A. Chehbouni et al., EFFECTS OF DIFFERENT PARAMETERS ON THE ON SET OF FLUIDIZATION IN A TURBULENT REGIME, Canadian journal of chemical engineering, 73(1), 1995, pp. 41-50
Much controversy exists in the literature about the effects of differe
nt variables on the onset of the turbulent regime in gas-solid fluidiz
ation, U-c, and on the transport velocity, U-tr. In order to study the
effect of four hydrodynamic factors upon these transition velocities,
a basic 8-run Plackett-Burman design was used. The factors and their
level were: (a) diameter of column (82 vs 200 mm), (b) particles (FCC
vs Sand), (d) static bed height (300 vs 450 mm) and (g) size distribut
ion of particles (narrow vs wide). In each run, U-c and U-tr were dete
rmined experimentally by means of differential pressure transducer and
also with a capacitance probe. The experimental results and statistic
al analysis show that bed diameter has the most important impact (61%
variability upon U-c and 51% upon U-tr). The product of particle size
and density (p(p)d(p)) seems to have a significant effect (35% variabi
lity upon U-c and 47% upon U-tr). Static bed height has a slight impac
t. There is essentially no effect of the particle size distribution. R
esults show that interactions effects are negligible between these fac
tors. Finally, two correlations for U-c and U-tr, which are in agreeme
nt with literature data are proposed.