In this study the geometry of the LHRE's cooling passage was simplified
and the symmetrical flow was assumed. A 24x16x20 grid (Fig.
1) was generated in quarter of the flow domain by using a grid generation
method.
The governing equation were non-dimensionalized
by using the following definitions of non-dimensional variables:
The boundary conditions was given as follows. On the walls, all components
of the velocity was zaro and the temperature was given by the measurements.
On the symmetry plans,
According to the known value of the relative parameters, the Rayleigh
number was estimated with the value of about 107. In the calculation,
four cases with the Rayleigh number of 106, 107,
2x107 and 3x107 was selected. The Prandtl number
was set to a constant value of 0.71.
Fig.2 shows the velocity vectors in two curved surfaces
and a section plane at Ra=107. The strong three dimensional
flow can be seen from the figure. In the region near the cylinder wall
(J=1), the fluid moves upward and in the region near the other wall
(J=16), the fluid moves downwards. So the larger scale circulation was
formed. Four circulations was also visible in the flow domain. Two
of them was in the upper region and near the symmetry planes and the fluid
in the region close to the sections I=12 and I=13 moved toward the cylinder
wall. At the region near the top wall, the fluid near I=12 and I=13 sections
moved toward the corner of the cylinder.
Similar flow pattern was gotten at the selected Rayleigh number, but the magnitude of the velocity shown in the figure with a vector increased with the Rayleigh number.
Fig. 3 shows the isotherms in the flatten section
of J=9, at different Rayleigh number. The distinct difference of the temperature
distribution among the them can be seen from the figure. It is obvious
that the flow pattern in the selection in the selected section affected
the temperature distribution in same section. Large velocity corresponded
to the higher value of temperature at the same position in the cross section
plane.
Fig. 4 presents the contours of the local Nusselt
number on the cylinder wall at different Rayleigh number. The local Nusselt
number is defined as
The locally large heat transfer rate was in the bottom region and the
minimum was in the top region. In the region near the symmetry, the heat
transfer rate takes about average value.
Overall heat transfer results are presented in terms of average Nusselt
number, which is defined as:
Where A is the area of the quarter of the cylinder line. The average
Nusselt numbers at different Rayleigh numbers are presented in table
1. The heat transfer rate increased with the Rayleigh. Which was the
direst result of the larger circulation at the higher Raylergh number.
Table 1 Average Nusselt numbers at different Rayleigh number
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