Gas-Solid Fluidized Bed#

It is strongly recommended to visit DEM parameters and CFD-DEM parameters for more detailed information on the concepts and physical meaning of the parameters ind DEM and CFD-DEM.

Features#

  • Solvers: lethe-particles and lethe-fluid-particles

  • Three-dimensional problem

  • Displays the selection of models and physical properties.

  • Simulates a solid-gas fluidized bed.

Files Used in This Example#

Both files mentioned below are located in the example’s folder (examples/unresolved-cfd-dem/gas-solid-fluidized-bed).

  • Parameter file for particle generation and packing: packing-particles.prm

  • Parameter file for CFD-DEM simulation of the gas-solid fluidized bed: gas-solid-fluidized-bed.prm

Description of the Case#

This example simulates the fluidization of spherical particles in air. First, we use lethe-particles to fill the bed with particles. We enable check-pointing in order to write the DEM checkpoint files which will be used as the starting point of the CFD-DEM simulation. Then, we use the lethe-fluid-particles solver within Lethe to simulate the fluidization of the particles by initially reading the checkpoint files from the DEM simulation.

DEM Parameter File#

All parameter subsections are described in the parameter section of the documentation.

To set-up the square fluidized bed case, we first fill the bed with particles.

We first introduce the different sections of the parameter file packing-particles.prm needed to run this simulation.

Mesh#

In this example, we are simulating a squared fluidized bed that has a half length of 0.1 m, and a side of 0.04 m. We use the subdivided_hyper_rectangle GridGenerator in order to generate the mesh. The square bed is divided 40 times in the y direction. The following portion of the DEM parameter file shows the function called:

subsection mesh
  set type               = dealii
  set grid type          = subdivided_hyper_rectangle
  set grid arguments     = 1,5,1:-0.02,-0.1,-0.02:0.02,0.1,0.02:true
  set initial refinement = 3
end

Simulation Control#

Another subsection, which is generally the one we put at the top of the parameter files, is the simulation control . time step, end time, log, and output frequency are defined here. Additionally, users can specify the output folder for the simulation results in this subsection. The log frequency parameter controls the frequency at which the iteration number is printed on the terminal. If log frequency = 1000 the iteration number will be printed out every 1000 iterations. This is an easy way to monitor the progress of the simulation. A simulation time of 1 s was chosen with a time step of 0.000005. It is important to choose a long enough time as to allow all particles to come to rest. We store the output files generated in the folder output_dem:

subsection simulation control
  set time step        = 0.000005
  set time end         = 0.5
  set log frequency    = 1000
  set output frequency = 1000
  set output path      = ./output_dem/
end

Restart#

The lethe-fluid-particles solver requires reading several DEM files to start the simulation. For this, we have to write the DEM simulation information. This is done by enabling the check-pointing option in the restart subsection. We give the written files a prefix “dem” set in the “set filename” option. The DEM parameter file is initialized exactly as the cylindrical packed bed example. The difference is in the number of particles, their physical properties, and the insertion box defined based on the new geometry. For more explanation about the individual subsections, refer to the DEM parameters and the CFD-DEM parameters .

subsection restart
  set checkpoint = true
  set frequency  = 10000
  set restart    = false
  set filename   = dem
end

Model Parameters#

The section on model parameters is explained in the DEM examples. We show the chosen parameters for this section:

subsection model parameters
  subsection contact detection
    set contact detection method = dynamic
    set neighborhood threshold   = 1.3
  end
  subsection load balancing
    set load balance method     = dynamic
    set threshold               = 0.5
    set dynamic check frequency = 10000
  end
  set particle particle contact force method = hertz_mindlin_limit_overlap
  set particle wall contact force method     = nonlinear
  set integration method                     = velocity_verlet
end

We enable dynamic load balancing in order to fully take advantage of the parallelization of the code.

Lagrangian Physical Properties#

The physical properties section of the particles allows us to specify the different parameters related to the particle such as its density, diameter, and the different coefficients that dictates the collision behavior of the particles. Also, in this section we define the total number of particles for the simulation. The gravitational acceleration as well as the physical properties of particles and walls are specified in the Lagrangian physical properties subsection. These properties include diameter and density of particles, Young’s modulus, Poisson’s ratio, restitution coefficient, friction and rolling friction coefficients. We insert 30,000 particles in the simulation.

subsection lagrangian physical properties
  set g                        = 0.0, -9.81, 0.0
  set number of particle types = 1
  subsection particle type 0
    set size distribution type            = uniform
    set diameter                          = 0.001
    set number                            = 30000
    set density particles                 = 1500
    set young modulus particles           = 1e6
    set poisson ratio particles           = 0.3
    set restitution coefficient particles = 0.2
    set friction coefficient particles    = 0.1
    set rolling friction particles        = 0.2
  end
  set young modulus wall           = 1e6
  set poisson ratio wall           = 0.3
  set restitution coefficient wall = 0.2
  set friction coefficient wall    = 0.1
  set rolling friction wall        = 0.3
end

Insertion Info#

The insertion info subsection manages the insertion of particles. It allows us to control the insertion of particles at each time step. This section is already explained in the DEM examples. However, further information regarding the information box will be given. The volume of the insertion box should be large enough to fit all particles. Also, its bounds should be located within the mesh generated in the Mesh subsection.

subsection insertion info
    set insertion method                               = volume
    set inserted number of particles at each time step = 30000
    set insertion frequency                            = 100000
    set insertion box points coordinates               = -0.018, -0.05, -0.018 : 0.018, 0.05, 0.018
    set insertion distance threshold                   = 1.5
    set insertion maximum offset                       = 0.2
    set insertion prn seed                             = 19
  end

Floating Walls#

We need to pack the particles in the middle of the square bed. Therefore, we create a stopper (floating wall) somewhere below the center of the bed. We chose the point with a y-coordinate of -0.06 to create the wall. We then define a normal to the wall at this point. Make sure that the end time of the floating wall is bigger than the simulation time to ensure that the particles remain suspended. This is shown in:

subsection floating walls
  set number of floating walls = 1
  subsection wall 0
    subsection point on wall
      set x = 0
      set y = -0.06
      set z = 0
    end
    subsection normal vector
      set nx = 0
      set ny = 1
      set nz = 0
    end
    set start time = 0
    set end time   = 5
  end
end

Running the DEM Simulation#

Launching the simulation is as simple as specifying the executable name and the parameter file. Assuming that the lethe-particles executable is within your path, the simulation can be launched on a single processor by typing:

lethe-particles packing-particles.prm

or in parallel (where 8 represents the number of processors)

mpirun -np 8 lethe-particles packing-particles.prm

Lethe will generate a number of files. The most important one bears the extension .pvd. It can be read by popular visualization programs such as Paraview.

Note

Running the packing should take approximately 20 minutes on 8 cores.

After the particles have been packed inside the square bed, it is now possible to simulate the fluidization of particles.

CFD-DEM Parameter File#

The CFD simulation is to be carried out using the packed bed simulated in the previous step. We will discuss the different parameter file sections. The mesh section is identical to that of the DEM so it will not be shown here.

Simulation Control#

The simulation is run for 1 s with a time step of 0.002 s. The time scheme chosen for the simulation is first order backward difference method (BDF1). The simulation control section is shown:

subsection simulation control
  set method               = bdf1
  set output frequency     = 10
  set time end             = 1
  set time step            = 0.001
  set output path          = ./output/
end

Physical Properties#

The physical properties subsection allows us to determine the density and viscosity of the fluid. We choose a density of 1 and viscosity of 0.00001 as to simulate the flow of air.

subsection physical properties
  subsection fluid 0
    set kinematic viscosity = 0.00001
    set density             = 1
  end
end

Initial Conditions#

For the initial conditions, we choose zero initial conditions for the velocity.

subsection initial conditions
  subsection uvwp
      set Function expression = 0; 0; 0; 0
  end
end

Boundary Conditions#

For the boundary conditions, we choose a slip boundary condition on the walls of the square bed (IDs = 0, 1, 4, 5) and an inlet velocity of 0.2 m/s at the lower face of the bed (ID = 2).

subsection boundary conditions
  set number = 6
  subsection bc 0
    set id   = 0
    set type = slip
  end
  subsection bc 1
    set id   = 1
    set type = slip
  end
  subsection bc 2
    set id   = 2
    set type = function
    subsection u
      set Function expression = 0
    end
    subsection v
      set Function expression = 2
    end
    subsection w
      set Function expression = 0
    end
  end
  subsection bc 3
    set id   = 3
    set type = outlet
  end
  subsection bc 4
    set id   = 4
    set type = slip
  end
  subsection bc 5
    set id   = 5
    set type = slip
  end
end

The additional sections for the CFD-DEM simulations are the void fraction subsection and the CFD-DEM subsection. These subsections are described in detail in the CFD-DEM parameters .

Void Fraction#

Since we are calculating the void fraction using the packed bed of the DEM simulation, we set the mode to “dem”. For this, we need to read the dem files which we already wrote using check-pointing. We, therefore, set the read dem to “true” and specify the prefix of the dem files to be dem. In order to ensure that our void fraction projection is bounded, we choose an upper bound limit of 1. We decide not to lower bound the void fraction and thus attributed a value of 0 to the L2 lower bound parameter. We now choose a smoothing factor for the void fraction to reduce discontinuity which can lead to oscillations in the velocity. The factor we choose is around the square of twice the particle’s diameter.

subsection void fraction
    set mode                = pcm
    set read dem            = true
    set dem file name       = dem
    set l2 smoothing factor = 0.000005
    set l2 lower bound      = 0
    set l2 upper bound      = 1
    set bound void fraction = false
end

CFD-DEM#

We also enable grad_div stabilization in order to improve local mass conservation. The void fraction time derivative is enabled to account for the time variation of the void fraction.

Note

For certain simulations, this parameter should be disabled to improve stability of the solver.

subsection cfd-dem
    set grad div                      = true
    set void fraction time derivative = true
    set drag force                    = true
    set buoyancy force                = true
    set shear force                   = false
    set pressure force                = false
    set drag model                    = difelice
    set coupling frequency            = 100
    set vans model                    = modelB
end

We determine the drag model to be used for the calculation of particle-fluid forces as the Di Felice model. Other optional forces that can be enabled are the buoyancy force, the shear force and the pressure force. We only decide to enable drag and buoyancy as for air, the other forces are considered to be negligible. The VANS model we are solving is model B. Other possible option is model A.

Finally, the linear and non-linear solver controls are defined.

Non-linear Solver#

We use the inexact Newton non-linear solver to minimize the number of time the matrix of the system is assembled. This is used to increase the speed of the simulation, since the matrix assembly requires significant computations.

subsection non-linear solver
  subsection fluid dynamics
    set solver           = inexact_newton
    set tolerance        = 1e-7
    set max iterations   = 20
    set matrix tolerance = 0.2
    set verbosity        = verbose
  end
end

Linear Solver#

subsection linear solver
  subsection fluid dynamics
    set method                                = gmres
    set max iters                             = 5000
    set relative residual                     = 1e-3
    set minimum residual                      = 1e-11
    set preconditioner                        = ilu
    set ilu preconditioner fill               = 1
    set ilu preconditioner absolute tolerance = 1e-14
    set ilu preconditioner relative tolerance = 1.00
    set verbosity                             = verbose
    set max krylov vectors                    = 200
  end
end

Running the CFD-DEM Simulation#

The simulation is run using the lethe-fluid-particles application. Assuming that the lethe-fluid-particles executable is within your path, the simulation can be launched as per the following command:

lethe-fluid-particles fluidized-bed.prm

Results#

The results are shown in an animation below. We show the fluidization of the particles as the gas is introduced from the bottom of the bed.