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Natural Convection Heat Transfer Calculator
Heat Transfer
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Geometry & Fluid Conditions
Geometry
Vertical Plate (Churchill-Chu)
Horizontal Plate (Top Surface Heated)
Horizontal Plate (Bottom Surface Heated)
Horizontal Cylinder
Characteristic Length L
0.30 m
0.01 m
3 m
Temperature Difference ΔT = T_s − T_f
50 °C
−100°C
300°C
Fluid
Air (20°C)
Air (100°C)
Water (20°C)
Water (60°C)
Custom
ρ (kg/m³)
1.204
μ (×10&supmin;&sup5; Pa·s)
1.825
k (W/mK)
0.026
Pr
0.71
β (×10&supmin;³ K&supmin;¹)
3.41
$Ra = g\beta\Delta T L^3/(\nu\alpha)$
Churchill-Chu (Vertical Plate):
$Nu = [0.825 + 0.387 Ra^{1/6} / \Psi]^2$
$\Psi = (1+(0.492/Pr)^{9/16})^{8/27}$
$h = Nu \cdot k / L$
—
Rayleigh Number Ra
—
Nusselt Number Nu
—
h (W/m²K)
—
q″ (W/m²)
h vs ΔT
Nu vs Ra (Log-Log)
Boundary Layer Temperature Profile (Schematic)