thermal conductivity (J/m·K) |
|
E
|
Modulus of elasticity (GPa) |
| σs
|
Yield strength (Mpa) |
| ν |
Poisson’s ratio |
|
t
|
heat pipe flattening thickness |
|
dp
|
copper powder particle size |
|
h
|
maximum thickness of the absorbent wick |
| ∆Pc,max
|
maximum capillary pressure of the wick |
|
σ
|
surface tension of the working liquid |
|
θ
|
contact angle of the working liquid |
|
reff
|
effective capillary radius of the wick |
| Rer
|
radial Reynolds number |
|
mv
|
mass flow rate of the steam |
|
μv
|
viscosity of the steam |
| ∆Pl
|
working liquid flow pressure drop in the wick from the condenser to the evaporator section |
| ∆Pv
|
total vapor flow pressure drop in the ultra-thin heat pipe |
| ∆Pevp
|
interface pressure drops due to vapor |
| ∆Pcon
|
interface pressure drops due to condensation |
| ∆Pg
|
gravitational pressure drop |
|
Q′max
|
capillary limit of the ultra-thin heat pipe |
|
ρv
|
vapor density |
|
rv
|
radius of the vapor space |
|
Av
|
vapor passage area |
|
hlv
|
latent heat of the liquid |
|
Leff
|
effective length of the ultra-thin heat pipe |
|
Dh
|
hydraulic diameter of the ultra-thin heat pipe |
| ∆Pw
|
flow pressure drop in the evaporator |
|
μl
,w
|
magnetic permeability |
| ∆Pbuoy,v
|
buoyancy force exerted on the water vapor by the temperature difference between the evaporating and condensing sections under gravity |
| ∆Pentrainment
|
additional pressure drop caused by the shear stress generated by the liquid-vapor counterflow at the interface of the two phases |
|
|
ratio of wetted to non-wetted surfaces at the boundary of the wick |
|
L
|
heat transfer length |
|
k
|
thermal conductivity |
|
A
|
heat transfer area |
|
Rvapor
|
thermal resistance of evaporator section |
|
R
liquidbridge
|
additional thermal resistance when liquid bridges occur in the evaporator |
|
R
1
|
radial heat conduction and thermal resistance of pipe wall of evaporation section |
|
R
2
|
radial heat conduction and thermal resistance of the wick in the evaporation section |
|
R
3
|
phase change heat transfer thermal resistance at the vapor-liquid interface in the evaporation section |
|
R
4
|
thermal resistance caused by steam axial flow heat transfer |
|
Lbridge
|
length of the liquid bridge |
|
kwall
|
thermal conductivity of the heat pipe wall |
|
d0
|
outer diameter of the heat pipe |
|
di
|
inner diameter of the heat pipe |
|
λw
|
thermal conductivity of the pipe wall |
|
L
1
|
length of the evaporation section |
|
dv
|
diameter of the vapor space inside the pipe |
|
λe
|
thermal conductivity of the wick compound |
|
R
|
vapor gas constant |
|
Tv
|
vapor temperature |
|
r
|
latent heat of vaporization |
|
p
|
vapor pressure |
|
Leq
|
effective length of the heat pipe |
|
Ti
|
central temperature of the thermal resist block |
|
λi
|
thermal conductivity thickness of the thermal resist block |