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Fluidized-bed crystallizers are widely utilized across numerous branches of industry. However, they have proven difficult to scale up. The present work reports the scale-up of an Oslo fluidized-bed crystallizer with a classification leg using computational fluid dynamic (CFD) methods. The apparatus was modeled in six volumes: 0.039, 0.33, 2.64, 29, 97, and 230m 3 . Calculations cover polydispersive...
The main goal of this paper is to model a multiphase flow of a monodispersed suspensions in various types of crystallizers: Draft Tube Magma (DTM), Double Draft Tube (DDT) and Fluidized bed (FL). To do this, the CFD (Computational Fluid Dynamics) methods were used. The geometry of model apparatus was similar to those applied in industry. The composition of suspensions and their physical properties...
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