C. Webb et al., THE MAGNETICALLY STABILIZED FLUIDIZED-BED BIOREACTOR - A TOOL FOR IMPROVED MASS-TRANSFER IN IMMOBILIZED ENZYME-SYSTEMS, Chemical engineering journal and the biochemical engineering journal, 61(3), 1996, pp. 241-246
Studies were carried out using novel magnetic carrier particles in a m
agnetically stabilized fluidized bed (MSFB) to determine the degree of
liquid phase mass transfer enhancement achievable over a range of mag
netic field strengths. The carrier particles, beads of K-carrageenan i
ncorporating magnetite, ranging in size from 0.25 to 1 mm are used for
enzyme immobilization. Results using a 113 mm diameter column showed
that a more than five-fold increase in liquid velocity could be achiev
ed when a current of 40 A was applied to a single magnetic coil. The '
'escape'' velocity of the particles from the bed was found to be propo
rtional to the magnetic field intensity squared. The effect was furthe
r increased (almost doubled) by inserting a steel rod into the centre
of the bed.