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However, despite decades of research and industrial application, the real time behavior of particle flow fields in CFB's is still not well understood.
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The real time and continuous measurement of dense phase gas solid flow parameters such as particle velocity, concentration and mass flow rate has great significance for the in-depth understanding of particle flow dynamic behaviors and the optimized design of the conveying system.
In a certain process, we study the behavior of the particle flow in two potential parameters and then find that structures exist in the net flow of particles in different potentials or processes.
The distinct element method (DEM) has proven to be reliable and effective in characterizing the behavior of particles in granular flow simulations.
The flow behavior of particle mixing or separation in bubbling fluidized beds was numerically predicted.
Furthermore, we investigate the self-similar solution of batch aggregation to show scaling behavior of particle size distributions in such flow systems using spatially dependent average particle sizes.
Small particles are gradually dispersed toward the periphery of the two-phase flow field after being ejected from the rectangular nozzle, giving rise to a bimodal behavior of particle size distributions in the region far from the guide baffle.
Flow behavior of particles in a porous media is simulated by means of CFD-DEM.
Flow behavior of particles is simulated using an Eulerian Eulerian two-fluid model based on the kinetic theory of rough spheres.
Flow behavior of particles in a two-dimensional spouted bed with a draft tube is studied using a continuous kinetic-friction stresses model.
Flow behavior of particles in a circulating fluidized bed (CFB) riser is numerically simulated using a two-fluid model incorporating with the kinetic theory for particle rotation and friction stress models.
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