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The 3D turbulence k-ε model flow of the steel melt(continuous phase)and the trajectories of individual gas bubbles(dispersed phase)in a continuous casting mold were simulated using an Eulerian-Lagrangian approach.In order to investigate the effect of bubble size distribution,the radii of bubbles are set with an initial value of 0.1-2.5mm which follows the normal distribution.The presented results indicate that,in the submerged entry nozzle(SEN),the distribution of void fraction is only near the wall.Due to the fact that the bubbles motion is only limited to the wall,the deoxidization products have no access to contacting the wall,which prevents clogging.In the mold,the bubbles with a radius of 0.25-2.5mm will move to the top surface.Larger bubbles issuing out of the ports will attack the meniscus and induce the fluid flows upwards in the top surface near the nozzle.It may induce mold powder entrapment into the mold.The bubbles with a radius of 0.1-0.25mm will move to the zone near the narrow surface and the wide surface.These small bubbles will probably be trapped by the solidification front.Most of the bubbles moving to the narrow surface will flow with the ascending flow,while others will flow with the descending flow.
The 3D turbulence k-ε model flow of the steel melt (continuous phase) and the trajectories of individual gas bubbles (dispersed phase) in a continuous casting mold were simulated using an Eulerian-Lagrangian approach. Order to investigate the effect of bubble size distribution of the radii of bubbles are set with an initial value of 0.1-2.5mm which follows the normal distribution. The presented results indicate that that, in the submerged entry nozzle (SEN), the distribution of void fraction is only near the wall. to the fact that the bubbles motion is only limited to the wall, the deoxidization products have no access to contacting the wall, which prevents clogging. in the mold, the bubbles with a radius of 0.25-2.5mm will move to the top surface. Larger bubbles issuing out of the ports will attack the meniscus and induce the fluid flows upwards in the top surface near the nozzle .It may induce mold powder entrapment into the mold. Bubbles with a radius of 0.1-0.25mm will move to the zone near the same narrow surface and the wide surface.These small bubbles will probably be trapped by the solidification front.Most of the bubbles moving to the narrow surface will flow with the ascending flow, while others will flow with the descending flow.