Flotation rates of fine, spherical particles or droplets by a spherica
l, rising bubble or drop have been computed for conditions relevant to
microflotation. The buoyancy-driven motion of the rising drop (or bub
ble) is characterized by small Reynolds, and large Peclet numbers. Par
ticular attention is given to suspended droplets (or particles) much s
maller than the rising drop; dilute conditions are assumed. Two comple
mentary regimes are considered: (1) convective capture dominated by th
e buoyancy-driven, relative motion between a collecting drop and small
er, dispersed droplets, and (2) capture dominated by diffusive transpo
rt of small droplets within a boundary layer on the surface of a large
r collecting drop. The first regime is relevant for the flotation of m
icron-size and larger droplets; the second is relevant for submicron s
izes. A scaling analysis reveals three distinct mechanisms for droplet
capture by a larger rising drop. According to the scaling analysis, f
lotation rates depend strongly on the size of the dispersed droplets,
the size of the collecting drops, and the mobility of the collecting d
rop interface; a bubble with a free surface is a more efficient collec
tor than a viscous drop, and a collector with an interface immobilized
by surfactant is least efficient. The scaling analysis predicts that
flotation rates depend weakly on the strength of van der Waals forces,
and are insensitive to the viscosity or density of the dispersed drop
lets; flotation rates of droplets and particles are very similar. The
scaling predictions are illustrated by dimensionless flotation rates c
omputed by a trajectory analysis in regime (1), and by mass transport
formulae for regime (2). Detailed pairwise, hydrodynamic and van der W
aals interactions are incorporated into the analysis of the first regi
me, but not the second where they are shown to be unimportant by scali
ng arguments. The droplet size that is most difficult to float and its
flotation rate are predicted by scaling and estimated numerically.