A model of agglomerate break-up, incorporating both rupture and erosion, is employed to predict the dynamics of filler size distribution in a plasticating single screw extruder. Filler spatial distribution along the extruder length was also ascertained and direct comparison of experimental and computational data proved to be satisfactory. The method was also used to investigate the effect of material properties, operating conditions and extruder geometry on the dynamics of agglomerate dispersion along a single screw extruder. Generally, dispersion levels were primarily governed by the magnitude of the hydrodynamic stresses developed in the extruder and the residence time in the melt
A new model for the residence-time distribution in a counter rotating twin-screw extruder is compare...
International audienceTo be able to predict the throughput of a single-screw extruder or the meterin...
The present work presents numerical simulations of dispersive and distributive mixing of a two phas...
A model of agglomerate break-up, incorporating both rupture and erosion, is employed to predict the ...
A model of agglomerate break-up, incorporating both rupture and erosion, is employed to predict the ...
International audienceParticle size distribution strongly affects physical and mechanical properties...
A model for solid agglomerate dispersion in single screw extruders is proposed. The model combines n...
A model for solid agglomerate dispersion in single screw extruders is proposed. The model combines n...
We present a new model for assessing mixing in extrusion processes. The model combines numerical sim...
A mathematical model to predict the evolution of the morphology of immiscible liquid-liquid systems ...
A model for agglomerate dispersion in screw extruders was developed and superimposed on the flow pa...
Simulation of monomeric material transport in reactive extrusion revealed that two different situati...
Polymer extrusion is one of the most important polymer processing techniques. Modelling of the pheno...
Models to predict the evolution of the morphology of immiscible liquid-liquid systems and of solid a...
Mixing indices can be derived from descriptions of morphology evolution of liquid-liquid or solid-li...
A new model for the residence-time distribution in a counter rotating twin-screw extruder is compare...
International audienceTo be able to predict the throughput of a single-screw extruder or the meterin...
The present work presents numerical simulations of dispersive and distributive mixing of a two phas...
A model of agglomerate break-up, incorporating both rupture and erosion, is employed to predict the ...
A model of agglomerate break-up, incorporating both rupture and erosion, is employed to predict the ...
International audienceParticle size distribution strongly affects physical and mechanical properties...
A model for solid agglomerate dispersion in single screw extruders is proposed. The model combines n...
A model for solid agglomerate dispersion in single screw extruders is proposed. The model combines n...
We present a new model for assessing mixing in extrusion processes. The model combines numerical sim...
A mathematical model to predict the evolution of the morphology of immiscible liquid-liquid systems ...
A model for agglomerate dispersion in screw extruders was developed and superimposed on the flow pa...
Simulation of monomeric material transport in reactive extrusion revealed that two different situati...
Polymer extrusion is one of the most important polymer processing techniques. Modelling of the pheno...
Models to predict the evolution of the morphology of immiscible liquid-liquid systems and of solid a...
Mixing indices can be derived from descriptions of morphology evolution of liquid-liquid or solid-li...
A new model for the residence-time distribution in a counter rotating twin-screw extruder is compare...
International audienceTo be able to predict the throughput of a single-screw extruder or the meterin...
The present work presents numerical simulations of dispersive and distributive mixing of a two phas...