An experimental study has been carried out investigating the fluidization
behavior of a bubble column with a bottom magnetic particle bed controlled
by an external transverse magnetic field. The
magnetization-first/gas-scanning mode was applied, at up to 45 kA m-1 field
intensity, with liquid superficial velocities of up to 20 mm s-1 and with a
gas flowrate of up to 8 m3 h-1. Particle fractions of two different sizes of
up to 1 mm were used. The focus has been both on the three-phase magnetic
particle bed expansion playing the role of a gas distributor and the gas
holdup of the abovepositioned two-phase section, as well as related column
parameters. Piezometric measurements have been performed that provided
detection of the position of the interface between the two column sections
without visual observation, as well as the gas holdup in the two-phase zone.
The bed expansion was strongly affected by the bed state created by the
initially established liquid flow rate. The results showed that the
intensity of the field applied to the magnetic solids allows control both of
bed expansion and internal bed structure, so the applicability of
magnetically assisted three-phase beed as a gas distributor in bubble column
seems promising.