The influence of aiding and opposing buoyancy forces on forced convect
ion heal transfer in vertically oriented, externally finned pipes is s
tudied numerically. A periodically varying external heat transfer coef
ficient is used to model the finned surface. Results are presented in
terms of the streamwise variation of the fluid bulk temperature and tu
be-side Nusselt number, axially-averaged and periodically fully develo
ped Nusselt number values, and axial velocity and temperature profiles
. Average Nusselt number correlations for both constant and periodical
ly varying Blot numbers are also presented. Buoyancy induced effects a
re observed to increase with higher levels of the external heat transf
er coefficient (or fin effectiveness) and decrease with increasing int
er-fin spacing. A constant spatially averaged Blot number approximatio
n to the periodic variation is found to be satisfactory only in the pe
riodically developed regions of the flow.