M. Cassanello et al., EXPERIMENTAL CHARACTERIZATION OF THE SOLID-PHASE CHAOTIC DYNAMICS IN 3-PHASE FLUIDIZATION, Industrial & engineering chemistry research, 34(9), 1995, pp. 2971-2980
An experimental study of the solid phase dynamics in a three-phase flu
idized bed reactor using heavy and light particles is carried out. A r
adioactive particle tracking technique is employed to obtain extended
time series of the tracer path. The tracer has the same properties as
the rest of the particles in the bed. A rescaled range-analysis is app
lied to time series of the fluctuating velocities to investigate the f
eatures of solid phase turbulence. It is found that turbulence is anis
otropic. In the axial direction, the correlations between the fluctuat
ing velocities are persistent in time, indicating a superdispersive ax
ial dispersion of the solids. Hence a constant axial dispersion coeffi
cient, which is traditionally used in these reactors to represent the
solid phase turbulence, only constitutes a lumped parameter hardly ext
rapolable to different operating conditions, different systems, and di
fferent geometries. The tracer path is also analyzed according to the
theory of deterministic chaos. It is found that the solids motion is c
haotic. An increase in the gas flow rate increases the values of the p
arameters that quantify the chaotic behavior of the solids motion. Thi
s analysis is found to constitute a promising tool to determine flow r
egime transitions.