En. Kaufman et al., CONTINUOUS AND SIMULTANEOUS FERMENTATION AND RECOVERY OF LACTIC-ACID IN A BIPARTICLE FLUIDIZED-BED BIOREACTOR, Applied biochemistry and biotechnology, 57-8, 1996, pp. 503-515
A continuous biparticle fluidized-bed reactor (BFBR) is developed for
the simultaneous fermentation and recovery of lactic acid. In this pro
cessing scheme, bacteria are immobilized in gelatin beads and are flui
dized in a columnar reactor. Solid particles (weak-base resin IRA-35)
with sorbent capacity for the product are introduced at the top of the
reactor and fall countercurrently to the biocatalyst, effecting in si
tu removal of the inhibitory lactic acid while also controlling reacto
r pH at optimal levels. One-week-long fermentation trials using immobi
lized Lactobacillus delbreuckii with sorbent addition demonstrated a v
olumetric productivity (6.9 g/L . h) at least 16-fold higher than that
of a free-cell batch fermentation with base pH control and identical
biomass concentration and medium composition. Regeneration of the load
ed sorbent from the BFBR has effected a 35-fold concentration of lacti
c acid compared with original levels in the fermentation broth (70 vs
2 g/L). Lactic acid concentrations as high as 610 g/L have been observ
ed when the loading solution contained 50 g/L lactic acid. Rich medium
formulations did not seem to increase BFBR performance. The benefits
of this reactor system, as opposed to conventional batch fermentation,
are discussed in terms of productivity and process economics.