Here we will consider a 2D square cavity with a steady-state natural convection, for which a highly-accurate numerical solution has been proposed in Ref. 7 and used as a benchmark for about 40 computer codes in Ref. 8, besides it well agrees with the semi-empirical formula proposed in Ref. 10 for rectangular cavities. This cavity's configuration and imposed boundary conditions, as well as the used coordinate system, are presented in Figure 1. Here, the left and right vertical walls are held at the constant temperatures of T1 = 305 K and T2 = 295 K, accordingly, whereas the upper and bottom walls are adiabatic. The cavity is filled with air.

The square cavity's side dimension, L, is varied within the range of 0.0111...0.111 m in order to vary the cavity's Rayleigh number within the range of 103…106. Rayleigh number describes the characteristics of the natural convection inside the cavity and is defined as follows:

where
is
the volume expansion coefficient of air,
g is the gravitational acceleration,
Cp is the air's specific heat at constant pressure,
ΔT = T1 – T2 = 10 K is the temperature difference between the walls,
k is the thermal conductivity of air,
μ is the dynamic viscosity of air.
The cavity's model is shown in Figure 2.

Due to gravity and different temperatures of the cavity's vertical walls, a steady-state natural convection flow (vortex) with a vertical temperature stratification forms inside the cavity. The Ra = 105 flow's prediction performed with Flow Simulation is shown in Figure 3.

A quantitative comparison
of the Flow
Simulation predictions
performed at result resolution level 8 with Ref. 7, Ref. 8 (computational
benchmark) and Ref. 10 (semi-empirical
formula) for different Ra values
is presented in Figure 4 - Figure 6. The Nusselt
number averaged over the cavity's hot vertical wall (evidently,
the same value must be obtained over the cavity's cold vertical
wall)
, where qw,av is
the heat flux from the wall to the fluid, averaged over the wall,
is considered in Figure 4.
Here, the dash line presents the Ref. 10 semi-empirical formula:
,
where D is the distance between the vertical walls and L is the cavity height (D = L in the case under consideration). One can see that the Flow Simulation predictions practically coincide with the benchmark at Ra ≤ 105 and are close to the semi-empirical data.

The dimensionless
velocities of the natural convection flow in the X and Y directions,
and
(which
are maximum along the cavity's mid-planes, i.e.,
along
the vertical mid-plane and
along
the horizontal mid-plane) are considered in Figure 5. The dimensionless
coordinates,
and
,
of these maximums' locations (i.e.,
for
and
for
) are presented in Figure 6. One can
see that the Flow
Simulation predictions
of the natural convection flow's local parameters are fairly close
to the benchmark data at Ra ≤ 105.

