Heat transfer coefficient convection cable—gas

Symbol
$h_{conv,og}$
Unit
W/(K.m$^2$)
Formulas
$\frac{k_{gas} \mathrm{Nu}_{og}}{L_{d}}$general case (Hartlein & Black)
$\frac{k_{gas} \mathrm{Nu}_{og}}{\delta_{d}}$Riser open at both ends, 133 ≤ $Ra$ ≤ 7000 (Hartlein & Black IIa)
$\frac{k_{gas} \mathrm{Nu}_{og}}{\delta_{d}}$Riser closed at both ends (Anders)
$\frac{\left(0.46\frac{D_{di}}{D_{o}}+0.54\right) k_{gas} \mathrm{Nu}_{og}}{\delta_{d}}$Riser open at both ends (Anders)
$\frac{k_{gas} \mathrm{Nu}_{og}}{L_{d}}$Riser open at top and closed at bottom (Anders)
Related
$D_{o}$
$\delta_{d}$
$k_{gas}$
$L_{d}$
$\mathrm{Nu}_{og}$