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Simultaneous ammonia and organics degradation from municipal landfill leachate by electrochemical oxidation

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dc.contributor.author Mandal, Pubali
dc.date.accessioned 2024-10-01T10:46:13Z
dc.date.available 2024-10-01T10:46:13Z
dc.date.issued 2024-03
dc.identifier.uri https://www.tandfonline.com/doi/full/10.1080/09593330.2024.2323554
dc.identifier.uri http://dspace.bits-pilani.ac.in:8080/jspui/xmlui/handle/123456789/15751
dc.description.abstract The two primary issues for wide implementation of the electrochemical oxidation of wastewater are the significant cost of electrode and high energy consumption. On the other side, conventional biological processes and membrane technology have several drawbacks for recalcitrant landfill leachate (LL) treatment. To address these issues, graphite/PbO2 anode was used to treat medium to mature age (biodegradability index, 5-day biochemical oxygen demand/chemical oxygen demand: 0.25) LL. To reduce the cost of the oxidation process and maximize the efficiency, operating conditions were optimized. The optimum parameter values were obtained as 24.7 mA cm−2, 180 ± 3 rpm, and 1.9 cm of current density, stirring rate, and electrode gap, respectively. Dissolved organic carbon (DOC), chemical oxygen demand (COD), and ammonia-N removal efficiencies of 55 ± 1.4%, 81 ± 1.9%, and 56 ± 3% were obtained after 8 h of degradation at optimum conditions. The decrease in aromatic substances and ultraviolet (UV) quenching materials were evaluated by UV-Visible spectroscopy and Specific UV absorbance. The conversion of aromatic compounds into simpler molecule compounds was also verified by Fourier-transform infrared spectroscopy analysis. The lab-scale anode synthesis cost was evaluated as 0.42 USD. en_US
dc.language.iso en en_US
dc.publisher Taylor & Francis en_US
dc.subject Civil Engineering en_US
dc.subject Energy consumption en_US
dc.subject UV-Vis analysis en_US
dc.subject UV-Vis analysis en_US
dc.subject Cost of anode en_US
dc.title Simultaneous ammonia and organics degradation from municipal landfill leachate by electrochemical oxidation en_US
dc.type Article en_US


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