Macroscopic flow structures of gas-liquid and gas-liquid-solid fluidiz
ation systems are studied through flow visualization using a two-dimen
sional column under various operating conditions. The gas distributor
in the column comprises multiple injectors which are individually regu
lated to generate desired gas flow rates, bubble injection frequencies
, and bubble sizes. Colored bed particles and neutrally buoyant partic
les as solid and liquid tracers, respectively, are used for flow visua
lization through video photography. In a gas-liquid system operated un
der liquid-batch conditions, bubble streams injected near both sidewal
ls are observed to migrate toward bed vertical axis, and vortices appe
ar along the sidewalls when gas velocity exceeds 4-6 mm/s. A considera
ble amount of liquid descends along the sidewalls in a vortical flow p
attern. The gross circulation pattern occurring at high gas velocities
is associated closely with induced liquid or liquid-solid flows resul
ting from rising bubbles and bubble wakes. When the gross circulation
occurs, four flow regions can be distinguished. The formation of and m
echanism for gross circulations can be interpreted in part based on tw
o simplified flow conditions involving single bubbles rising in a stat
ionary liquid and single chains of bubbles injected in a batch liquid.
The effects of particle size, inlet liquid velocity and gas flow dist
ribution on the macroscopic flow structure are also examined.