The University of Southampton
University of Southampton Institutional Repository

Addition of an external carbon source to enhance nitrogen biological removal in the treatment of liquid industrial wastes

Addition of an external carbon source to enhance nitrogen biological removal in the treatment of liquid industrial wastes
Addition of an external carbon source to enhance nitrogen biological removal in the treatment of liquid industrial wastes
This paper deals with the optimization of biological nitrogen removal in the treatment of liquid industrial wastes. In particular, the use of an external carbon source in a two-step alternate oxic?anoxic process with separate biomass has been investigated. A 4-month experimental work analyzing both carbon and nitrogen removal and enhancing the latter through acetic acid addition as a second step at the beginning of the anoxic phase was performed. Nitrogen mass balance, cycle analysis, and a typical trend of dissolved oxygen and oxidation reduction potential (ORP) are used as tools to evaluate the success of the method and to understand the exact role of the two steps and the effect of carbon addition. The approach to using a two-step treatment with separate biomass does not reveal satisfactory performances in nitrogen removal if the nitrification is mainly confined to the second step, because enough carbon is not always available. The implementation with an external carbon source allowed a high performance and showed a typical flex point in the ORP trend. The comparison among ORP slopes does not produce any way to estimate the carbon addition: on the other hand, a useful tool for saving on managing cost can be the carbon addition when it is clear that the ORP does not reach a 0 mV level in a prefixed time, after the anoxic phase has started. All N-oxide (NOx?N) concentrations in the effluent have been rationalized in a mass balance for nitrogen providing a prevision of the final effluent quality in relation to the process performances.
0888-5885
2805-2811
Battistoni, Paolo
3ae7cd29-ddef-43c5-856a-626ea37bd75e
Boccadoro, Raffaella
cfe5777f-414a-4eb9-9b33-5bfa4a72ea1c
Innocenti, Laura
ed26ec55-5d54-4f6b-836d-92d3fe75b71e
Bolzonella, David
4d19a164-6356-42c5-a20e-603591a56e4e
Battistoni, Paolo
3ae7cd29-ddef-43c5-856a-626ea37bd75e
Boccadoro, Raffaella
cfe5777f-414a-4eb9-9b33-5bfa4a72ea1c
Innocenti, Laura
ed26ec55-5d54-4f6b-836d-92d3fe75b71e
Bolzonella, David
4d19a164-6356-42c5-a20e-603591a56e4e

Battistoni, Paolo, Boccadoro, Raffaella, Innocenti, Laura and Bolzonella, David (2002) Addition of an external carbon source to enhance nitrogen biological removal in the treatment of liquid industrial wastes. Industrial & Engineering Chemistry Research, 41 (11), 2805-2811. (doi:10.1021/ie010828+).

Record type: Article

Abstract

This paper deals with the optimization of biological nitrogen removal in the treatment of liquid industrial wastes. In particular, the use of an external carbon source in a two-step alternate oxic?anoxic process with separate biomass has been investigated. A 4-month experimental work analyzing both carbon and nitrogen removal and enhancing the latter through acetic acid addition as a second step at the beginning of the anoxic phase was performed. Nitrogen mass balance, cycle analysis, and a typical trend of dissolved oxygen and oxidation reduction potential (ORP) are used as tools to evaluate the success of the method and to understand the exact role of the two steps and the effect of carbon addition. The approach to using a two-step treatment with separate biomass does not reveal satisfactory performances in nitrogen removal if the nitrification is mainly confined to the second step, because enough carbon is not always available. The implementation with an external carbon source allowed a high performance and showed a typical flex point in the ORP trend. The comparison among ORP slopes does not produce any way to estimate the carbon addition: on the other hand, a useful tool for saving on managing cost can be the carbon addition when it is clear that the ORP does not reach a 0 mV level in a prefixed time, after the anoxic phase has started. All N-oxide (NOx?N) concentrations in the effluent have been rationalized in a mass balance for nitrogen providing a prevision of the final effluent quality in relation to the process performances.

This record has no associated files available for download.

More information

Published date: 30 April 2002

Identifiers

Local EPrints ID: 189031
URI: http://eprints.soton.ac.uk/id/eprint/189031
ISSN: 0888-5885
PURE UUID: c4686dc7-1f3a-4ac9-b326-c7582ff956fc

Catalogue record

Date deposited: 15 Jun 2011 12:00
Last modified: 14 Mar 2024 03:34

Export record

Altmetrics

Contributors

Author: Paolo Battistoni
Author: Raffaella Boccadoro
Author: Laura Innocenti
Author: David Bolzonella

Download statistics

Downloads from ePrints over the past year. Other digital versions may also be available to download e.g. from the publisher's website.

View more statistics

Atom RSS 1.0 RSS 2.0

Contact ePrints Soton: eprints@soton.ac.uk

ePrints Soton supports OAI 2.0 with a base URL of http://eprints.soton.ac.uk/cgi/oai2

This repository has been built using EPrints software, developed at the University of Southampton, but available to everyone to use.

We use cookies to ensure that we give you the best experience on our website. If you continue without changing your settings, we will assume that you are happy to receive cookies on the University of Southampton website.

×