Heat or mass transport due to forced convection is characterised by a relation of the form
${\textit{Nu}} = {\mathcal F}({\textit{Pe}})$. The Nusselt number,
${\textit{Nu}}$, is the non-dimensional heat or mass (scalar) transport rate and
${\textit{Pe}} = Ua/D$, the Péclet number, is a dimensionless parameter measuring the relative importance of convection and diffusion. Here,
$a$ is the characteristic size of the particle or drop,
$D$ the scalar diffusivity and
$U$ an appropriate velocity scale;
${\textit{Nu}}$ is defined to be unity in the absence of a flow (
${\textit{Pe}} = 0$). We attempt to understand the nature of the
${\textit{Nu}}{-}{\textit{Pe}}$ relationships that arise for scalar transport from suspended particles and drops. For the simple case of an ambient uniform flow convecting the scalar, a scenario that arises for a particle or drop translating relative to an otherwise quiescent ambient,
${\mathcal F}({\textit{Pe}})$ transitions from unity, to eventually increasing as a power of Pe, for large Pe. The large-Pe exponent is 1/3 for particles and 1/2 for drops, and is directly related to the thickness of the scalar boundary layer that develops on the particle (drop) surface at large Pe. Our main focus is on transport from neutrally buoyant particles and drops in linear shearing flows, in which case
$U=\dot {\gamma }a$,
$\dot {\gamma }$ being the ambient shear rate. Although Pe remains an important parameter, Nu now depends sensitively on the geometry of the linear flow. The latter determines the near-surface flow that, in turn, controls the nature of the boundary-layer-enhanced transport for large Pe. The topology of the near-surface streamlines or pathlines can vary widely, depending on ambient flow-type, leading to a variety of transport scenarios. Understanding the Nu–Pe relationships across this wide range is crucial to understanding transport in more complicated situations, including particles (drops) in turbulence.