An experimental technique has been developed to delineate the differen
t hydrodynamic regimes of a gas-solid fluidized bed, each regime signi
fying a characteristic type of fluidization. The technique involves th
e measurement and statistical analysis of temperature-history records
of an element of the heat-transfer surface immersed in a fluidized bed
in which different regimes are brought about by changing gas velocity
. The experiments were conducted in a 0.153-m square fluidized bed of
2093-mu m average diameter spherical glass beads at ambient conditions
. The statistical functions computed at each gas velocity were the sta
ndard deviation, probability density function, autocorrelation functio
n, and power spectral density function. The standard deviation and the
major frequency defined from the power spectral density function were
found to represent characteristically the bubbling, transitional and
turbulent hydrodynamic regimes. The bed voidage and the local heat-tra
nsfer coefficient were also measured as functions of gas velocity. The
ir appropriateness to represent the quality of bed fluidization has be
en examined. (C) 1998 Elsevier Science Ltd. All rights reserved.