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Dittus–Boelter Convection

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Nusselt number (and film coefficient h) for turbulent pipe flow: Nu = 0.023·Re^0.8·Pr^n (n = 0.4 heating, 0.3 cooling).

Formula

$$ Nu = 0.023 \cdot Re^{0.8} \cdot Pr^n, \quad h = \frac{Nu \cdot k}{D_h} $$

Symbol legend

SymbolMeaningUnitSource
$Re$Reynolds number-fluid flow
$Pr$Prandtl number = ν/α-fluid property
$k$Thermal conductivityW/(m·K)fluid table
$D_h$Hydraulic diametermgeometry
$h$Convective film coefficientW/(m²·K)result

Sources

  • Dittus-Boelter (1930).