12 – 2D Thermal Convection (Non-Dimensional)

This exercise revisits 2-D thermal convection in a fully non-dimensional framework. You will define characteristic scaling constants, transform the governing equations into dimensionless form, and investigate how the resulting flow depends on the Rayleigh number. The model assumes an isoviscous rheology, bottom heating, and the Boussinesq approximation.

Objectives

  1. Define physically motivated scaling constants and apply the corresponding scaling relations to the governing equations.
  2. Formulate the dimensionless energy, momentum, and mass conservation equations, including the buoyancy term $Ra\,T'$.
  3. Implement Dirichlet and Neumann thermal boundary conditions and free-slip velocity boundary conditions.
  4. Solve the coupled system of advection, diffusion, momentum, and mass conservation using finite-difference methods and the available GeoModBox.jl solvers.
  5. Run and compare models for $Ra=10^4$, $10^5$, and $10^6$, and examine changes in plume and downwelling scales and overall flow vigor.
  6. Compute diagnostic quantities such as the surface Nusselt number and RMS velocity, and assess the approach to statistical steady state.

As the Rayleigh number increases:

  • the characteristic flow velocities increase,
  • convection becomes more vigorous, and
  • thermal plumes and downwellings become narrower and more localized.

The grid resolution must therefore be adjusted accordingly to maintain numerical stability and solution accuracy.

A finer grid, however, also substantially increases the computational cost.

The resolution prescribed here is sufficient for the investigated Rayleigh numbers. Nevertheless, some numerical methods already show noticeable inaccuracies at this resolution, indicating that a finer grid would provide a more accurate solution.

12a

Figure 1. Isoviscous, bottom-heated thermal convection for $Ra=10^6$ with a resolution of $150\times50$ cells. The initial condition consists of a temperature profile that increases linearly with depth, with a small elliptical thermal perturbation superimposed on the background field. The top and bottom temperatures are fixed, while zero heat flux is prescribed along the lateral boundaries. All velocity boundaries are free slip. Heat diffusion is solved using a Crank–Nicolson discretization, the Stokes equations using the defect-correction method, and temperature advection using the semi-Lagrangian method. The model is run until statistical steady state is reached or for a maximum of 8000 iterations.

12b

Figure 2. Evolution of the surface Nusselt number and root mean square (RMS) velocity. These quantities describe the efficiency of heat transport and the overall vigor of convection. Details of their calculation are provided in the exercise.

12c

Figure 3. Evolution of the relative variation in RMS velocity with numerical iteration. The variation is evaluated over a moving window of $3.8\times10^{-3}$ non-dimensional time units. A relative tolerance of $10^{-4}$ is used to identify statistical steady state. Low-$Ra$ models typically reach statistical steady state within fewer than 3000 iterations.