Production of alpha-amylase by a strain of Bacillus amyloliquefaciens
was investigated in a cell recycle bioreactor incorporating a membrane
filtration module for cell separation. Experimental fermentation stud
ies with the B. amyloliquefaciens strain WA-4 clearly showed that inco
rporating cell recycling increased alpha-amylase yield and volumetric
productivity as compared to conventional continuous fermentation. The
effect of operating conditions on alpha-amylase production was difficu
lt to demonstrate experimentally due to the problems of keeping the pe
rmeate and bleed rates constant over an extended period of time. Compu
ter simulations were therefore undertaken to support the experimental
data, as well as to elucidate the dynamics of alpha-amylase production
in the cell recycle bioreactor as compared to conventional chemostat
and batch fermentations. Taken together, the simulations and experimen
ts clearly showed that low bleed rate (high recycling ratio) various a
high level of alpha-amylase activity. The simulated fermentations rev
ealed that this was especially pronounced at high recycling ratios. Vo
lumetric productivity was maximum at a dilution rate of around 0.4 h(-
1) and a high recycling ratio. The latter had to exceed 0.75 before vo
lumetric productivity was significantly greater than with conventional
chemostat fermentation.