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Fig. 5 Nondimensional radial velocity of the warm buoyant jet as a function of Rayleigh number
in the double logarithmic scale
Table 2 Overview of the experimental parameters for nonrotating case. The radius of the tank
R
¼
0
:
3 m and the slope angle
a ¼
39 is the same for all experiments
B (m 3 /s 3 )
Type of markers
q (Wt/m)
10 9
6.37
ð
3
:
12
3
:
13
Þ
13.1
10 9
ð
6
:
4
6
:
6
Þ
25.7
ð 1 : 2 1 : 3 Þ 10 8
4.2 Nonrotating Case
In the nonrotating case, the external dimensional parameters are the same as
described in Sect. 4.1 , excepting the Coriolis parameter (it is absent). Results of
laboratory experiments have shown that the radial propagation velocity of the jet
U ~ B 1/2 and that it is independent of time; k T and
are nearly constant. Therefore,
the main dimensionless parameter is (flux) Rayleigh number, Ra B ¼
n
BH 3
2
,
where B is the buoyancy flux (m 3 /s 3 ); H the vertical length scale (m); k T the thermal
diffusivity (m 2 /s);
=k
T n
the viscosity (m 2 /s).
By analogy with Eq. 3 in Sect. 4.1 , we should parameterize the velocity of the
buoyant jet as follows:
n
U
B 1 = 3
Ra 1 = 2
(5)
Thus, the formula for velocity jet is obtained in the final form:
1 = 2
B 1 = 3 H 3
k T n
U
(6)
The results are presented in log-log scale in Fig. 5 , which includes the data of
all experimental runs in nonrotating case (Table 2 ). The solid line in Fig. 5 is the
best fit of the predicted law ( 5 ) to the all-laboratory experiments with the high
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