We
examine the effectiveness of forced convective heat transfer
in a toroidal helical pipe (THP), as a compact process intensification
device for use in heat exchangers. Earlier, we showed that mixing
was enhanced significantly in such devices due to a continuously changing
curvature along the length of the pipe while retaining its compactness.
In this work, we examine six Reynolds numbers ranging from 1 to 200,
two Prandtl numbers (1 and 7), and two thermal boundary conditions
(fixed temperature and fixed flux). The heat transfer efficiency in
THP is quantified mainly by the Nusselt number as a function of the
downstream distance, and it is compared with that in straight pipes
of identical setup. Thus, enhancement by the geometric factor alone
is extracted. We found in THP that the Nusselt number is not monotonic
but varies periodically around mean values that can be more than four
times higher than straight pipes. The unique coupled-Dean vortex flow
pattern, due to the varying curvature of the THP axis, significantly
enhances the in-plane mixing and causes the higher and oscillatory
Nusselt numbers.