P. Chudoba et R. Pujol, Technical solutions for upgrading high rate and medium loaded activated sludge plants for nutrient removal, WATER SCI T, 41(9), 2000, pp. 131-138
In order to meet the requirements for total nitrogen removal in sensitive a
rea, as specified by the EC Standards, existing high-rate or medium loaded
activated sludge plants treating only carbonaceous pollution have to be upg
raded. Two attractive technical solutions are proposed. Depending on both t
he design and operational conditions of the activated sludge plants, all ex
isting treatment facilities will be reused for nutrient removal with either
an immobilized nitrifying system implemented directly in the existing acti
vated sludge tank or with an additional up-flow nitrifying biofilter. Both
technical solutions enable the effluent total nitrogen concentration to be
as low as 10 mg TN/I. When a high or medium loaded activated sludge plant w
ith primary settling tanks is designed for a HRT of more than five hours, t
he Pegazur immobilized carrier system can be implemented directly in the bi
ological reactors. The existing aeration tank is divided into anoxic and ae
rated zones, and the nitrifying Biocubes are introduced in the aerated one.
Such an upgraded activated sludge system (which did not nitrify before the
upgrading) can reach a maximum eliminated loading rate of 0.5 kg NH4-N per
m(3) of aerated volume per day at 12 degrees C. This solution was used to
upgrade the 120,000 p.e. Bellozanne Sewage Treatment Works, Jersey, Channel
Islands, UK. When an existing high rate activated sludge plant is designed
for a HRT of less than five hours, the activated sludge tank can be transf
ormed into a high-rate denitrifying anoxic reactor, coupled to a nitrifying
Biofor up-flow filter. The high-rate anoxic sludge is continuously control
led by an ORP probe in order to ensure both the denitrifying conditions and
recycle ratios are at their optimum level. This controlled operation and h
igh water velocities applied to the nitrifying up-flow Biofor enable the op
erational mode to switch from dry weather conditions to wet weather conditi
ons where the recycle of nitrified liquor is switched off and the high load
ed anoxic sludge is temporarily aerated.