The optimization of the operation of biological reactors is an interesting
non-linear problem whose solution offers potential economic benefit. We app
ly a peak seeking method to approach the maximum biomass production rate in
a continuous stirred tank bioreactor. Two models, Monod and Haldane, are i
nvestigated and it is shown by simulation that the peak seeking scheme achi
eves optimization for both cases. A stabilizing feedback controller with a
washout filter is designed to extend the operating range for the Haldane mo
del. Copyright (C) 1999 John Wiley & Sons, Ltd.