Duct geometry consideration for rough and curved ducts

For fully developed flow through straight, smooth ducts, the thermal solver supports a wide range of friction factor and heat transfer correlations for different duct geometries.

Corresponding reliable correlations for rough or curved ducts do not exist for all these geometries. Indeed, the only comprehensive set of correlations is for ducts with circular cross sections (pipes). To fully extend geometry-dependent correlations to rough and curved ducts, the following approximations are made:

The coefficient for the rough duct is the coefficient for the smooth duct of the appropriate geometry times the ratio of the rough and smooth coefficients for circular geometry. i.e.,

As above, the coefficient for the curved duct is the coefficient for the straight duct of the appropriate geometry, times the ratio of the curved and straight coefficients for circular geometry.

An extra factor is also used to account for the increased length of the curved duct compared to the straight-line distance between the end nodes of the duct. i.e.,

where:

  • ϕ is the angle of the bend in degrees.
  • R is the radius of curvature of the bend.
  • L is the straight-line distance between the end nodes of the element.

The coefficients for circular geometry given above are evaluated using the hydraulic diameter of the duct.

All correlations given in sections 3 to 5 are for circular ducts. Additionally, it is approximated that the flow is fully developed.