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(a)
(b)
VIa
VIb
Ib
II
4
5
a
b
c
d
A
Ia
Ib
VIa
V
VIIa
Ib
2
II
0
0
-2
-5
0.1
0.2
0.3 0.4
Prandtl number Pr
0.5
0.6
0.7
2
4
6 8
Prandtl number Pr
10
12
Figure 2.2. Results for the (m 1 , m 2 ) = ( 3, 2 ) mode interaction point. Computed values of the normal form coefficients a , b , c ,
and d and A = ad
bc are shown as a function of the Prandtl number Pr. (a) Results for Pr between 0.025 and 0.7 and (b) results
for Pr between 0.7 and 13, where at Pr = 0.025 the parameters correspond to those of mercury, at Pr = 0.7 to those of air, and
at Pr = 13 to those of a water-glycerol mixture. In order to ensure that the values of ν and κ correspond to those of these fluids
at the given Prandtl number, it is necessary to change the magnitude of the incrementation of ν and κ as the Prandtl number is
varied; discontinuous changes in the incrementation result in kinks in the graphs of b , c ,and A . Vertical lines indicate transitions
between qualitatively different dynamics that are labeled according to the case numbers of Guckenheimer and Holmes [1983].
(a)
(b)
VIa
VIb
4
5
a
b
c
d
A
Ia
II
V
VIIa
Ib
III
II′
2
VIIa
0
0
-2
-5
0.1
0.2
0.3 0.4
Prandtl number Pr
0.5
0.6
0.7
2
4
6
8
10
12
Prandtl number Pr
Figure 2.3. Results for the (m 1 , m 2 ) = ( 4, 3 ) mode interaction point. See caption of Figure 2.2 for description.
(a)
(b)
VIb
II
Ia
VIIb
VIa
2
b
d
A
4
Ia
Ib′
VIIa
II
2
0
0
-2
-2
-4
-4
0.1
0.2
0.3 0.4
Prandtl number Pr
0.5
0.6
0.7
2
4
6
Prandtl number Pr
8
10
12
Figure 2.4. Results for the (m 1 , m 2 ) = ( 5, 4 ) mode interaction point. See caption of Figure 2.2 for description.
 
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