The Bio-Denipho(R) process, a ''phased isolation ditch'' technology, v
aries both aeration pattern and flow path in a continuous flow multi-r
eactor system to force oscillation of organic and nutrient concentrati
ons in process reactors. Using a six-phase cycle, desired biochemical
transformations (e.g. nitrification, denitrification), are accomplishe
d at different times in the same reactor. We used an industry-standard
biokinetic model (IAWPRC) to develop and test three control strategie
s of increasing sophistication: (a) fixed phase lengths, (b) use of co
nstant set points to switch between phases thus resulting in variable
phase lengths, and (c) use of switching set points which are a functio
n of on-line measurements (criteria functions). These strategies were
optimized for nominal diurnal operating conditions, with the objective
of minimizing effluent soluble nitrogen, subject to an upper bound on
the oxygen transfer coefficient. In addition, performance of the stra
tegies was simulated against 1-, 2-, and 5-day sustained peak loads. U
nder nominal diurnal conditions, the performance obtained with each st
rategy was comparable. Under peak loading conditions, both of the swit
ching set point strategies gave substantially better performance than
the fixed phase length strategy. Criteria functions were marginally be
tter than constant switch points.