Simultaneous Partial Nitrification and Denitrification Maintained in Membrane Bioreactor for Nitrogen Removal and Hydrogen Autotrophic Denitrification for Further Treatment

Low C/N wastewater results from a wide range of factors that significantly harm the environment. They include insufficient carbon sources, low denitrification efficiency, and <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semanti...

Full description

Bibliographic Details
Main Authors: Kun Dong, Xinghui Feng, Wubin Wang, Yuchao Chen, Wei Hu, Haixiang Li, Dunqiu Wang
Format: Article
Language:English
Published: MDPI AG 2021-11-01
Series:Membranes
Subjects:
Online Access:https://www.mdpi.com/2077-0375/11/12/911
_version_ 1827671235907026944
author Kun Dong
Xinghui Feng
Wubin Wang
Yuchao Chen
Wei Hu
Haixiang Li
Dunqiu Wang
author_facet Kun Dong
Xinghui Feng
Wubin Wang
Yuchao Chen
Wei Hu
Haixiang Li
Dunqiu Wang
author_sort Kun Dong
collection DOAJ
description Low C/N wastewater results from a wide range of factors that significantly harm the environment. They include insufficient carbon sources, low denitrification efficiency, and <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><msubsup><mrow><mi>NH</mi></mrow><mn>4</mn><mo>+</mo></msubsup></semantics></math></inline-formula>-N concentrations in low C/N wastewater that are too high to be treated. In this research, the membrane biofilm reactor and hydrogen-based membrane biofilm reactor (MBR-MBfR) were optimized and regulated under different operating parameters: the simulated domestic sewage with low C/N was domesticated and the domestic sewage was then denitrified. The results of the MBR-MBfR experiments indicated that a C/N ratio of two was suitable for <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><msubsup><mrow><mi>NH</mi></mrow><mn>4</mn><mo>+</mo></msubsup></semantics></math></inline-formula>-N, <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><msubsup><mrow><mi>NO</mi></mrow><mn>2</mn><mo>−</mo></msubsup></semantics></math></inline-formula>-N, <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><msubsup><mrow><mi>NO</mi></mrow><mn>3</mn><mo>−</mo></msubsup></semantics></math></inline-formula>-N, and chemical oxygen demand (COD) removal in partial nitrification-denitrification (PN-D) and hydrogen autotrophic denitrification for further treatment. The steady state for domestic wastewater was reached when the MBR-MBfR in the experimental conditions of HRT = 15 h, SRT = 20 d, 0.04 Mpa for H<sub>2</sub> pressure in MBfR, 0.4–0.8 mg/L DO in MBR, MLSS = 2500 mg/L(MBR) and 2800 mg/L(MBfR), and effluent concentrations of <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><msubsup><mrow><mi>NH</mi></mrow><mn>4</mn><mo>+</mo></msubsup></semantics></math></inline-formula>-N, <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><msubsup><mrow><mi>NO</mi></mrow><mn>3</mn><mo>−</mo></msubsup></semantics></math></inline-formula>-N, and <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><msubsup><mrow><mi>NO</mi></mrow><mn>2</mn><mo>−</mo></msubsup></semantics></math></inline-formula>-N were 4.3 ± 0.5, 1.95 ± 0.04, and 2.05 ± 0.15 mg/L, respectively. High-throughput sequencing results revealed the following: (1) The genus <i>Nitrosomonas</i> as the ammonia oxidizing bacteria (AOB) and <i>Denitratisoma</i> as potential denitrifiers were simultaneously enriched in the MBR; (2) at the genus level, <i>Meiothermus,</i><i>Lentimicrobium</i><i>, Thauera</i><i>,</i><i>Hydrogenophaga</i>, and <i>Desulfotomaculum</i> played a dominant role in leading to <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><msubsup><mrow><mi>NO</mi></mrow><mn>3</mn><mo>−</mo></msubsup></semantics></math></inline-formula>-N and <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><msubsup><mrow><mi>NO</mi></mrow><mn>2</mn><mo>−</mo></msubsup></semantics></math></inline-formula>-N removal in the MBfR.
first_indexed 2024-03-10T03:36:17Z
format Article
id doaj.art-8191ec99c17a4f5e847fe49ad9446d91
institution Directory Open Access Journal
issn 2077-0375
language English
last_indexed 2024-03-10T03:36:17Z
publishDate 2021-11-01
publisher MDPI AG
record_format Article
series Membranes
spelling doaj.art-8191ec99c17a4f5e847fe49ad9446d912023-11-23T09:29:47ZengMDPI AGMembranes2077-03752021-11-01111291110.3390/membranes11120911Simultaneous Partial Nitrification and Denitrification Maintained in Membrane Bioreactor for Nitrogen Removal and Hydrogen Autotrophic Denitrification for Further TreatmentKun Dong0Xinghui Feng1Wubin Wang2Yuchao Chen3Wei Hu4Haixiang Li5Dunqiu Wang6College of Environmental Science and Engineering, Guilin University of Technology, 319 Yanshan Street, Guilin 541006, ChinaCollege of Environmental Science and Engineering, Guilin University of Technology, 319 Yanshan Street, Guilin 541006, ChinaCollege of Environmental Science and Engineering, Guilin University of Technology, 319 Yanshan Street, Guilin 541006, ChinaCollege of Environmental Science and Engineering, Guilin University of Technology, 319 Yanshan Street, Guilin 541006, ChinaCollege of Environmental Science and Engineering, Guilin University of Technology, 319 Yanshan Street, Guilin 541006, ChinaCollege of Environmental Science and Engineering, Guilin University of Technology, 319 Yanshan Street, Guilin 541006, ChinaCollege of Environmental Science and Engineering, Guilin University of Technology, 319 Yanshan Street, Guilin 541006, ChinaLow C/N wastewater results from a wide range of factors that significantly harm the environment. They include insufficient carbon sources, low denitrification efficiency, and <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><msubsup><mrow><mi>NH</mi></mrow><mn>4</mn><mo>+</mo></msubsup></semantics></math></inline-formula>-N concentrations in low C/N wastewater that are too high to be treated. In this research, the membrane biofilm reactor and hydrogen-based membrane biofilm reactor (MBR-MBfR) were optimized and regulated under different operating parameters: the simulated domestic sewage with low C/N was domesticated and the domestic sewage was then denitrified. The results of the MBR-MBfR experiments indicated that a C/N ratio of two was suitable for <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><msubsup><mrow><mi>NH</mi></mrow><mn>4</mn><mo>+</mo></msubsup></semantics></math></inline-formula>-N, <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><msubsup><mrow><mi>NO</mi></mrow><mn>2</mn><mo>−</mo></msubsup></semantics></math></inline-formula>-N, <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><msubsup><mrow><mi>NO</mi></mrow><mn>3</mn><mo>−</mo></msubsup></semantics></math></inline-formula>-N, and chemical oxygen demand (COD) removal in partial nitrification-denitrification (PN-D) and hydrogen autotrophic denitrification for further treatment. The steady state for domestic wastewater was reached when the MBR-MBfR in the experimental conditions of HRT = 15 h, SRT = 20 d, 0.04 Mpa for H<sub>2</sub> pressure in MBfR, 0.4–0.8 mg/L DO in MBR, MLSS = 2500 mg/L(MBR) and 2800 mg/L(MBfR), and effluent concentrations of <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><msubsup><mrow><mi>NH</mi></mrow><mn>4</mn><mo>+</mo></msubsup></semantics></math></inline-formula>-N, <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><msubsup><mrow><mi>NO</mi></mrow><mn>3</mn><mo>−</mo></msubsup></semantics></math></inline-formula>-N, and <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><msubsup><mrow><mi>NO</mi></mrow><mn>2</mn><mo>−</mo></msubsup></semantics></math></inline-formula>-N were 4.3 ± 0.5, 1.95 ± 0.04, and 2.05 ± 0.15 mg/L, respectively. High-throughput sequencing results revealed the following: (1) The genus <i>Nitrosomonas</i> as the ammonia oxidizing bacteria (AOB) and <i>Denitratisoma</i> as potential denitrifiers were simultaneously enriched in the MBR; (2) at the genus level, <i>Meiothermus,</i><i>Lentimicrobium</i><i>, Thauera</i><i>,</i><i>Hydrogenophaga</i>, and <i>Desulfotomaculum</i> played a dominant role in leading to <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><msubsup><mrow><mi>NO</mi></mrow><mn>3</mn><mo>−</mo></msubsup></semantics></math></inline-formula>-N and <inline-formula><math xmlns="http://www.w3.org/1998/Math/MathML" display="inline"><semantics><msubsup><mrow><mi>NO</mi></mrow><mn>2</mn><mo>−</mo></msubsup></semantics></math></inline-formula>-N removal in the MBfR.https://www.mdpi.com/2077-0375/11/12/911partial nitrification-denitrificationhydrogen autotrophic denitrificationMBR-MBfR
spellingShingle Kun Dong
Xinghui Feng
Wubin Wang
Yuchao Chen
Wei Hu
Haixiang Li
Dunqiu Wang
Simultaneous Partial Nitrification and Denitrification Maintained in Membrane Bioreactor for Nitrogen Removal and Hydrogen Autotrophic Denitrification for Further Treatment
Membranes
partial nitrification-denitrification
hydrogen autotrophic denitrification
MBR-MBfR
title Simultaneous Partial Nitrification and Denitrification Maintained in Membrane Bioreactor for Nitrogen Removal and Hydrogen Autotrophic Denitrification for Further Treatment
title_full Simultaneous Partial Nitrification and Denitrification Maintained in Membrane Bioreactor for Nitrogen Removal and Hydrogen Autotrophic Denitrification for Further Treatment
title_fullStr Simultaneous Partial Nitrification and Denitrification Maintained in Membrane Bioreactor for Nitrogen Removal and Hydrogen Autotrophic Denitrification for Further Treatment
title_full_unstemmed Simultaneous Partial Nitrification and Denitrification Maintained in Membrane Bioreactor for Nitrogen Removal and Hydrogen Autotrophic Denitrification for Further Treatment
title_short Simultaneous Partial Nitrification and Denitrification Maintained in Membrane Bioreactor for Nitrogen Removal and Hydrogen Autotrophic Denitrification for Further Treatment
title_sort simultaneous partial nitrification and denitrification maintained in membrane bioreactor for nitrogen removal and hydrogen autotrophic denitrification for further treatment
topic partial nitrification-denitrification
hydrogen autotrophic denitrification
MBR-MBfR
url https://www.mdpi.com/2077-0375/11/12/911
work_keys_str_mv AT kundong simultaneouspartialnitrificationanddenitrificationmaintainedinmembranebioreactorfornitrogenremovalandhydrogenautotrophicdenitrificationforfurthertreatment
AT xinghuifeng simultaneouspartialnitrificationanddenitrificationmaintainedinmembranebioreactorfornitrogenremovalandhydrogenautotrophicdenitrificationforfurthertreatment
AT wubinwang simultaneouspartialnitrificationanddenitrificationmaintainedinmembranebioreactorfornitrogenremovalandhydrogenautotrophicdenitrificationforfurthertreatment
AT yuchaochen simultaneouspartialnitrificationanddenitrificationmaintainedinmembranebioreactorfornitrogenremovalandhydrogenautotrophicdenitrificationforfurthertreatment
AT weihu simultaneouspartialnitrificationanddenitrificationmaintainedinmembranebioreactorfornitrogenremovalandhydrogenautotrophicdenitrificationforfurthertreatment
AT haixiangli simultaneouspartialnitrificationanddenitrificationmaintainedinmembranebioreactorfornitrogenremovalandhydrogenautotrophicdenitrificationforfurthertreatment
AT dunqiuwang simultaneouspartialnitrificationanddenitrificationmaintainedinmembranebioreactorfornitrogenremovalandhydrogenautotrophicdenitrificationforfurthertreatment