
8.4 High Rayleigh Number Convection 489
Fig. 8.2 Schematic
representation of boundary
layer convection
10
−6
m
2
s
−1
, and for these values, the Rayleigh number is about 0.85 ×10
8
. Thus
the Rayleigh number is much larger than the critical value, and as a consequence we
can expect the convection to be vigorous (if velocities of centimetres per year can
be said to be vigorous).
There are various intuitive ways in which we can get a sense of the likely be-
haviour of the convective solutions of the Boussinesq equations when R 1. Since
R multiplies the buoyancy term, any O(1) lateral temperature gradient will cause
enormous velocities (this is best seen in (8.26) rather than (8.12)). One might thus
expect the flow to organise itself so that either horizontal temperature gradients are
small, or they are confined to thin regions, or both. Since O(1) temperature varia-
tions are enforced by the boundary conditions, the latter is more plausible, and thus
we have the idea of the thermal plume, a localised upwelling of hot fluid which will
be instantly familiar to glider pilots and seabirds.
A mathematically intuitive way of inferring the same behaviour follows from
the expectation that increasing R drives increasing velocities; then large R should
imply large velocity, and the conduction term in the heat equation u.∇T =∇
2
T is
correspondingly small. Since the conduction term represents the highest derivative
in the equation, its neglect would imply a reduction of order, and correspondingly we
would expect thermal boundary layers to exist at the boundaries of the convecting
cell. This is in fact what we will find: a hot thermal boundary layer adjoins the
lower boundary, and a cold one adjoins the upper boundary, and a rapid circulation
in the interior of the cell detaches these as upwelling and downwelling plumes. The
general structure of the resulting flow is shown in Fig. 8.2. We analyse this structure
in the following sections.