Biological nitrogen removal over nitritation/denitritation using phenol as carbon source

A laboratory scale activated sludge sequencing batch reactor was operated in order to obtain total removal of influent ammonia (200; 300 and 500 mg NH3-N.L-1) with sustained nitrite accumulation at the end of the aerobic stages with phenol (1,000 mg C6H5OH.L-1) as the carbon source for denitrifying microorganisms during the anoxic stages. Ammonia removal above 95% and ratios of (NO2--N / (NO2--N + NO3--N)) ranging from 89 to 99% were obtained by controlling the dissolved oxygen concentration (1.0 mg O2.L-1) and the pH value of 8.3 during the aerobic stages. Phenol proved to be an adequate source of carbon for nitrogen removal via nitrite with continuous feeding throughout part of the anoxic stage. Nitrite concentrations greater than 70.0 mg NO2--N.L-1 inhibited the biological denitritation process.

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Main Authors: Queiroz,L. M., Aun,M. V., Morita,D. M., Alem Sobrinho,P.
Format: Digital revista
Language:English
Published: Brazilian Society of Chemical Engineering 2011
Online Access:http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322011000200004
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spelling oai:scielo:S0104-663220110002000042011-07-04Biological nitrogen removal over nitritation/denitritation using phenol as carbon sourceQueiroz,L. M.Aun,M. V.Morita,D. M.Alem Sobrinho,P. Ammonia Phenol Nitritation Denitritation A laboratory scale activated sludge sequencing batch reactor was operated in order to obtain total removal of influent ammonia (200; 300 and 500 mg NH3-N.L-1) with sustained nitrite accumulation at the end of the aerobic stages with phenol (1,000 mg C6H5OH.L-1) as the carbon source for denitrifying microorganisms during the anoxic stages. Ammonia removal above 95% and ratios of (NO2--N / (NO2--N + NO3--N)) ranging from 89 to 99% were obtained by controlling the dissolved oxygen concentration (1.0 mg O2.L-1) and the pH value of 8.3 during the aerobic stages. Phenol proved to be an adequate source of carbon for nitrogen removal via nitrite with continuous feeding throughout part of the anoxic stage. Nitrite concentrations greater than 70.0 mg NO2--N.L-1 inhibited the biological denitritation process.info:eu-repo/semantics/openAccessBrazilian Society of Chemical EngineeringBrazilian Journal of Chemical Engineering v.28 n.2 20112011-06-01info:eu-repo/semantics/articletext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322011000200004en10.1590/S0104-66322011000200004
institution SCIELO
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country Brasil
countrycode BR
component Revista
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region America del Sur
libraryname SciELO
language English
format Digital
author Queiroz,L. M.
Aun,M. V.
Morita,D. M.
Alem Sobrinho,P.
spellingShingle Queiroz,L. M.
Aun,M. V.
Morita,D. M.
Alem Sobrinho,P.
Biological nitrogen removal over nitritation/denitritation using phenol as carbon source
author_facet Queiroz,L. M.
Aun,M. V.
Morita,D. M.
Alem Sobrinho,P.
author_sort Queiroz,L. M.
title Biological nitrogen removal over nitritation/denitritation using phenol as carbon source
title_short Biological nitrogen removal over nitritation/denitritation using phenol as carbon source
title_full Biological nitrogen removal over nitritation/denitritation using phenol as carbon source
title_fullStr Biological nitrogen removal over nitritation/denitritation using phenol as carbon source
title_full_unstemmed Biological nitrogen removal over nitritation/denitritation using phenol as carbon source
title_sort biological nitrogen removal over nitritation/denitritation using phenol as carbon source
description A laboratory scale activated sludge sequencing batch reactor was operated in order to obtain total removal of influent ammonia (200; 300 and 500 mg NH3-N.L-1) with sustained nitrite accumulation at the end of the aerobic stages with phenol (1,000 mg C6H5OH.L-1) as the carbon source for denitrifying microorganisms during the anoxic stages. Ammonia removal above 95% and ratios of (NO2--N / (NO2--N + NO3--N)) ranging from 89 to 99% were obtained by controlling the dissolved oxygen concentration (1.0 mg O2.L-1) and the pH value of 8.3 during the aerobic stages. Phenol proved to be an adequate source of carbon for nitrogen removal via nitrite with continuous feeding throughout part of the anoxic stage. Nitrite concentrations greater than 70.0 mg NO2--N.L-1 inhibited the biological denitritation process.
publisher Brazilian Society of Chemical Engineering
publishDate 2011
url http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322011000200004
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