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Nitrifying trickling filters and denitrifying bioreactors for nitrogen management of high-strength anaerobic digestion effluent

The treatment of high-strength anaerobic digester effluent in laboratory-scale trickling filters for nitrification and then anaerobic filters for denitrification is reported. Five media types were investigated in the trickling filters: biochar, granular activated carbon (GAC), zeolite, Pall rings, a...

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Autores principales: Forbis-Stokes, Aaron A., Rocha-Melogno, Lucas, Deshusses, Marc A.
Formato: Online Artículo Texto
Lenguaje:English
Publicado: Elsevier Science Ltd 2018
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC5953278/
https://www.ncbi.nlm.nih.gov/pubmed/29655104
http://dx.doi.org/10.1016/j.chemosphere.2018.03.137
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author Forbis-Stokes, Aaron A.
Rocha-Melogno, Lucas
Deshusses, Marc A.
author_facet Forbis-Stokes, Aaron A.
Rocha-Melogno, Lucas
Deshusses, Marc A.
author_sort Forbis-Stokes, Aaron A.
collection PubMed
description The treatment of high-strength anaerobic digester effluent in laboratory-scale trickling filters for nitrification and then anaerobic filters for denitrification is reported. Five media types were investigated in the trickling filters: biochar, granular activated carbon (GAC), zeolite, Pall rings, and gravel. Three media were tested in five denitrifying filters: sand (S), bamboo wood chips (B), eucalyptus wood chips (E), bamboo with sand (B+S), and eucalyptus with sand (E+S). The different wood chips served as a supplemental electron donor for denitrification. From six months of operation, biochar, GAC, zeolite, Pall rings, and gravel media had turbidity (NTU) removal efficiencies of 90, 91, 77, 74, and 74%, respectively, and ammonia removal efficiencies of 83, 87, 85, 30, and 80%, respectively, which was primarily by nitrification to nitrate. For the anaerobic filters, S, B, B+S, E, and E+S had nitrate removal efficiencies of 30, 66, 53, 35, and 35%, and turbidity removal efficiencies of 88, 89, 84, 89, and 88%, respectively. Biochar and bamboo were selected as the best combination of media for trickling filter and anaerobic filter sequential treatment. Based on an average initial influent of 600 mg NH(3)-N L(−1), 50 mg NO(3)-N L(−1), and 980 NTU, the biochar filter's effluent would be 97 mg NH(3)-N L(−1), 475 mg NO(3)-N L(−1), and 120 NTU. The bamboo filter's final effluent would be 82 mg NH(3)-N L(−1), 157 mg NO(3)-N L(−1), and 13 NTU, which corresponds to 63% removal of total N and 99% removal of turbidity. These filter media thus present a simple option for sustainable post-treatment for nitrogen management and effluent polishing in low-resources settings.
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spelling pubmed-59532782018-08-01 Nitrifying trickling filters and denitrifying bioreactors for nitrogen management of high-strength anaerobic digestion effluent Forbis-Stokes, Aaron A. Rocha-Melogno, Lucas Deshusses, Marc A. Chemosphere Article The treatment of high-strength anaerobic digester effluent in laboratory-scale trickling filters for nitrification and then anaerobic filters for denitrification is reported. Five media types were investigated in the trickling filters: biochar, granular activated carbon (GAC), zeolite, Pall rings, and gravel. Three media were tested in five denitrifying filters: sand (S), bamboo wood chips (B), eucalyptus wood chips (E), bamboo with sand (B+S), and eucalyptus with sand (E+S). The different wood chips served as a supplemental electron donor for denitrification. From six months of operation, biochar, GAC, zeolite, Pall rings, and gravel media had turbidity (NTU) removal efficiencies of 90, 91, 77, 74, and 74%, respectively, and ammonia removal efficiencies of 83, 87, 85, 30, and 80%, respectively, which was primarily by nitrification to nitrate. For the anaerobic filters, S, B, B+S, E, and E+S had nitrate removal efficiencies of 30, 66, 53, 35, and 35%, and turbidity removal efficiencies of 88, 89, 84, 89, and 88%, respectively. Biochar and bamboo were selected as the best combination of media for trickling filter and anaerobic filter sequential treatment. Based on an average initial influent of 600 mg NH(3)-N L(−1), 50 mg NO(3)-N L(−1), and 980 NTU, the biochar filter's effluent would be 97 mg NH(3)-N L(−1), 475 mg NO(3)-N L(−1), and 120 NTU. The bamboo filter's final effluent would be 82 mg NH(3)-N L(−1), 157 mg NO(3)-N L(−1), and 13 NTU, which corresponds to 63% removal of total N and 99% removal of turbidity. These filter media thus present a simple option for sustainable post-treatment for nitrogen management and effluent polishing in low-resources settings. Elsevier Science Ltd 2018-08 /pmc/articles/PMC5953278/ /pubmed/29655104 http://dx.doi.org/10.1016/j.chemosphere.2018.03.137 Text en © 2018 The Authors http://creativecommons.org/licenses/by/4.0/ This is an open access article under the CC BY license (http://creativecommons.org/licenses/by/4.0/).
spellingShingle Article
Forbis-Stokes, Aaron A.
Rocha-Melogno, Lucas
Deshusses, Marc A.
Nitrifying trickling filters and denitrifying bioreactors for nitrogen management of high-strength anaerobic digestion effluent
title Nitrifying trickling filters and denitrifying bioreactors for nitrogen management of high-strength anaerobic digestion effluent
title_full Nitrifying trickling filters and denitrifying bioreactors for nitrogen management of high-strength anaerobic digestion effluent
title_fullStr Nitrifying trickling filters and denitrifying bioreactors for nitrogen management of high-strength anaerobic digestion effluent
title_full_unstemmed Nitrifying trickling filters and denitrifying bioreactors for nitrogen management of high-strength anaerobic digestion effluent
title_short Nitrifying trickling filters and denitrifying bioreactors for nitrogen management of high-strength anaerobic digestion effluent
title_sort nitrifying trickling filters and denitrifying bioreactors for nitrogen management of high-strength anaerobic digestion effluent
topic Article
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC5953278/
https://www.ncbi.nlm.nih.gov/pubmed/29655104
http://dx.doi.org/10.1016/j.chemosphere.2018.03.137
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