In this paper a mathematical steady-state model for the design of the pre-denitrification system is proposed. This model takes into account four substrates (soluble and particulate biodegradable organic matter, ammonia nitrogen and nitrate nitrogen) and extends a previous version proposed by Esposito et al. (2003), considering the biomass decay. This tool makes it possible: i) to define the applicability of the pre-denitrification system; ii) to solve completely the design problem, with explicit expressions of the biological reactor volumes. Model applications show the increase of the oxidation phase volume, which is necessary either to face a higher influent organic load or to achieve a higher nitrogen ammonia removal.

A Design Tool for the Predenitrification Systems / Esposito, G.; Fabbricino, Massimiliano; Pirozzi, Francesco; Lens, P.. - STAMPA. - (2003), pp. 183-186. (Intervento presentato al convegno IWA International Conference on Design, Operation and Economics of Large Wastewater Tretment Plants tenutosi a Prague (CZECH REPUBLIC) nel 1-4 September).

A Design Tool for the Predenitrification Systems

FABBRICINO, MASSIMILIANO;PIROZZI, FRANCESCO;
2003

Abstract

In this paper a mathematical steady-state model for the design of the pre-denitrification system is proposed. This model takes into account four substrates (soluble and particulate biodegradable organic matter, ammonia nitrogen and nitrate nitrogen) and extends a previous version proposed by Esposito et al. (2003), considering the biomass decay. This tool makes it possible: i) to define the applicability of the pre-denitrification system; ii) to solve completely the design problem, with explicit expressions of the biological reactor volumes. Model applications show the increase of the oxidation phase volume, which is necessary either to face a higher influent organic load or to achieve a higher nitrogen ammonia removal.
2003
A Design Tool for the Predenitrification Systems / Esposito, G.; Fabbricino, Massimiliano; Pirozzi, Francesco; Lens, P.. - STAMPA. - (2003), pp. 183-186. (Intervento presentato al convegno IWA International Conference on Design, Operation and Economics of Large Wastewater Tretment Plants tenutosi a Prague (CZECH REPUBLIC) nel 1-4 September).
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11588/184799
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