heat_transfer_pipe
Calculate convective heat-transfer coefficient for internal pipe flow using Dittus-Boelter correlation, with laminar fallback to 3.66. Input velocity and diameter to obtain Nusselt number and h.
Instructions
Convective heat-transfer coefficient for internal flow (Dittus-Boelter Nu = 0.023 Re^0.8 Pr^n; laminar Nu = 3.66). Defaults are for water. Returns Nusselt number and h (W/m^2K).
Input Schema
| Name | Required | Description | Default |
|---|---|---|---|
| density | No | ||
| heating | No | ||
| prandtl | No | ||
| diameter | Yes | ||
| velocity | Yes | ||
| conductivity | No | ||
| kinematic_viscosity | No |