Wastewaters treatment containing phenol and ammonium using aerobic submerged membrane bioreactor

Abstract Phenolic wastewater was treated using anaerobic submerged membrane bioreactor (ASMBR). Effect of different solids retention times on MBR performance was studied. Various ratios of carbon to nitrogen were used in the synthetic wastewaters. During the operation, phenol concentration of feed w...

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Main Authors: Mashallah Rezakazemi, Mohsen Maghami, Toraj Mohammadi
Format: Article
Language:English
Published: BMC 2018-07-01
Series:Chemistry Central Journal
Subjects:
Online Access:http://link.springer.com/article/10.1186/s13065-018-0450-1
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spelling doaj-3b03ad6ae1a0482393a605e2c525128b2021-08-02T18:38:33ZengBMCChemistry Central Journal1752-153X2018-07-0112111010.1186/s13065-018-0450-1Wastewaters treatment containing phenol and ammonium using aerobic submerged membrane bioreactorMashallah Rezakazemi0Mohsen Maghami1Toraj Mohammadi2Faculty of Chemical and Materials Engineering, Shahrood University of TechnologyResearch and Technology Centre for Membrane Processes, Faculty of Chemical Engineering, Iran University of Science and Technology (IUST)Research and Technology Centre for Membrane Processes, Faculty of Chemical Engineering, Iran University of Science and Technology (IUST)Abstract Phenolic wastewater was treated using anaerobic submerged membrane bioreactor (ASMBR). Effect of different solids retention times on MBR performance was studied. Various ratios of carbon to nitrogen were used in the synthetic wastewaters. During the operation, phenol concentration of feed was changed from 100 to 1000 mg L−1. Phenol concentration was increased stepwise over the first 30 days and kept constant at 1000 mg L−1, thereafter. For the first 100 days, a chemical oxygen demand (COD) to N ratio of 100:5.0 was used and this resulted in phenol and COD removal more than 99 and 95%, respectively. However, the ammonium removal decreased from 95 to 40% by increasing the phenol concentration of feed, from 100 to 1000 mg L−1. For the last 25 days, a COD to N ratio of 100:2.1 was used due to the ammonium accumulation in the ASMBR. This led to the complete ammonium removal and no ammonium was detected in the ASMBR permeate. These results suggest that in the ASMBR at high phenol loading of 1000 mg L−1, COD to N ratio of the phenolic wastewater must be 100:2.1 for ammonium removal, while at low phenol loading, COD to N ratio of 100:5.0 can be used.http://link.springer.com/article/10.1186/s13065-018-0450-1MembraneHollow fiberWastewaterAmmonium removalEnvironment
collection DOAJ
language English
format Article
sources DOAJ
author Mashallah Rezakazemi
Mohsen Maghami
Toraj Mohammadi
spellingShingle Mashallah Rezakazemi
Mohsen Maghami
Toraj Mohammadi
Wastewaters treatment containing phenol and ammonium using aerobic submerged membrane bioreactor
Chemistry Central Journal
Membrane
Hollow fiber
Wastewater
Ammonium removal
Environment
author_facet Mashallah Rezakazemi
Mohsen Maghami
Toraj Mohammadi
author_sort Mashallah Rezakazemi
title Wastewaters treatment containing phenol and ammonium using aerobic submerged membrane bioreactor
title_short Wastewaters treatment containing phenol and ammonium using aerobic submerged membrane bioreactor
title_full Wastewaters treatment containing phenol and ammonium using aerobic submerged membrane bioreactor
title_fullStr Wastewaters treatment containing phenol and ammonium using aerobic submerged membrane bioreactor
title_full_unstemmed Wastewaters treatment containing phenol and ammonium using aerobic submerged membrane bioreactor
title_sort wastewaters treatment containing phenol and ammonium using aerobic submerged membrane bioreactor
publisher BMC
series Chemistry Central Journal
issn 1752-153X
publishDate 2018-07-01
description Abstract Phenolic wastewater was treated using anaerobic submerged membrane bioreactor (ASMBR). Effect of different solids retention times on MBR performance was studied. Various ratios of carbon to nitrogen were used in the synthetic wastewaters. During the operation, phenol concentration of feed was changed from 100 to 1000 mg L−1. Phenol concentration was increased stepwise over the first 30 days and kept constant at 1000 mg L−1, thereafter. For the first 100 days, a chemical oxygen demand (COD) to N ratio of 100:5.0 was used and this resulted in phenol and COD removal more than 99 and 95%, respectively. However, the ammonium removal decreased from 95 to 40% by increasing the phenol concentration of feed, from 100 to 1000 mg L−1. For the last 25 days, a COD to N ratio of 100:2.1 was used due to the ammonium accumulation in the ASMBR. This led to the complete ammonium removal and no ammonium was detected in the ASMBR permeate. These results suggest that in the ASMBR at high phenol loading of 1000 mg L−1, COD to N ratio of the phenolic wastewater must be 100:2.1 for ammonium removal, while at low phenol loading, COD to N ratio of 100:5.0 can be used.
topic Membrane
Hollow fiber
Wastewater
Ammonium removal
Environment
url http://link.springer.com/article/10.1186/s13065-018-0450-1
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AT mohsenmaghami wastewaterstreatmentcontainingphenolandammoniumusingaerobicsubmergedmembranebioreactor
AT torajmohammadi wastewaterstreatmentcontainingphenolandammoniumusingaerobicsubmergedmembranebioreactor
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