COSTA, T. M. M.; http://lattes.cnpq.br/9688739254952937; COSTA, Tuana Maria de Medeiros.
Resumo:
Fluidized beds are widely used in many operations in the chemical, agricultural, biochemical,
power generation and especially petrochemical industries. Full understanding of the movement
of solids in a fluidized bed remains quite complex, and depends on parameters such as bed
geometry and particle properties. The first mathematical models that describe the fluid
dynamics of the fluidized bed considered a one-dimensional flow and constant parameters.
With the advent of faster and more efficient computers have enabled the use of mathematical
models based on the complete equations of conservation of mass, linear momentum, heat and
matter applying Computational Fluid Dynamics (CFD). In this sense, the purpose of this paper
is to evaluate the fluid dynamics of fluidized bed applying Eulerian-Lagrangean approach
considering the Dense Discrete Phase Model (DDPM) in combination with the Discrete
Element Method (DEM), this is responsible for modeling the collisions of a given discrete
phase. Ansys Fluent commercial application was used to obtain the results of numerical
simulations. The base case for comparison and verification is presented by Azhar e Stopford
(2012), which was also simulated via the Ansys Fluent DDPM-DEM coupling. The results
obtained with the simulations were finally validated with the experimental data found in
Taghipuor et al. (2005).