Degradation of acridine orange using sustainable bio-electro-Fenton and bio-electro-peroxone systems with MIL-53(Fe)-derived Fe3O4 and MWCNT composite: A comparative assessment

• MIL-53(Fe)-derived Fe 3 O 4 /MWCNT ( c Fe@MWCNT) found an excellent cathode catalyst. • A comparison between Bio-electro-Fenton (BEF) and Bio-electro-Peroxone (BEP). • BEP- c Fe@MWCNT outperformed BEF- c Fe@MWCNT in acridine orange (ACO) degradation. • ACO degradation and concurrent power generation were accomplished by both systems. • Potential pathways for the degradation of ACO were identified. The present investigation articulates the application of a MIL-53(Fe) metal-organic framework (MOF)-derived Fe 3 O 4 and multi-walled carbon nanotubes ( c Fe@MWCNT) composite as cathode catalyst in bio-electro-Fenton (BEF) and bio-electro-peroxone (BEP) systems. Both the systems were comparatively inspected for the in-situ production of hydrogen peroxide (H 2 O 2 ), further turning into hydroxyl radical ( ˙ OH) to degrade the acridine orange (ACO) dye. The k value for the degradation of ACO in BEF- c Fe@MWCNT was 0.0075 min −1 , which was 17.3-fold lower than the k value attained by the BEP- c Fe@MWCNT system (0.1298 min −1 ). Interestingly, the baffling in the BEP system increased the degradation rate from 0.0575 to 0.1298 min −1 . Further, the ACO degradation in the secondary treated sewage was determined to be 78.51 ± 3.02 % (240 min) and 83.2 ± 2.7 % (50 min) in BEF- c Fe@MWCNT and BEP- c Fe@MWCNT, respectively. The demethylation reaction, initiated by the ˙ OH attack, was identified as the primary pathway for ACO degradation in both systems. Simultaneously, the intrinsic microbial activity in the anodic chamber was capable of generating power of 120.0 ± 2.2 and 103.6 ± 4.7 mW m −2 in BEF and BEP, respectively. A comprehensive comparative assessment of both systems was conducted based on pollutant degradation, power generation, and operational cost. Overall, results indicated the superiority of the baffled BEP- c Fe@MWCNT system towards emerging contaminant degradation in a shorter reaction time and affirmed its practical feasibility in wastewater treatment.

Authors

Institutions

Publication Details

Journal
Electrochimica Acta
Published
2025-04-23
DOI
https://doi.org/10.1016/j.electacta.2025.146285
Citations
3
Primary Topic
Advanced oxidation water treatment
Type
article
Field-Weighted Citation Impact
2.45
Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Degradation of acridine orange using sustainable bio-electro-Fenton and bio-electro-peroxone systems with MIL-53(Fe)-derived Fe3O4 and MWCNT composite: A comparative assessment

Azhan Ahmad, Shraddha Yadav, Monali Priyadarshini, Makarand M. Ghangrekar
3 citations
Electrochimica Acta
Advanced oxidation water treatment
2.45
article

Degradation of acridine orange using sustainable bio-electro-Fenton and bio-electro-peroxone systems with MIL-53(Fe)-derived Fe3O4 and MWCNT composite: A comparative assessment

Azhan Ahmad, Shraddha Yadav, Monali Priyadarshini, Makarand M. Ghangrekar
article en
3 citations

Abstract

• MIL-53(Fe)-derived Fe 3 O 4 /MWCNT ( c Fe@MWCNT) found an excellent cathode catalyst. • A comparison between Bio-electro-Fenton (BEF) and Bio-electro-Peroxone (BEP). • BEP- c Fe@MWCNT outperformed BEF- c Fe@MWCNT in acridine orange (ACO) degradation. • ACO degradation and concurrent power generation were accomplished by both systems. • Potential pathways for the degradation of ACO were identified. The present investigation articulates the application of a MIL-53(Fe) metal-organic framework (MOF)-derived Fe 3 O 4 and multi-walled carbon nanotubes ( c Fe@MWCNT) composite as cathode catalyst in bio-electro-Fenton (BEF) and bio-electro-peroxone (BEP) systems. Both the systems were comparatively inspected for the in-situ production of hydrogen peroxide (H 2 O 2 ), further turning into hydroxyl radical ( ˙ OH) to degrade the acridine orange (ACO) dye. The k value for the degradation of ACO in BEF- c Fe@MWCNT was 0.0075 min −1 , which was 17.3-fold lower than the k value attained by the BEP- c Fe@MWCNT system (0.1298 min −1 ). Interestingly, the baffling in the BEP system increased the degradation rate from 0.0575 to 0.1298 min −1 . Further, the ACO degradation in the secondary treated sewage was determined to be 78.51 ± 3.02 % (240 min) and 83.2 ± 2.7 % (50 min) in BEF- c Fe@MWCNT and BEP- c Fe@MWCNT, respectively. The demethylation reaction, initiated by the ˙ OH attack, was identified as the primary pathway for ACO degradation in both systems. Simultaneously, the intrinsic microbial activity in the anodic chamber was capable of generating power of 120.0 ± 2.2 and 103.6 ± 4.7 mW m −2 in BEF and BEP, respectively. A comprehensive comparative assessment of both systems was conducted based on pollutant degradation, power generation, and operational cost. Overall, results indicated the superiority of the baffled BEP- c Fe@MWCNT system towards emerging contaminant degradation in a shorter reaction time and affirmed its practical feasibility in wastewater treatment.

Electrochimica ActaVol. 528
Indian Institute of Technology Kharagpur (IN), ITPEnergised Group (India) (IN), Vellore Institute of Technology University (IN)
Responsible consumption and production
Openalex Percentile: Top 12%
Advanced oxidation water treatment
2.45
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.