New exact differential models for fully developed turbulent flow and convec
tion were solved numerically for both uniformly heated and isothermal round
tubes for a wide range of the Reynolds number and a complete range of the
Prandtl number. These models are expressed directly in terms of the local t
ime-averaged turbulent shear stress and heal flux density, and utilize a th
eoretically based algebraic correlating equation for the former and a purel
y empirical one for the latter rather than the customary heuristic differen
tial models involving the eddy diffusivities. The predicted rates of heat t
ransfer were found to be relatively insensitive to the particular empirical
expressions utilized for the turbulent Prandtl number, which is the only s
ignificant source of uncertainty. The predicted Nusselt numbers are closely
represented by a single, simple, generic correlating equation that is free
of any explicit empiricism and is directly applicable for all geometries a
nd all thermal boundary conditions. (C) 2001 Elsevier Science Ltd. All righ
ts reserved.