High-throughput nitritation of reject water with a novel ammonium control loop

This work presents a new control system for the nitritation of high-strength ammonium wastewater as reject water from sludge dewatering. It is based on three independent feedback control loops: (i) DO control by manipulating the aeration flow-rate, (ii) pH control with the addition of solid Na₂CO₃ a...

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Detalles Bibliográficos
Autores: Torà Suárez, Josep Anton|||0000-0003-3704-1933, Lafuente Sancho, Francisco Javier|||0000-0002-4601-9001, Garcia-Belinchón, Carme|||0000-0001-9697-9273, Bouchy, Lynne, Carrera, Julian|||0000-0002-2599-2312, Baeza, Juan Antonio|||0000-0003-1290-1669
Tipo de recurso: artículo
Fecha de publicación:2014
País:España
Institución:Universitat Autònoma de Barcelona
Repositorio:Dipòsit Digital de Documents de la UAB
Idioma:inglés
OAI Identifier:oai:ddd.uab.cat:169684
Acceso en línea:https://ddd.uab.cat/record/169684
https://dx.doi.org/urn:doi:10.1016/j.cej.2013.11.056
Access Level:acceso abierto
Palabra clave:Anammox
AOB
Control
Partial nitrification
Nitritation
TAN
Descripción
Sumario:This work presents a new control system for the nitritation of high-strength ammonium wastewater as reject water from sludge dewatering. It is based on three independent feedback control loops: (i) DO control by manipulating the aeration flow-rate, (ii) pH control with the addition of solid Na₂CO₃ and (iii) control of NH₄+-N concentration in the reactor using the influent flow-rate as the manipulated variable. Its application in an activated sludge configuration with one reactor and a settler, demonstrated: (i) capability to achieve stable effluent composition with proper NO₂-N/NH₄+-N ratio for anammox treatment and ii) possibility to obtain an effluent with full nitritation suitable for heterotrophic denitrification only modifying the ammonium setpoint. A nitrogen loading rate (NLR) up to 5.0 ± 1.0 gN L⁻¹ d⁻¹ was stably treated using real reject water (T = 30ºC, pH = 7.5) with a NO₂-N/(NO₂-N+NO₃-N) ratio of 99%. NLR reached up to 9.3 ± 0.5 gN L⁻¹ d⁻¹ with synthetic wastewater.