A new concept for ammonium removal from secondary effluent by zeolite
followed by bioregeneration has been studied. In contrast to other stu
dies of hybrid biological-ion exchange multireactor Systems, the propo
sed process uses the ion exchange material, zeolite, as a carrier for
the nitrifying biomass. Therefore, the entire process is carried out i
n a single reactor. Since all the ammonium from the original effluent
is concentrated in the zeolite and released gradually during regenerat
ion, nitrification is carried out in a small volume reactor in an almo
st batch mode where optimal conditions for nitrification can easily be
maintained. Moreover, the conversion of ammonium cations to nitrate a
nions allows for regenerate recycle, where the amount of chemicals add
ed for desorption is reduced to the amount of sodium bicarbonate added
as a buffer for nitrification. As a result, operational costs and pro
duction of large volumes of brine are minimized. To achieve sufficient
NH4+ concentration in the solution to allow for high rate nitrificati
on, the cation-rich regenerant solution (or part of it) is reused from
one cycle to the next. A theoretical model including ion exchange and
bioregeneration modes, indicates that the total cation concentration
and each cation in the recycled regenerant should reach constant value
s after several cycles of adsorption-regeneration and remain constant
as long as the influent characteristics and operation conditions stay
similar. Experiments results verified the predicted values. (C) 1998 E
lsevier Science Ltd. All rights reserved.