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Nitrogen removal in multi-stage wastewater treatment plants by using a modified post-denitrification system
Affiliation:1. Department of Environment and Planning, University of Aveiro, Campus Universitário de Santiago, 3810-193 Aveiro, Portugal;2. GOVCOPP, Investigation Unit for Governance, Competitiveness and Public Policy, Portugal;3. Department of Economy, Management and Industrial Engineering, University of Aveiro, Campus Universitário de Santiago, 3810-193 Aveiro, Portugal;4. CESAM, Centre for Environmental and Marine Studies, Portugal;1. Laboratoire de Virologie, Hôpitaux Universitaires de Strasbourg, Strasbourg, France;2. INSERM, UMR_S1109, LabEx TRANSPLANTEX, Centre de Recherche d''Immunologie et d''Hématologie, Faculté de Médecine, Fédération Hospitalo-Universitaire (FHU) OMICARE, Fédération de Médecine Translationnelle de Strasbourg (FMTS), Université de Strasbourg, Strasbourg, France;3. Service des Maladies Infectieuses et Tropicales, Hôpitaux Universitaires de Strasbourg, Strasbourg, France;4. Département d''Anesthésie et Réanimation Chirurgicale, Hôpitaux Universitaires de Strasbourg, Strasbourg, France;5. Centre d''Investigation Clinique INSERM CIC-1434, Hôpitaux Universitaires de Strasbourg, Strasbourg, France;6. Département de Médecine Intensive-Réanimation, Hôpitaux Universitaires de Strasbourg, Strasbourg, France;7. Département des Urgences Médicales, Hôpitaux Universitaires de Strasbourg, Strasbourg, France;8. Service de Médecine Intensive-Réanimation, Hôpitaux Universitaires de Strasbourg, Strasbourg, France;9. INSERM, UMR 1260, Regenerative Nanomedicine (RNM), FMTS, Strasbourg, France
Abstract:Systems in which denitrification follows nitrification (post-denitrification) copy the natural sequence of nitrogen removal. The disadvantage of post-denitrification, however, is that an external carbon source must be added to the denitrification reactor. In the concept discussed in this paper, excess sludge from a high loaded activated sludge plant is used as carbon source and as source of denitrifiers in a three-stage system. The sludge is fed into a anoxic reactor placed in between the nitrification reactor (e.g., trickling filter) and the final clarifier. Two different operation methods were investigated at a pilot-scale system set up at the Ingolstadt wastewater treatment plant Low nitrate effluent values were obtained at high sludge feeding rates, but at the expense of a significant increase in turbidity and NH4-N effluent concentrations. This problem could be solved by a reduction of the sludge feeding rate and by applying intermittent feeding. The effluent turbidity was kept at an acceptable level, but denitrification was relatively slow in progress. To achieve both low effluent turbidity and low nitrate discharge, a combination of pre- and post-denitrification is recommended.
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