Please use this identifier to cite or link to this item: https://hdl.handle.net/11499/7253
Title: Sequential anaerobic, aerobic/anoxic treatment of simulated landfill leachate
Authors: Ağdağ, Osman Nuri
Sponza, D.T.
Keywords: Anaerobic/aerobic/denitrifying sequential
Anammox - anaerobic ammonia oxidation
COD removal
Leachate treatment
NH4-N removal
NO3-N removal
ammonia
methane
nitrate
Ammonia
Bioreactors
Chemical oxygen demand
Microorganisms
Nitrification
anoxic conditions
bioreactor
chemical oxygen demand
experimental study
landfill
leachate
methanogenesis
municipal solid waste
nitrification
oxic conditions
oxidation
pollutant removal
retention
aerobic reactor
anaerobic reactor
article
denitrification
hydraulic conductivity
landfill leachate
simulation
stirred reactor
upflow reactor
Anaerobiosis
Environmental Remediation
Equipment Design
Models, Chemical
Models, Statistical
Oxygen
Sewage
Waste Disposal, Fluid
Water Pollutants, Chemical
Water Purification
Abstract: In this study COD, ammonia and nitrate were treated through methanogenesis, nitrification denitrification and anammox processes in anaerobic-aerobic and anaerobic/anoxic sequential in leachate samples produced from municipal solid waste in an anaerobic simulated landfilling bioreactor. The experiments were performed in an upflow anaerobic sludge blanket reactor (UASB), aerobic completely stirred tank reactor (CSTR) and upflow anaerobic/anoxic sludge blanket reactor (UA/ANSB). Hydraulic retention times in anaerobic, aerobic and anaerobic/anoxic stages were 1, 3.6 and 1 days, respectively, through 244 days of total operation period with 168 days of adaptation period of microorganisms to the reactors. The organic loading rates increased from 5.9 to 50 kg COD m-3 day-1. The total COD and TN removal efficiencies of the anaerobic-aerobic-anoxic system were 96 % and 99 %, respectively, at an influent OLR as high as 50 kg COD m-3 day-1. The maximum methane percentage in the UASB reactor was 82 % while the methane percentage was zero in UA/ANSB reactor for the aforementioned OLR at the end of steady-state conditions. NH4-N removal efficiency of the aerobic reactor was 90% while anaerobic ammonia oxidation was measured as 99 % in the anoxic reactor. The denitrification efficiency was 99% in the same reactor. Total TN removal of the whole system was 99 %. © Taylor & Francis, 2008.
URI: https://hdl.handle.net/11499/7253
https://doi.org/10.1080/09593330802028758
ISSN: 0959-3330
Appears in Collections:Mühendislik Fakültesi Koleksiyonu
PubMed İndeksli Yayınlar Koleksiyonu / PubMed Indexed Publications Collection
Scopus İndeksli Yayınlar Koleksiyonu / Scopus Indexed Publications Collection
WoS İndeksli Yayınlar Koleksiyonu / WoS Indexed Publications Collection

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