Using a 3D Front Tracking (FT) model, closures for the drag, lift and virtual mass forces have been derived for single freely deformable air bubbles rising in water. The combination of a large surface tension force, a high density ratio as well as a high Reynolds number poses a severe numerical challenge for Direct Numerical Simulations. Therefore, the numerical implementation of the FT model was improved to allow simulation of very small air bubbles (~1 mm) in water using realistic physical properties without numerical problems or unphysical volume changes. The computed drag force coefficients for air bubbles in the range of 1-5 mm compare reasonably well with experimental data from literature. The small discrepancies may be explained by t...
Dispersed gas-liquid flows are often encountered in the chemical process industry. Large scale model...
It is well-known that the lift force is responsible for the segregation of small and large bubbles e...
CFD modeling of dispersed multiphase flows can be quite challenging because of the wide range of tim...
Using a 3D Front Tracking (FT) model, closures for the drag, lift and virtual mass forces have been ...
Closures for the drag, virtual mass and lift forces acting on a single air bubble or toluene droplet...
Closures for the drag and virtual mass forces acting on a single air bubble rising in initially quie...
Closures for the drag, virtual mass and lift forces acting on a single air bubble or toluene droplet...
Closures for the drag and virtual mass forces acting on a single air bubble rising in initially quie...
In this paper a three-dimensional (3-D) front-tracking (FT) model is presented featuring a new metho...
In recent years CFD has proven to be a valuable and powerful tool for advancing our understanding of...
In recent years CFD has proven to be a valuable and powerful tool for advancing our understanding of...
Dispersed gas-liquid flows are often encountered in the chemical process industry. Large scale model...
It is well-known that the lift force is responsible for the segregation of small and large bubbles e...
Dispersed gas-liquid flows are often encountered in the chemical process industry. Large scale model...
It is well-known that the lift force is responsible for the segregation of small and large bubbles e...
CFD modeling of dispersed multiphase flows can be quite challenging because of the wide range of tim...
Using a 3D Front Tracking (FT) model, closures for the drag, lift and virtual mass forces have been ...
Closures for the drag, virtual mass and lift forces acting on a single air bubble or toluene droplet...
Closures for the drag and virtual mass forces acting on a single air bubble rising in initially quie...
Closures for the drag, virtual mass and lift forces acting on a single air bubble or toluene droplet...
Closures for the drag and virtual mass forces acting on a single air bubble rising in initially quie...
In this paper a three-dimensional (3-D) front-tracking (FT) model is presented featuring a new metho...
In recent years CFD has proven to be a valuable and powerful tool for advancing our understanding of...
In recent years CFD has proven to be a valuable and powerful tool for advancing our understanding of...
Dispersed gas-liquid flows are often encountered in the chemical process industry. Large scale model...
It is well-known that the lift force is responsible for the segregation of small and large bubbles e...
Dispersed gas-liquid flows are often encountered in the chemical process industry. Large scale model...
It is well-known that the lift force is responsible for the segregation of small and large bubbles e...
CFD modeling of dispersed multiphase flows can be quite challenging because of the wide range of tim...