An experimental study is performed for the development of the mean vel
ocity field of swirling turbulent flows in straight pipes with a smoot
h wall. Swirl intensities were selected in a range that can be expecte
d to occur in large piping systems. Measurements were taken for two di
fferent Reynolds numbers, and two widely different initial conditions.
Although the swirl intensity can best be expressed by the axial flow
of angular momentum, a representation by a single swirl angle seems to
be satisfactory for the final decay process. While the difference bet
ween the initial conditions persists during a considerable part of the
decay process, the decay rates are not essentially different. The rat
e of decay appears to vary with the Reynolds number in the same way as
the friction factor does. (C) 1998 Elsevier Science Ltd. All rights r
eserved.