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Nitrogen Removal from Milking Center Wastewater via Simultaneous Nitrification and Denitrification Using a Biofilm Filtration Reactor

Milking center wastewater (MCW) has a relatively low ratio of carbon to nitrogen (C/N ratio), which should be separately managed from livestock manure due to the negative impacts of manure nutrients and harmful effects on down-stream in the livestock manure process with respect to the microbial grow...

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Autores principales: Won, Seung-Gun, Jeon, Dae-Yong, Kwag, Jung-Hoon, Kim, Jeong-Dae, Ra, Chang-Six
Formato: Online Artículo Texto
Lenguaje:English
Publicado: Asian-Australasian Association of Animal Production Societies (AAAP) and Korean Society of Animal Science and Technology (KSAST) 2015
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC4412987/
https://www.ncbi.nlm.nih.gov/pubmed/25925067
http://dx.doi.org/10.5713/ajas.14.0839
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author Won, Seung-Gun
Jeon, Dae-Yong
Kwag, Jung-Hoon
Kim, Jeong-Dae
Ra, Chang-Six
author_facet Won, Seung-Gun
Jeon, Dae-Yong
Kwag, Jung-Hoon
Kim, Jeong-Dae
Ra, Chang-Six
author_sort Won, Seung-Gun
collection PubMed
description Milking center wastewater (MCW) has a relatively low ratio of carbon to nitrogen (C/N ratio), which should be separately managed from livestock manure due to the negative impacts of manure nutrients and harmful effects on down-stream in the livestock manure process with respect to the microbial growth. Simultaneous nitrification and denitrification (SND) is linked to inhibition of the second nitrification and reduces around 40% of the carbonaceous energy available for denitrification. Thus, this study was conducted to find the optimal operational conditions for the treatment of MCW using an attached-growth biofilm reactor; i.e., nitrogen loading rate (NLR) of 0.14, 0.28, 0.43, and 0.58 kg m(−3) d(−1) and aeration rate of 0.06, 0.12, and 0.24 m(3) h(−1) were evaluated and the comparison of air-diffuser position between one-third and bottom of the reactor was conducted. Four sand packed-bed reactors with the effective volume of 2.5 L were prepared and initially an air-diffuser was placed at one third from the bottom of the reactor. After the adaptation period of 2 weeks, SND was observed at all four reactors and the optimal NLR of 0.45 kg m(−3) d(−1) was found as a threshold value to obtain higher nitrogen removal efficiency. Dissolved oxygen (DO) as one of key operational conditions was measured during the experiment and the reactor with an aeration rate of 0.12 m(3) h(−1) showed the best performance of NH(4)-N removal and the higher total nitrogen removal efficiency through SND with appropriate DO level of ~0.5 mg DO L(−1). The air-diffuser position at one third from the bottom of the reactor resulted in better nitrogen removal than at the bottom position. Consequently, nitrogen in MCW with a low C/N ratio of 2.15 was successfully removed without the addition of external carbon sources.
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spelling pubmed-44129872015-06-01 Nitrogen Removal from Milking Center Wastewater via Simultaneous Nitrification and Denitrification Using a Biofilm Filtration Reactor Won, Seung-Gun Jeon, Dae-Yong Kwag, Jung-Hoon Kim, Jeong-Dae Ra, Chang-Six Asian-Australas J Anim Sci Article Milking center wastewater (MCW) has a relatively low ratio of carbon to nitrogen (C/N ratio), which should be separately managed from livestock manure due to the negative impacts of manure nutrients and harmful effects on down-stream in the livestock manure process with respect to the microbial growth. Simultaneous nitrification and denitrification (SND) is linked to inhibition of the second nitrification and reduces around 40% of the carbonaceous energy available for denitrification. Thus, this study was conducted to find the optimal operational conditions for the treatment of MCW using an attached-growth biofilm reactor; i.e., nitrogen loading rate (NLR) of 0.14, 0.28, 0.43, and 0.58 kg m(−3) d(−1) and aeration rate of 0.06, 0.12, and 0.24 m(3) h(−1) were evaluated and the comparison of air-diffuser position between one-third and bottom of the reactor was conducted. Four sand packed-bed reactors with the effective volume of 2.5 L were prepared and initially an air-diffuser was placed at one third from the bottom of the reactor. After the adaptation period of 2 weeks, SND was observed at all four reactors and the optimal NLR of 0.45 kg m(−3) d(−1) was found as a threshold value to obtain higher nitrogen removal efficiency. Dissolved oxygen (DO) as one of key operational conditions was measured during the experiment and the reactor with an aeration rate of 0.12 m(3) h(−1) showed the best performance of NH(4)-N removal and the higher total nitrogen removal efficiency through SND with appropriate DO level of ~0.5 mg DO L(−1). The air-diffuser position at one third from the bottom of the reactor resulted in better nitrogen removal than at the bottom position. Consequently, nitrogen in MCW with a low C/N ratio of 2.15 was successfully removed without the addition of external carbon sources. Asian-Australasian Association of Animal Production Societies (AAAP) and Korean Society of Animal Science and Technology (KSAST) 2015-06 /pmc/articles/PMC4412987/ /pubmed/25925067 http://dx.doi.org/10.5713/ajas.14.0839 Text en Copyright © 2015 by Asian-Australasian Journal of Animal Sciences This is an open-access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/by-nc/3.0/), wwhich permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
spellingShingle Article
Won, Seung-Gun
Jeon, Dae-Yong
Kwag, Jung-Hoon
Kim, Jeong-Dae
Ra, Chang-Six
Nitrogen Removal from Milking Center Wastewater via Simultaneous Nitrification and Denitrification Using a Biofilm Filtration Reactor
title Nitrogen Removal from Milking Center Wastewater via Simultaneous Nitrification and Denitrification Using a Biofilm Filtration Reactor
title_full Nitrogen Removal from Milking Center Wastewater via Simultaneous Nitrification and Denitrification Using a Biofilm Filtration Reactor
title_fullStr Nitrogen Removal from Milking Center Wastewater via Simultaneous Nitrification and Denitrification Using a Biofilm Filtration Reactor
title_full_unstemmed Nitrogen Removal from Milking Center Wastewater via Simultaneous Nitrification and Denitrification Using a Biofilm Filtration Reactor
title_short Nitrogen Removal from Milking Center Wastewater via Simultaneous Nitrification and Denitrification Using a Biofilm Filtration Reactor
title_sort nitrogen removal from milking center wastewater via simultaneous nitrification and denitrification using a biofilm filtration reactor
topic Article
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC4412987/
https://www.ncbi.nlm.nih.gov/pubmed/25925067
http://dx.doi.org/10.5713/ajas.14.0839
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