Upgrading of a wastewater treatment plant with a hybrid moving bed biofilm reactor (MBBR)
The wastewater treatment plant of Porto Tolle (RO, Italy) was originally projected for 2200 person equivalent (p.e.) and it was made of a pumping station, an activated sludge oxidation tank (395 m3), a settler (315 m3), and two sludge drying beds. Other units were not yet in use in 2008: a fine sc...
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doaj-0dc5c6ee827c45349a138f9e76bbdef92020-11-25T01:12:34ZengAIMS PressAIMS Environmental Science2372-03442372-03522014-11-0112455210.3934/environsci.2014.2.45Upgrading of a wastewater treatment plant with a hybrid moving bed biofilm reactor (MBBR)Luigi Falletti0Lino Conte1Andrea Maestri2Department of Industrial Engineering, University of Padova, via Marzolo 9–35127 Padova, ItalyDepartment of Industrial Engineering, University of Padova, via Marzolo 9–35127 Padova, ItalyPolesine Acque SpA, via B. Tisi da Garofolo 11–45100 Rovigo, ItalyThe wastewater treatment plant of Porto Tolle (RO, Italy) was originally projected for 2200 person equivalent (p.e.) and it was made of a pumping station, an activated sludge oxidation tank (395 m3), a settler (315 m3), and two sludge drying beds. Other units were not yet in use in 2008: a fine screen, a sand and grit removal unit, a new settler (570 m3), a disinfection tank and a sludge thickener. Effective hydraulic load was 245% higher, organic load was 46% lower and nitrogen load was 39% higher than project values. Moreover, higher pollutant loads and more strict emission limits for nitrogen were expected. So the plant was upgraded: the old settler was divided into a sector of 180 m3 that was converted into a predenitrification tank, and a sector of 100 m3 that was converted into a hybrid MBBR tank filled with 50% AnoxKaldnesTM K3 carriers; the new settler was connected to the hybrid MBBR, and the other units were started. Biofilm growth was observed two months after plant restarting, its concentration reached 1.1 gTS/m2 (0.26 kgTS/m3), while activated sludge concentration was 2.0–2.8 kgTSS/m3 in all the period of study. The upgraded plant treats 1587 m3/d wastewater with 57 kgCOD/d, 23 kgBOD/d and 13.3 kgN/d, and has a significant residual capacity; the effluent respects all emission limits. http://www.aimspress.com/article/10.3934/environsci.2014.2.45/fulltext.htmlhybrid moving bednitrogenbiofilmactivated sludgewastewater treatmentupgrading |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Luigi Falletti Lino Conte Andrea Maestri |
spellingShingle |
Luigi Falletti Lino Conte Andrea Maestri Upgrading of a wastewater treatment plant with a hybrid moving bed biofilm reactor (MBBR) AIMS Environmental Science hybrid moving bed nitrogen biofilm activated sludge wastewater treatment upgrading |
author_facet |
Luigi Falletti Lino Conte Andrea Maestri |
author_sort |
Luigi Falletti |
title |
Upgrading of a wastewater treatment plant with a hybrid moving bed biofilm reactor (MBBR) |
title_short |
Upgrading of a wastewater treatment plant with a hybrid moving bed biofilm reactor (MBBR) |
title_full |
Upgrading of a wastewater treatment plant with a hybrid moving bed biofilm reactor (MBBR) |
title_fullStr |
Upgrading of a wastewater treatment plant with a hybrid moving bed biofilm reactor (MBBR) |
title_full_unstemmed |
Upgrading of a wastewater treatment plant with a hybrid moving bed biofilm reactor (MBBR) |
title_sort |
upgrading of a wastewater treatment plant with a hybrid moving bed biofilm reactor (mbbr) |
publisher |
AIMS Press |
series |
AIMS Environmental Science |
issn |
2372-0344 2372-0352 |
publishDate |
2014-11-01 |
description |
The wastewater treatment plant of Porto Tolle (RO, Italy) was originally projected for 2200 person equivalent (p.e.) and it was made of a pumping station, an activated sludge oxidation tank
(395 m3), a settler (315 m3), and two sludge drying beds. Other units were not yet in use in 2008: a fine screen, a sand and grit removal unit, a new settler (570 m3), a disinfection tank and a sludge thickener. Effective hydraulic load was 245% higher, organic load was 46% lower and nitrogen load was 39% higher than project values. Moreover, higher pollutant loads and more strict emission limits for nitrogen were expected. So the plant was upgraded: the old settler was divided into a sector of 180 m3 that was converted into a predenitrification tank, and a sector of 100 m3 that was converted into a hybrid MBBR tank filled with 50% AnoxKaldnesTM K3 carriers; the new settler was connected to the hybrid MBBR, and the other units were started. Biofilm growth was observed two months after plant restarting, its concentration reached 1.1 gTS/m2 (0.26 kgTS/m3), while activated sludge concentration was 2.0–2.8 kgTSS/m3 in all the period of study. The upgraded plant treats 1587 m3/d wastewater with 57 kgCOD/d, 23 kgBOD/d and 13.3 kgN/d, and has a significant residual capacity; the effluent respects all emission limits.
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topic |
hybrid moving bed nitrogen biofilm activated sludge wastewater treatment upgrading |
url |
http://www.aimspress.com/article/10.3934/environsci.2014.2.45/fulltext.html |
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