CFD modeling of droplet permeability in fluidized beds

The deposition of droplets of size [5–22] μm on the surface of particles in a gas–solid fluidized bed has been investigated employing a one-way coupled CFD-DEM modeling. In this approach the gas phase is solved as a continuum and the free-droplets are solved as Lagrangian objects, while solid partic...

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Bibliographic Details
Main Authors: Balice, D.M (Author), Deen, N.G (Author), Fochesato, M. (Author), Molenaar, C.W.C (Author), Roghair, I. (Author), van Sint Annaland, M. (Author), Venier, C.M (Author)
Format: Article
Language:English
Published: Elsevier Ltd 2022
Subjects:
Online Access:View Fulltext in Publisher
LEADER 03082nam a2200529Ia 4500
001 10.1016-j.ijmultiphaseflow.2022.104069
008 220425s2022 CNT 000 0 und d
020 |a 03019322 (ISSN) 
245 1 0 |a CFD modeling of droplet permeability in fluidized beds 
260 0 |b Elsevier Ltd  |c 2022 
856 |z View Fulltext in Publisher  |u https://doi.org/10.1016/j.ijmultiphaseflow.2022.104069 
520 3 |a The deposition of droplets of size [5–22] μm on the surface of particles in a gas–solid fluidized bed has been investigated employing a one-way coupled CFD-DEM modeling. In this approach the gas phase is solved as a continuum and the free-droplets are solved as Lagrangian objects, while solid particles are assumed to be stationary and act as an obstacle for the fluid flow. In this way, it was possible to calculate the deposition factor, defined as the ratio of droplets deposited on the surface of the particles to the number of droplets injected into the domain as a function of the droplet Stokes number and particle Reynolds number. An empirical correlation was developed that describes the deposition factor as a function of the operating conditions, which is valid for the inertial regime where effects of Brownian motion can be neglected. The final goal of this investigation is to employ the developed correlation in a larger scale CFD-DEM model describing a polymerization fluidized bed reactor operated in condensed mode, i.e. by injecting liquid into the gas–solid suspension through the gas distributor plate or via nozzles in order to improve the heat management. In this kind of modeling the free-droplets phase is described as a continuum and the deposition rate of droplets determines the amount of liquid on the particle surface, which affects for the hydrodynamic (i.e. formation of liquid bridges between particles) and thermal behavior (i.e. liquid evaporation, kinetic and subsequent cooling effect) of the system. © 2022 The Author(s) 
650 0 4 |a Brownian movement 
650 0 4 |a CFD modeling 
650 0 4 |a CFD-DEM 
650 0 4 |a CFD-DEM 
650 0 4 |a Computational fluid dynamics 
650 0 4 |a DEM modelling 
650 0 4 |a Deposition rates 
650 0 4 |a Droplets 
650 0 4 |a Drops 
650 0 4 |a Fluidization 
650 0 4 |a Fluidized bed 
650 0 4 |a Fluidized beds 
650 0 4 |a Gas-phases 
650 0 4 |a Gas-solids fluidized beds 
650 0 4 |a Granular matter 
650 0 4 |a Granular matter 
650 0 4 |a Lagrangian 
650 0 4 |a Liquids 
650 0 4 |a Multiphase flow 
650 0 4 |a OpenFOAM 
650 0 4 |a OpenFOAM 
650 0 4 |a Particle 
650 0 4 |a Particles 
650 0 4 |a Reynolds number 
650 0 4 |a Solid particles 
650 0 4 |a Spray nozzles 
650 0 4 |a Suspensions (fluids) 
700 1 |a Balice, D.M.  |e author 
700 1 |a Deen, N.G.  |e author 
700 1 |a Fochesato, M.  |e author 
700 1 |a Molenaar, C.W.C.  |e author 
700 1 |a Roghair, I.  |e author 
700 1 |a van Sint Annaland, M.  |e author 
700 1 |a Venier, C.M.  |e author 
773 |t International Journal of Multiphase Flow