The steady axisymmetric flow in and around a deformable drop moving
under the action of gravity along the axis of a vertical tube at intermediate
Reynolds number is
studied by solving the nonlinear free-boundary problem using a Galerkin
finite-element method. For the case where the drop and suspending liquid
have the
same viscosity, the ratio of the densities is 6/5 or 5/6, and the
radius of the tube is equal to
twice the radius of a sphere having the drop volume, four significant results
are
apparent in the computations. First, we compute drops showing much more
deformation, and in particular the development of considerably more non-convexity,
than those found in previous calculations for non-zero Reynolds number.
The degree
of non-convexity typically grows with the Reynolds number. Secondly, external
recirculation zones can be attached to or disjoint from the drop. We find
when there
is a single external recirculation zone, that is disjoint (as found by
Dandy
& Leal), it
can attach to the drop as the Reynolds number is increased. As the Reynolds
number
further increases, this is immediately followed by division of the drop
into two
adjacent recirculating regions. Thirdly, we sometimes find two recirculation
zones
in the suspending liquid. Finally, the drag coefficient, axis ratio, and
normalized
interfacial and frontal areas of the drop can vary non-monotonically with
the Weber
number, exhibiting as many as four local extrema. The results are compared
to
previous theoretical and experimental work, and implications for drop motion
and
heat and mass transfer are discussed.