functionNu_Turbulent_Local_Developed

Nusselt Number | Single phase | Turbulent | Local | Internal | Fully Developed

Information

Local heat transfer model for fully developed laminar and turbulent flow in circular pipes.

  • The laminar region has been shown to be significantly impacted by the duct shape and wall boundary conditions but not the surface roughness.
  • The turbulent region has been shown to be highly depenedent of surface roughness but not impacted by duct shape or wall boundary conditions.
  • The characteristic dimension is defined as dimension = 4*crossArea/perimeter where "crossArea" is the cross sectional flow area and "perimeter" is the wetted perimeter.

Range of validity:

  • fully developed pipe flow
  • forced convection
  • one phase Newtonian fluid
  • 2300 ≤ Re ≤ 1e6, 0.1 ≤ Pr ≤ 1000, d/L ≤ 1
  • Turbulent region is independent of pipe shape.

References

  1. VDI Heat Atlas 2E, 2010.
  2. Heat Transfer. Nellis and Klein. 2009

Inputs

TypeNameDefaultDescription
SI.ReynoldsNumberReReynolds Number
SI.PrandtlNumberPrPrandtl Number
SI.LengthxPosition of local heat transfer calculation
SI.LengthdimensionCharacteristic dimension (e.g., hydraulic diameter)
SI.Heightroughness2.5e-5Average height of surface asperities

Outputs

TypeNameDefaultDescription
SI.NusseltNumberNuNusselt number