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Stable performance of non‐aerated two‐stage partial nitritation/anammox (PANAM) with minimal process control

Partial nitritation/anammox (PANAM) technologies have rapidly developed over the last decade, but still considerable amounts of energy are required for active aeration. In this study, a non‐aerated two‐stage PANAM process was investigated. In the first‐stage upflow fixed‐film bioreactor, nitratation...

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Detalles Bibliográficos
Autores principales: Bagchi, Samik, Biswas, Rima, Vlaeminck, Siegfried E., Roychoudhury, Kunal, Nandy, Tapas
Formato: Online Artículo Texto
Lenguaje:English
Publicado: Blackwell Publishing Ltd 2012
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC3821685/
https://www.ncbi.nlm.nih.gov/pubmed/22414169
http://dx.doi.org/10.1111/j.1751-7915.2012.00336.x
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author Bagchi, Samik
Biswas, Rima
Vlaeminck, Siegfried E.
Roychoudhury, Kunal
Nandy, Tapas
author_facet Bagchi, Samik
Biswas, Rima
Vlaeminck, Siegfried E.
Roychoudhury, Kunal
Nandy, Tapas
author_sort Bagchi, Samik
collection PubMed
description Partial nitritation/anammox (PANAM) technologies have rapidly developed over the last decade, but still considerable amounts of energy are required for active aeration. In this study, a non‐aerated two‐stage PANAM process was investigated. In the first‐stage upflow fixed‐film bioreactor, nitratation could not be prevented at ammonium loading rates up to 186 mg N l(−1) d(−1) and low influent dissolved oxygen (0.1 mg O(2) l(−1)). Yet, increasing the loading rate to 416 and 747 mg N l(−1) d(−1) by decreasing the hydraulic retention time to 8 and 5 h, respectively, resulted in partial nitritation with the desired nitrite to ammonium nitrogen ratio for the subsequent anammox stage (0.71–1.05). The second‐stage anammox reactor was established with a synthetic feeding based on ammonium and nitrite. After establishing anammox at low biomass content (0.5 g VSS l(−1)), the anammox influent was switched to partial nitritation effluent at a loading rate of 71 mg N l(−1) d(−1), of which 78% was removed at the stoichiometrically expected nitrite to ammonium consumption ratios (1.19) and nitrate production to ammonium consumption ratio (0.24). The combined PANAM reactors were operated for 3 months at a stable performance. Overall, PANAM appeals economically, saving about 50% of the energy costs, as well as technically, given straightforward operational principles.
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spelling pubmed-38216852014-02-12 Stable performance of non‐aerated two‐stage partial nitritation/anammox (PANAM) with minimal process control Bagchi, Samik Biswas, Rima Vlaeminck, Siegfried E. Roychoudhury, Kunal Nandy, Tapas Microb Biotechnol Research Articles Partial nitritation/anammox (PANAM) technologies have rapidly developed over the last decade, but still considerable amounts of energy are required for active aeration. In this study, a non‐aerated two‐stage PANAM process was investigated. In the first‐stage upflow fixed‐film bioreactor, nitratation could not be prevented at ammonium loading rates up to 186 mg N l(−1) d(−1) and low influent dissolved oxygen (0.1 mg O(2) l(−1)). Yet, increasing the loading rate to 416 and 747 mg N l(−1) d(−1) by decreasing the hydraulic retention time to 8 and 5 h, respectively, resulted in partial nitritation with the desired nitrite to ammonium nitrogen ratio for the subsequent anammox stage (0.71–1.05). The second‐stage anammox reactor was established with a synthetic feeding based on ammonium and nitrite. After establishing anammox at low biomass content (0.5 g VSS l(−1)), the anammox influent was switched to partial nitritation effluent at a loading rate of 71 mg N l(−1) d(−1), of which 78% was removed at the stoichiometrically expected nitrite to ammonium consumption ratios (1.19) and nitrate production to ammonium consumption ratio (0.24). The combined PANAM reactors were operated for 3 months at a stable performance. Overall, PANAM appeals economically, saving about 50% of the energy costs, as well as technically, given straightforward operational principles. Blackwell Publishing Ltd 2012-05 2012-04-16 /pmc/articles/PMC3821685/ /pubmed/22414169 http://dx.doi.org/10.1111/j.1751-7915.2012.00336.x Text en Copyright © 2012 The Authors. Microbial Biotechnology © 2012 Society for Applied Microbiology and Blackwell Publishing Ltd
spellingShingle Research Articles
Bagchi, Samik
Biswas, Rima
Vlaeminck, Siegfried E.
Roychoudhury, Kunal
Nandy, Tapas
Stable performance of non‐aerated two‐stage partial nitritation/anammox (PANAM) with minimal process control
title Stable performance of non‐aerated two‐stage partial nitritation/anammox (PANAM) with minimal process control
title_full Stable performance of non‐aerated two‐stage partial nitritation/anammox (PANAM) with minimal process control
title_fullStr Stable performance of non‐aerated two‐stage partial nitritation/anammox (PANAM) with minimal process control
title_full_unstemmed Stable performance of non‐aerated two‐stage partial nitritation/anammox (PANAM) with minimal process control
title_short Stable performance of non‐aerated two‐stage partial nitritation/anammox (PANAM) with minimal process control
title_sort stable performance of non‐aerated two‐stage partial nitritation/anammox (panam) with minimal process control
topic Research Articles
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC3821685/
https://www.ncbi.nlm.nih.gov/pubmed/22414169
http://dx.doi.org/10.1111/j.1751-7915.2012.00336.x
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