Revolving Rice Dryer Using DPM CFD Simulation

$360.00 Student Discount

In this project, a revolving rice dryer using one-way DPM has been simulated and the results of this simulation have been investigated.

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Description

Rice Dryer Using DPM (Revolving ), CFD Simulation Ansys Fluent Training

In this project, a revolving rice dryer device was simulated using Evaporating droplets with a one-way DPM model in Ansys Fluent software, and then the results were investigated. Hot air enters the rice dryer through the holes in a porous tube located at the center of the enormous chamber. About three million rice particles are injected with 15% moisture droplets into a chamber revolving with 100rpm angular speed.

Geometry & Mesh

The 3D geometry was generated in Design Modeler software. A cylinder with a 4.5m diameter and 1.68m  height.

Rice Dryer

In addition, an unstructured mesh grid was carried out using Ansys meshing software, and overall, 2703907 elements were generated.

Rice DryerRice Dryer

CFD Simulation

Several assumptions have been considered to simulate Revolving rice dryer, including:

  • The simulation is Transient(unsteady) in order to capture the behavior of fluid and particles over time.
  • The pressure-based solver type was used due to the incompressibility of the working fluid(air).
  • The One-way Discrete Phase Model(DPM) was utilized, so the grains of rice particles were injected with our desired condition into the fluid domain.
  • Gravitational acceleration effects were considered 9.81m/s^2 in z-direction.

The following table represents a summary of the solution:

Models(Viscous)
Energy On
Viscous k-epsilon Standard Standard Wall Function
Species Species Transport Mixture-template
Discrete Phase Model
Interaction with continuous phase
Unsteady particle tracking
off

on

Injections
Injection Type

Number of streams

Surface – wallinlet

 

Particle Type Droplet
Material

Evaporating species

Diameter distribution

Water-liquid

H2o

Uniform

Diameter 0.00214m Stop Time 8s
Temperature 300K Velocity Magnitude 1m/s
Start Time 0s Total Flow Rate 0.05kg/s
Materials
Mixture-template Definition method Fluent database
Material name Air
Droplet Particle Definition method Fluent database
  Material name Water-liquid

Volatile component fraction = 15%

Cell zone condition
Material name Mixture-template
Frame Motion Speed 100rpm
Boundary condition
Inlet Type Velocity inlet
Velocity magnitude 0.3m/s
Turbulent intensity 10%
Hydraulic Diameter 0.0254
Temperature 308K
DPM BC Type escape
Outlet Type Wall
DPM BC Type reflect
Tube Type Wall
Coupled
DPM BC Type reflect
Solver configuration
Pressure-velocity coupling Scheme Coupled
Spatial Discretization Gradient Least squares cell-based
Pressure Second-order
Momentum Second-order upwind
Turbulent kinetic energy First-order upwind
Turbulent dissipation rate First-order upwind
H2o Second-order upwind
Energy Second-order upwind
Initialization Initialization methods Standard Initialization
Run calculation Time step size 0.1
Number of time steps 1600
Max iterations per time step 20

Results

After injecting about three million rice particles through the inlet, they gather around the porous tube in the middle of the chamber. As shown in figure 1, H2o mass fraction concentrated around the tube at first, but after a while, due to the release of hot air from tube holes to the chamber, the evaporating process begins and causes vaporizing material(H2o) to disperse; This may reduce the moisture of rice particles which was 15% at the beginning and as a result, the diameter decrease that depicted in figure 2. In addition, the Rotational speed of the chamber accelerates the circulation of hot air.

Rice DryerRice DryerRice Dryer

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