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. 2022 Aug 8;15(15):5459. doi: 10.3390/ma15155459
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
Qmax 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
ξ 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