functionNu_Laminar_Local_Developed_Circular
Nusselt Number | Single phase | Laminar | Local | Circular | 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
- constant wall temperature or constant heat flux in laminar region
- 0 ≤ Re ≤ ~2300, 0.1 ≤ Pr ≤ 1000, d/L ≤ 1
- Applies only to circular pipes in the laminar region but can approximate other shapes with the characteristic dimension.
- Laminar region is independent of surface roughness
References
- VDI Heat Atlas 2E, 2010.
Inputs
| Type | Name | Default | Description |
|---|---|---|---|
| SI.ReynoldsNumber | Re | Reynolds Number | |
| SI.PrandtlNumber | Pr | Prandtl Number | |
| SI.Length | x | Position of local heat transfer calculation | |
| SI.Length | dimension | Characteristic dimension (e.g., hydraulic diameter) | |
| Boolean | constantTwall | true | = true for constant wall temperature correlation else constant heat flux |
Outputs
| Type | Name | Default | Description |
|---|---|---|---|
| SI.NusseltNumber | Nu | Nusselt number |