Concept reference
The Darcy friction factor packages wall shear into a dimensionless multiplier. On a Moody chart, laminar flow follows one line, turbulent flow depends on both Reynolds number and relative roughness, and the high-Reynolds fully rough region flattens because viscosity no longer controls the wall-scale loss.
Relative roughness is ε/D. In turbulent flow the Colebrook-White relation is 1/√f = −2 log10[ε/(3.7D) + 2.51/(Re√f)]. It is implicit in Darcy f; explicit approximations are convenient only within their documented validation ranges.
A single “typical f” can be adequate for a rough estimate but is not a property of pipe material alone. Reading the chart with absolute roughness instead of ε/D, or extending a turbulent fit into transition, produces a precise-looking unsupported result.
Physics sets the relationships; the owner, manufacturer and governing local standard set the project criteria.