Simulation of commercial scale tablet press feed system with a coupled CFD-DEM model.
CFD-DEM simulation of a fine, poly-disperse pharmaceutical powder in a closed tube. It can be clearly seen that size segregation is caused by the counter-current airflow which is induced by the particle stream falling downwards. This use case is inspired by Kocevar et al. (2015).
This video shows a simulation of solid-liquid mixing in stirred tank. A semi-implicit immersed boundary method has been used to solve the fluid flow due to the rotating geometry. The CFD-DEM coupling, however, is of the unresolved type. Please, refer to the following publication for further information: Blais, B. et al. (2016). Development of an unresolved CFD–DEM model for the flow of viscous suspensions and its application to solid–liquid mixing.
Rotating drum with concave particles.
Mixing of convex particles:
Mixing simulation of cohesive (right) and non-cohesive (left) material. In this project we investigated the mixing efficiency of the geometry, the change of the mixing efficiency for different materials (see graph in video), the residence time distribution and design questions of the mixer geometry.
Application case – magnetic separation of particles. The conveyor belt transports particles into magnetic region – particles with strong dipole are separated (depending on their position within the particle bed).
Three-phase (Euler-Euler) CFD-DEM simulations of a fluidized bed.
KPIs like residence time distributions from processes which take hours used to be inaccessible to highly resolved DEM simulations – now they are accessible!
Simulation of commercial scale tablet press feed system with a coupled CFD-DEM model.
CFD-DEM simulation of a fine, poly-disperse pharmaceutical powder in a closed tube. It can be clearly seen that size segregation is caused by the counter-current airflow which is induced by the particle stream falling downwards. This use case is inspired by Kocevar et al. (2015).
This video shows a simulation of solid-liquid mixing in stirred tank. A semi-implicit immersed boundary method has been used to solve the fluid flow due to the rotating geometry. The CFD-DEM coupling, however, is of the unresolved type. Please, refer to the following publication for further information: Blais, B. et al. (2016). Development of an unresolved CFD–DEM model for the flow of viscous suspensions and its application to solid–liquid mixing.
Rotating drum with concave particles.
Mixing of convex particles:
Mixing simulation of cohesive (right) and non-cohesive (left) material. In this project we investigated the mixing efficiency of the geometry, the change of the mixing efficiency for different materials (see graph in video), the residence time distribution and design questions of the mixer geometry.
Application case – magnetic separation of particles. The conveyor belt transports particles into magnetic region – particles with strong dipole are separated (depending on their position within the particle bed).
Three-phase (Euler-Euler) CFD-DEM simulations of a fluidized bed.
KPIs like residence time distributions from processes which take hours used to be inaccessible to highly resolved DEM simulations – now they are accessible!