Decentralized two-stage sewage treatment by chemical–biological flocculation combined with microalgae biofilm for nutrient immobilization in a roof installed parallel plate reactor

[Display omitted] ► A two-stage treatment system for domestic wastewater treatment in situ is proposed. ► In the first stage, COD and P are removed by chemical biological adsorption. ► In the second stage, N and P are removed by immobilization in microalgae biomass biofilm. ► Algal biofilm grown in...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Veröffentlicht in:Bioresource technology 2013-02, Vol.130, p.152-160
Hauptverfasser: Zamalloa, Carlos, Boon, Nico, Verstraete, Willy
Format: Artikel
Sprache:eng
Schlagworte:
Online-Zugang:Volltext
Tags: Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
Beschreibung
Zusammenfassung:[Display omitted] ► A two-stage treatment system for domestic wastewater treatment in situ is proposed. ► In the first stage, COD and P are removed by chemical biological adsorption. ► In the second stage, N and P are removed by immobilization in microalgae biomass biofilm. ► Algal biofilm grown in an innovative parallel plate reactor installed on a roof. ► COD and P discharge limits meet EU regulation but N is just below these limits. In this lab-scale study, domestic wastewater is subjected to a chemical biological adsorption (A-stage), followed by treatment in an innovative roof installed parallel plate microalgae biofilm reactor for nutrient immobilization (I-stage). The A-stage process was operated at a hydraulic retention time (HRT) of 1h and a solid retention time of 1day (FeSO4 as flocculant). The I-stage, which consequently received the effluent of the A-stage process, was operated at an HRT of 1day and exposed to natural light. The overall system removed on average 74% of the total chemical oxygen demand, 82% of the total suspended solids, 67% of the total nitrogen and 96% of the total phosphorous in the wastewater. The design involves a relatively low capital and operating cost which is in the order of 0.5€/m3 wastewater treated. These aspects suggest that the A/I process can be used as a decentralized domestic wastewater treatment system.
ISSN:0960-8524
1873-2976
DOI:10.1016/j.biortech.2012.11.128