Accurate defection of minimum liquid fluidization is essential to the
successful operation of gas-liquid-solid fluidized beds, especially wh
en particle or liquid properties evolve. A gas-liquid-solid system of
3-mm glass beads exhibits three distinct flow regimes as the liquid ve
locity is increased: compacted agitated and fluidized-bed regimes. Mea
surements showed that the bed is not fluidized in the agitated bed reg
ime. Pressure gradient and bed height measurements do not provide the
minimum liquid fluidization velocity; instead they offer the velocity
between the compacted and agitated bed regimes. Time-averaged signals
are not reliable for determining the minimum liquid fluidization veloc
ity. it can be obtained from the standard deviation, the average frequ
ency, the Hurst exponent and the V statistic of the cross-sectional av
erage conductivity, which can be measured under many industrial condit
ions.