Shanghai University
Article Information
- SUN Chuanshi, LIU Shuang, WANG Qi, WAN Zhenhua, SUN Dejun
- Bifurcations in penetrative Rayleigh-Bénard convection in a cylindrical container
- Applied Mathematics and Mechanics (English Edition), 2019, 40(5): 695-704.
- http://dx.doi.org/10.1007/s10483-019-2474-6
Article History
- Received Jul. 29, 2018
- Revised Oct. 19, 2018
θm, density inversion parameter; | a, aspect ratio; |
Ra, Rayleigh number; | θ, dimensionless temperature; |
Pr, Prandtl number; | t, dimensionless time; |
T, temperature; | u, dimensionless velocity. |
m, wave number; |
Penetrative convection refers to the phenomena whenever the convection in a thermally unstable fluid layer penetrates into the adjacent stable layers. It is commonly known to happen in many geophysical and astrophysical flows[1]. Typical stellar convection zones are bounded by stably stratified regions, and the fluid motions in the convection zones can penetrate into these stably stratified regions, leading to momentum transport and internal gravity waves. It is also found that the zonal flow in Jupiter's atmosphere originates from the penetrative convection taking place in the deep hydrogen-helium interior[2]. Although Earth's liquid core is unstable to convect, and generates a magnetic field[3], the outermost part of Earth's core may be stably stratified[4]. Thus, a detailed study of penetrative convection is necessary for the understanding of convection in many stars and planets.
The fact that water has a maximum density at Tm=4℃ makes it well suited to study penetrative convection. Consider a Rayleigh-Bénard convection (RBC)[5-6] system using water as the working fluid, in which the temperature of the bottom plate is higher than Tm while the temperature of the top plate is lower than Tm. The fluid in the lower layer above 4℃ is convectively unstable, while the upper layer below 4℃ is gravitationally stable. When the Rayleigh number Ra of the unstable layer exceeds a critical value, the convection will happen and may penetrate into the upper stably stratified region.
The first important work on the subject of penetrative convection was performed in a layer of water, in which the bottom boundary was maintained at 0℃ and the top boundary was kept at a temperature higher than 4℃[1]. Thus, a gravitationally unstable fluid layer lies below a layer which is stably stratified. For the convection onset, a stable finite amplitude solution and an unstable small amplitude solution are observed. The convective instability can take place at a finite amplitude, and the convection is stable at the values of Ra less than the critical value of the infinitesimal stability theory. Moore and Weiss[7] used numerical simulations to extend the finite amplitude solution of penetrative convection to higher Ra, and gave a model explaining the finite amplitude instability with the consideration of the distortion of the mean temperature. Large and Andereck[8] experimentally studied the onset and pattern formation in the penetrative RBC in water near 4℃, and confirmed the subcritical behavior. Due to the symmetric breaking, two different arrangements of hexagonal convection cells were observed. Hu et al.[9] investigated the RBC of cold water near 4℃ in a cubical cavity with different thermal boundary conditions on the sidewalls. They found that there were multiple flow pattern coexistence and hysteresis phenomena during the flow pattern transition.
The above works are all performed in two-dimensional (2D) or three-dimensional (3D) rectangular containers. In recent years, the penetrative RBC in cylindrical containers has attracted much attention. Li et al.[10-11] investigated the pattern formation of the RBC of cold water near 4℃ in a vertical cylindrical container. They showed that the critical Rayleigh number Rac increased with the increase in θm for the convection onset. Hu et al.[12] investigated the aspect ratio dependence of the penetrative RBC in vertical cylindrical containers. Their results showed that the aspect ratio had a great effect on the flow patterns, and the number of rolls increased with the increase in the aspect ratio. More recently, Huang et al.[13] studied the turbulent RBC of cold water near 4℃ in a vertical cylindrical container, and proposed the power law scalings between the average Nusselt number and Ra for different θm.
In the previous works, the subcritical behavior of finite amplitude solutions was observed in penetrative RBC. However, it is known that the axisymmetric convection occurs through supercritical pitchfork bifurcation within the Oberbeck-Boussinesq (OB) approximation[14]. There are two kinds of axisymmetric convection with upward and downward flows at the center for a cylindrical cell. These two kinds of axisymmetric convection possess the same stability characteristics since they are conjugate to each other within the OB approximation[15-16]. In the penetrative RBC, these two solutions are different, and also have distinctive bifurcation processes due to the symmetry breaking. However, few works are devoted to the bifurcations of finite amplitude solutions in the cylindrical penetrative RBC. The effect of θm on the stability of axisymmetric solutions is still unclear. In this paper, the onset of penetrative convection is studied, and the relationship of θm and Rac is investigated. More importantly, the bifurcation processes based on the axisymmetric solutions are investigated in detail. Besides, particular attention is paid to showing the differences between the stability of the two axisymmetric solutions by diagrams.
2 Problem formulationThe problem is sketched in Fig. 1. The aspect ratio is defined as a=R/H. In the cylindrical coordinates, the domain is (r, φ, z)∈ [0, a]× [0, 2π]× [0, 1]. The cylinder is heated from the bottom with a temperature Th, and cooled from the top with a temperature Tc. It should be noted that Th>Tc. The side wall is adiabatic. All the boundaries of the container are rigid. All the material properties remain constant except for the density in the buoyancy term. The temperature-dependent density of cold water is given by Gebhart and Mollendorf[17] as follows:
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(1) |
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Fig. 1 Sketch of the cylindrical container with the radius R and the height H |
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where
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H, H2/ν, ν/H, and ρ (ν/H)2 are used as the length, time, velocity, and pressure scales, respectively, where ν is the viscosity coefficient. The dimensionless temperature is defined as θ=(T-Tc)/(Th-Tc). The dimensionless governing equations can be written as follows:
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(2) |
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(3) |
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(4) |
The dimensionless parameters controlling this problem are the Prandtl number Pr=ν/κ, the Rayleigh number Ra=(gγ(Th-Tc)q H3)/(νκ), and the density inversion parameter θm=(Tm-Tc)/(Th-Tc), where κ is the thermal diffusivity, and g denotes the acceleration due to gravity. Here, Pr is fixed at 11.57.
The boundary conditions for the temperature and velocity can be expressed as follows:
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(5) |
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(6) |
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(7) |
The temperature distribution is θ(z)=1-z for the motionless conductive state.
3 Numerical methodAn improved fractional-step method is used to solve the governing equations in 3D cylindrical coordinates with the second-order accuracy in time and space. This method is an improved version of the algorithm of Verzicco and Orlandi[18], in which an additional pressure predictor[19] is carried out at each time step. The results show that the improved method is more robust than the original version, especially for the Newton method.
In the linear stability analysis (LSA), the Jacobian-free Newton-Krylov method[20] is used to obtain both the stable and unstable solutions. A first-order implicit/explicit Euler scheme is used to calculate the Stokes pre-conditioner, which is the matrix-free inversion of the preconditioned Jacobian for each Newton iteration[21]. The BICGSTAB algorithm[22] is used to solve the corresponding linear system, which is free from constructing the Jacobian matrix.
The linear stability equation for the infinitesimal perturbations u ' of a steady state u is
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(8) |
Thus, the eigenvalues λiof the matrix (Nu + L) control the linear stability of the steady state u:
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(9) |
For a given basic flow, we use the Arnoldi algorithm[23] to calculate the leading eigenvalues. A small matrix is constructed by time stepping the linearized equations, which represents the action of the Jacobian matrix on the subspace of the leading eigenvectors. The leading eigenvalues and eigenvectors are obtained by the diagonalization of the small matrix.
These methods have been proven to be effective in our previous works[15, 24]. Furthermore, the current numerical results with density inversion are also in good agreement with the results of Hu et al.[12] and Li et al.[10-11] (see Tables 1 and 2). Most of our simulations are performed with grids of 90×60×60 in the azimuthal, radial, and vertical directions, respectively.
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In the present system, the flow is quiescent at the conductive state at low Ra. When Ra increases above a critical value, the flow will bifurcate into the convective state. In a cylindrical container, the flow patterns at the convective state can be characterized by the azimuthal wave number m. The Rac and the corresponding m of the convection onset depend on the aspect ratio a and the density inversion parameter θm.
4.1 Effects of the density inversion parameter on convection onsetBy the LSA, the convection onset is studied with 0.66≤ a≤ 2. Figure 2 shows the stability curves of the convection onset. At θm=0, the Rac and the critical wave numbers are similar to those under the OB approximation[24]. The results also show that the critical wave numbers of the convection onset are affected by θm.
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Fig. 2 Critical Rayleigh numbers as functions of the aspect ratio a for different density inversion parameters θm |
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Figure 3 shows the normalized Rac for a=0.66, 1.1, and 2 and θm=0.4, 0.45, and 0.5. The normalizations are carried out by using the corresponding values at θm=0. It is seen that twelve different aspect ratios of each θm are uniformly distributed between 0.66 and 2. This indicates that, with different aspect ratios, the normalized Rac fluctuates within a limited range. Although the values of the normalized Rac fluctuate, no significant difference is found in the normalized Rac when 0.66≤ a≤ 2. The three curves in Fig. 3 are for the normalized Rac at a=0.66, 1.1, and 2. It is clear that all the three curves almost coincide with each other. This indicates that, the normalized Rac is strongly affected by θm, while the aspect ratio has a minor effect on the normalized Rac. In the parameter range of our study, the Rac of the convection onset increases when θm increases, and it increases more rapidly when θm>0.4.
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Fig. 3 Normalized critical Rayleigh numbers Rac(θm)/Rac(0) for selected aspect ratios a and density inversion parameters θm |
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It is obvious that the stably stratified fluid layer will become thicker when θm increases, and the stably stratified fluid layer will suppress the convection onset of the lower unstable fluid layer. Therefore, the flow is more stable at higher θm. Supposing that there is an effective Rayleigh number
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(10) |
Now, consider the effective depth of the unstable fluid layer in the conductive solution. We note that, the convection in the unstable fluid layer will penetrate into the upper stably stratified fluid layer, and there is a penetrative depth in the penetrative RBC. We account for this effect by introducing a coefficient f in the following expression with the effective height of the convection layer:
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(11) |
The coefficient f of the penetrative depth is a function of θm and f ≥ 1. When θm=0, we have f=1, due to the restriction of the upper boundary on the penetrative depth. When θm increases, the stably stratified layer becomes thicker, and the influence of the upper boundary becomes weaker. We expect that f tends to be constant for large enough θm.
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(12) |
Without the consideration of the effect of side walls, the critical
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(13) |
Thus, the relationship between θm and Rac can be written as follows:
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(14) |
Figure 4 shows the normalized critical Rayleigh numbers as a function of 1-θm for a=0.66, 1.1, and 2. The dashed lines in Fig. 4 denote the predicted normalized Rac based on Eq. (14) with f=1.5. The specific mathematical expression is
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(15) |
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Fig. 4 Normalized critical Rayleigh number Rac(θm)/Rac(0) as a function of 1-θm for a=0.66, 1.1, and 2 |
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The results show that the normalized Rac distributes around the dashed lines when 1-θm < 0.6, while it tends to 1 when 1-θm>0.6. When 1-θm increases, the upper boundary will restrict the depth of the penetrative convection. Therefore, the normalized Rac tends to 1 when 1-θm increases to 1.
4.2 Bifurcations of the axisymmetric solutionsIt is found that the conductive solution bifurcates to convective axisymmetric flow at a=1 when θm is from 0 to 0.5. Via the DNS with different initial conditions, we find that there are still two kinds of steady axisymmetric solutions for all considered θm with the central fluid moving upward (A) and downward (B), respectively, although the top-bottom symmetry is broken for the present system. The coexistence of the solutions A and B is observed in a certain range of Ra above the threshold of the first bifurcation. Figure 5 shows the typical temperature fields of the solutions A and B at Ra=3 800 and θm=0.2. Different from the prior results within the OB approximation, the stability properties of the two solutions are rather different due to the symmetry breaking. Moreover, when Ra increases, the bifurcation processes and flow patterns after the onset are also quite different.
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Fig. 5 Temperature fields of the axisymmetric solutions at Ra=3~800 and θm=0.2 (color online) |
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Using the solutions A and B as the initial conditions, we first calculate Rac by gradually decreasing Ra in the DNS. Figure 6 shows the Rac of the solutions A and B for the first bifurcation. It is obvious that the Rac of the solution A is close to that of the solution B for small θm, but their difference becomes more evident when θm increases. For instance, at θm=0, the Rac of the solution A is 2 189, while it is 2 206 for the solution B. However, at θm=0.5, Rac is 15 878 for the solution A, while it is increased up to 18 829 for the solution B.
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Fig. 6 Comparison between the critical Ra numbers of the solutions A and B for different θm |
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Figure 7 shows the bifurcation diagram near the threshold of the first bifurcation based on the vertical velocities of the monitoring point (φ=0, r=0.5, z=0.5) at θm=0.35. Different from the previous results in the penetrative convection, the coexistence of solutions with a small stable amplitude and a finite amplitude is observed, and the conductive solution bifurcates to the solution B with a small stable amplitude instead of the solution A with a finite amplitude when Ra increases. It is clearly shown that the values of | uz | of the solutions A and B are not equal. Within the OB approximation, it has already been found that the two kinds of axisymmetric solutions appear through a supercritical pitchfork bifurcation due to the top-bottom symmetry, which are conjugate to each other. However, in the penetrative RBC, the onset of the axisymmetric convective solutions will occur through a trans-critical bifurcation, due to the fact that the top-bottom symmetry is broken because of the non-linear density and temperature relationship.
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Fig. 7 Bifurcation diagram for uz as functions of Ra at θm=0.35, where the solid curves correspond to the stable state, while the dashed curves correspond to the unstable state |
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We now turn to study the stability properties of the axisymmetric solutions. Figure 8 shows the pattern evolutions of the solutions A and B after the convection onset. The stability curves are calculated by the LSA with either decreasing or increasing Ra. The base flows for Figs. 8(a) and 8(b) are the solutions A and B, respectively. The results of the stability analysis show that the bifurcations of both the axisymmetric solutions to the 3D convection are stationary. In Fig. 8(a), it is shown that a stable region of the solution A (AS) is bounded by two stability curves. Taking the solution A in the AS region as the base flow, the decrease in Ra will result in a conductive state, while, when Ra increases, the solution A will bifurcate into the steady 3D convection. In Fig. 8(b), a region of the stable solution B is non-existent (NE), and two stable regions (AS) and two unstable regions (AU) of the solution B are separated by four stability curves. Resembling the prior work within the OB approximation for low Pr[16], we here find a stable region of the solution B beyond the secondary bifurcation at Pr = 11.57.
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Fig. 8 Stability curves of the axisymmetric solutions, where AS indicates the region in which the solution A or B is stable, AU means the region in which the axisymmetric solution is unstable, and NE means the region in which the solution A (stable solution B) is non-existent |
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From Fig. 8, we can also find that, when θm increases, the values of Rac of both the solutions increase rapidly, and θm will affect the azimuthal wave number m. Moreover, the effect of θm on the pattern evolutions of the solution A is considerably different from that of the solution B. Specifically, the Rac of the solution B is more sensitive to the increase in θm than that of the solution A. For instance, the Rac of the solution A is 21 226 at θm=0 and 38 328 at θm=0.5, but the highest Rac of the solution B is 13 858 at θm=0 and 142 395 at θm=0.5.
In addition, the critical m of the solution A is more sensitive to the change in θm. When θm changes from 0 to 0.5, the critical m of the solution A changes from 1 to 4, to 3, and then to 1 sequentially. While for the solution B, the critical m of the secondary bifurcation remains to be 2 until θm reaches 0.5, and then becomes 3. In the stable region of the solution B beyond the secondary bifurcation, when θm changes from 0 to 0.5, the critical m is 1 when Ra increases, while is 2 when Ra decreases.
The existence of multiple active patterns can lead to complicated nonlinear flow evolutions. At Ra=37 000 and θm=0.4, the flow transition process from the solution A obtained by the DNS is shown in Fig. 9(a), where the time series of the azimuthal velocity of a monitoring point (φ=0, r=0.5, z=0.5) is given. For this parameter combination, the solution A is unstable, and the m=3 mode grows in the amplitude and saturates due to the nonlinear effect. This is consistent with the results of the LSA, which shows that the most unstable mode of the solution A is of the azimuthal wave number m=3 for θm=0.4. The saturated m=3 pattern is actually unstable, and will further transit to a m=2 pattern as time goes on. The typical flow structures appearing in this transition process are shown in Figs. 9(b), 9(c), and 9(d).
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Fig. 9 Time evolution from the A solution at Ra=37 000, θm=0.4 and contours of uz in the horizontal midplane, where the solid curves correspond to positive values, while the dashed curves correspond to negative values |
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In summary, the bifurcation processes are studied in detail by the LSA and DNS in the penetrative RBC for cold water near its maximum density in the cylindrical containers at 0.66≤ a≤ 2.0 and 0≤ θm≤ 0.8. For the convection onset, Rac increases with the increase in θm, and it increases more rapidly when θm>0.4. The effect of the aspect ratio on the normalized Rac is limited in the parameter range of our study. Furthermore, the relationship between θm and the normalized Rac is formulated as follows:
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which is in good agreement with the results of the LSA when θm>0.4.
In such a top-bottom symmetry breaking system, we still identify two kinds of qualitatively different steady axisymmetric solutions beyond the first bifurcation. The onset of the axisymmetric convection occurs through a trans-critical bifurcation rather than the supercritical pitchfork bifurcation within the OB approximation. Moreover, the subcritical behavior is observed for the solution A, while is absent for the solution B. Interestingly, we find that the pattern evolution based on the solution A is considerably different from that of the solution B, and a stable region of the solution B beyond the secondary bifurcation is identified at Pr=11.57. Furthermore, the Rac of the solution B is more sensitive to the increase in θm than that of the solution A, while the critical m of the solution A is more sensitive to the variation of θm than that of the solution B.
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