Rayleigh-Bénard Convection
Rayleigh-Bénard convection describes the flow in a liquid that is heated from below. Since we use a nondimensional formulation, temperatures $T_A$ and $T_B$ are only used when rescaling back to dimensional quantities.
Governing Equations
In a domain of dimensions $L \times B \times D$, the governing equations for Rayleigh-Bénard convection are given by
with boundary conditions
where $T_A$ is the temperature of the gas just above the interface. See Symbols for the definition of all quantities used here.
Nondimensional formulation
In TransiFlow, we implement the following nondimensionalized equations
with boundary conditions
Here $x$, $y$ and $z$ are scaled by $D$, and hence $A_x = L / D$ and $A_y = B / D$. The other quantities are scaled using $u = \hat u \nu / D$, $t = \hat t D^2 / \nu$, $p = \hat p (\mu \nu / D^2) - \rho_0 g z$, $T = (T_B - T_A) \hat T + T_A$ and additionally $\hat u = \tilde u \mathrm{Gr}^{1/2}$, $\hat t = \tilde t \mathrm{Gr}^{-1/2}$, $\hat p = \tilde p \mathrm{Gr}$, $\hat T = \tilde T$. Moreover, the Prandtl number is given by $\mathrm{Pr} = \nu / \kappa_T$, the Rayleigh number by $\mathrm{Ra} = (\alpha_T g \Delta T D^3) / (\nu \kappa_T)$, the Grashof number by $\mathrm{Gr} = \mathrm{Ra} / \mathrm{Pr}$ and the Biot number is given by $\mathrm{Bi} = h D / k$. All other quantities are defined in Symbols.
Perturbation formulation
Alternatively, we can also look at the perturbation from the motionless solution
which is less prone to numerical errors. This results in the following nondimensional formulation
with boundary conditions
Parameters
These are the relevant parameters in the parameters dictionary for this problem type.
Parameter name |
Default value |
Notes |
|---|---|---|
|
Set to
'Rayleigh-Benard' or'Rayleigh-Benard Perturbation' |
|
|
1.0 |
Unused if Gr is defined |
|
1.0 |
|
|
Ra / Pr |
Overrides Ra if defined |
|
0.0 |
|
|
0.0 |
Used to switch branches |