Technical solutions for upgrading high rate and medium loaded activated sludge plants for nutrient removal

Citation
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
Citations number
10
Categorie Soggetti
Environment/Ecology
Journal title
WATER SCIENCE AND TECHNOLOGY
ISSN journal
02731223 → ACNP
Volume
41
Issue
9
Year of publication
2000
Pages
131 - 138
Database
ISI
SICI code
0273-1223(2000)41:9<131:TSFUHR>2.0.ZU;2-B
Abstract
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.