This paper presents a numerical study of the transient developing laminar f
low of a Newtonian incompressible fluid in a straight horizontal pipe oscil
lating around the vertical diameter at its entrance. The flow field is infl
uenced by the tangential and Coriolis forces, which depend on the through-f
low Reynolds number, the oscillation Reynolds number and the angular amplit
ude of the pipe oscillation. The impulsive start of the latter generates a
transient pulsating flow, whose duration increases with axial distance. In
any cross-section, this flow consists of a pair of symmetrical counter-rota
ting vortices, which are alternatively clockwise and anti-clockwise. The ci
rcumferentially averaged friction factor and the axial pressure gradient fl
uctuate with time and are always larger than the corresponding values for a
stationary pipe. On the other hand, local axial velocities and local wall
shear stress can be smaller than the corresponding stationary pipe values d
uring some part of the pipe oscillation. The fluctuation amplitude of these
local variables increases with axial distance and can be as high as 50% of
the corresponding stationary pipe value, even at short distances from the
pipe entrance. Eventually, the flow field reaches a periodic regime that de
pends only on the axial position. The results show that the transient flow
field depends on the pipe oscillation pattern (initial position and/or dire
ction of initial movement). Copyright (C) 2000 John Wiley & Sons, Ltd.