Feasibility of hydraulic separation in a novel anaerobic-anoxic upflow reactor for biological nutrient removal
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Díez Montero, Rubén


Fecha
2014-07-08Derechos
© Springer “The final publication is available at Springer via http://dx.doi.org/10.1007/s00449-014-1247-9"
Publicado en
Bioprocess and Biosystems Engineering , Vol. 38, No. 1 (July 2014), p. 93-103
Editorial
Springer
Enlace a la publicación
Palabras clave
Wastewater treatment
Denitrification
Tracer tests
Hydrodynamic behaviour
Mathematical modelling
Numerical simulation
Resumen/Abstract
ABSTRACT : This contribution deals with a novel anaerobic-anoxic reactor for biological nutrient removal (BNR) from wastewater, termed AnoxAn. In the AnoxAn reactor, the anaerobic and anoxic zones for phosphate removal and denitrification are integrated in a single continuous upflow sludge blanket reactor, aiming at high compactness and efficiency. Its application is envisaged in those cases where retrofitting of existing wastewater treatment plants for BNR, or the construction of new ones, is limited by the available surface area. The environmental conditions are vertically divided up inside the reactor with the anaerobic zone at the bottom and the anoxic zone above. The capability of the AnoxAn configuration to establish two hydraulically separated zones inside the single reactor was assessed by means of hydraulic characterization experiments and model simulations. Residence time distribution (RTD) experiments in clean water were performed in a bench-scale (48.4 L) AnoxAn prototype. The required hydraulic separation between the anaerobic and anoxic zones, as well as adequate mixing in the individual zones, was obtained through selected mixing devices. The observed behaviour was described by a hydraulic model consisting of continuous stirred tank reactors and plug-flow reactors. The impact of the denitrification process in the anoxic zone on the hydraulic separation was subsequently evaluated through model simulations. The desired hydraulic behaviour proved feasible, involving little mixing between the anaerobic and anoxic zones (mixing flowrate 40.2% of influent flowrate) and negligible nitrate concentration in the anaerobic zone (less than 0.1 mgN L-1) when denitrification was considered.
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