This work concerns the evaluation of a numerical model of a scaled circulat
ing fluidized bed (CFB) with a square cross section. The evaluation consist
s of a comparison of the numerical results with measurements achieved using
laser Doppler anemometry (LDA) and pressure taps. The CFB is fluidized usi
ng metal particles, which enable the laboratory-scale CFB to be operated un
der scaled conditions of a full-scale CFB. The numerical part is based on a
three-dimensional multiphase computational fluid dynamics (CFD) model that
uses an Eulerian description for the gas and solid phases. The conservatio
n equations for the solid phases are based on the kinetic theory for granul
ar flow, which provides adequate modeling of the solid phase when the Euler
ian approach is used. Three-dimensional simulations. are found to be superi
or to two-dimensional simulations in comparisons to the experimental findin
gs.