An application of numerical bifurcation analysis
Greg Lewis
University of Ontario Institute of Technology (UOIT)
with Bill Langford (Guelph) and Wayne Nagata (UBC)
BIRS, August 8, 2007
BIRS – p.1/48
An application of numerical bifurcation analysis Greg Lewis - - PowerPoint PPT Presentation
An application of numerical bifurcation analysis Greg Lewis University of Ontario Institute of Technology (UOIT) with Bill Langford (Guelph) and Wayne Nagata (UBC) BIRS, August 8, 2007 BIRS p.1/48 Outline Introduction The
BIRS, August 8, 2007
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b
a
b a
y r x φ z
Ω
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South Pole North Pole
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b
a
b a
y r x φ z
Ω
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lower symmetric vacillation irregular steady waves upper symmetric knee
log(Thermal Rossby number) log(Taylor number)
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lower symmetric vacillation irregular steady waves upper symmetric knee
log(Thermal Rossby number) log(Taylor number)
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1
^
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α G(x, ) = 0
α 0 α
α 1
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0 ,
0 ] is the tangent to the solution curve
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α G(x, ) = 0
t 2 t 1
α 0 α
α 1
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b
a
b a
y r x φ z
Ω
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lower symmetric vacillation irregular steady waves upper symmetric knee
log(Thermal Rossby number) log(Taylor number)
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10
5
10
6
10
7
10
8
10
−3
10
−2
10
−1
10
Taylor number thermal Rossby number
(3,4) (4,5) (5,6) (6,7) (7,8) (8,7) (7,6) (6,5) theoretical transition curve theoretical critical wave number transitions experimental transition curve experimental critical wave number transitions
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10
5
10
6
10
7
10
8
10
−3
10
−2
10
−1
10 Taylor number thermal Rossby number (3,4) (4,5) (5,6) (6,7) (7,8) (8,7) (7,6) (6,5) theoretical transition curve theoretical critical wave number transitions boundaries of region of bistability
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0.5 1 1.5 1.5 2 2.5 3 3.5 4 4.5
θ T T = T0 T = T0 − ∆ T cos(2 θ) pole equator
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r0 R
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x y stream function 1 2 0.5 1 1.5 2 x y azimuthal fluid velocity
1 2 0.5 1 1.5 2 x y temperature deviation
1 2 0.5 1 1.5 2
Bristol 05 – p.10/24
x y stream function 1 2 0.5 1 1.5 2 x y azimuthal fluid velocity
1 2 0.5 1 1.5 2 x y temperature deviation
1 2 0.5 1 1.5 2
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x y stream function 1 2 0.5 1 1.5 2 x y azimuthal fluid velocity
1 2 0.5 1 1.5 2 x y temperature deviation
1 2 0.5 1 1.5 2
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x y stream function 1 2 0.5 1 1.5 2 x y azimuthal fluid velocity
1 2 0.5 1 1.5 2 x y temperature deviation
1 2 0.5 1 1.5 2
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x y stream function 1 2 0.5 1 1.5 2 x y azimuthal fluid velocity
1 2 0.5 1 1.5 2 x y temperature deviation
1 2 0.5 1 1.5 2
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0.01 0.0125 0.015 0.0175 0.02 −9.7 −9.6 x 10
−5
Eigenvalue with largest real part ∆ T max real(λ)
0.01 0.0125 0.015 0.0175 0.02 3 4 5 6 x 10
−3
Continuation of steady solution 1−cell 2−cell ∆ T || ξ ||2
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x y stream function 1 2 0.5 1 1.5 2 x y azimuthal fluid velocity
1 2 0.5 1 1.5 2 x y temperature deviation
1 2 0.5 1 1.5 2
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x y stream function 1 2 0.5 1 1.5 2 x y azimuthal fluid velocity
1 2 0.5 1 1.5 2 x y temperature deviation
1 2 0.5 1 1.5 2
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0.0107 0.0108 0.0109 −10 −5 x 10
−8
Eigenvalue with largest real part ∆ T max real(λ)
0.0107 0.0108 0.0109 1 1.5 x 10
−3
Continuation of steady solution 1−cell 2−cell ∆ T || ξ ||2
DEDS: Pattern Formation – p.27/35
∆T ∆T ∆T
small η η = η0 large η
HP SN SN
Dynamics Day – p.28/35
∆T
η
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0.
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