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Catalytic membrane cathode integrated in a proton exchange membrane-free microbial fuel cell for coking wastewater treatment
•A catalytic membrane cathode-microbial fuel cell system was constructed.•The CNF-CFO/PM cathode obtained effective catalytic and antifouling activities.•The COD removal efficiency of CW reached 96.5% with output voltage of 0.40 V.•Replacing proton exchange membrane with quartz sand layer reduced th...
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Published in: | Journal of the Taiwan Institute of Chemical Engineers 2022-03, Vol.132, p.104117, Article 104117 |
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Main Authors: | , , , , , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
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Summary: | •A catalytic membrane cathode-microbial fuel cell system was constructed.•The CNF-CFO/PM cathode obtained effective catalytic and antifouling activities.•The COD removal efficiency of CW reached 96.5% with output voltage of 0.40 V.•Replacing proton exchange membrane with quartz sand layer reduced the cost.
Coking wastewater (CW) is characterized by complex composition, high concentration and toxicity, thereby challenging the treatment technologies. Traditional microbial fuel cell (MFC) is deficient in effluent quality and capital cost. Therefore, integrating the catalytic electrode membrane in separation process in MFC is promising for actual wastewater treatment, while replacing proton exchange membrane (PEM) to reduce cost.
A CNF-CFO/PM membrane (blended with carbon nanofiber-CoFe2O4, polyvinylidene fluoride) was prepared via casting and phase inversion. By using this membrane as cathode, activated carbon-loaded electrogenic bacteria as bio-anode, the catalytic membrane cathode-MFC system (CM-MFC) was constructed with quartz sand separating layer (QSL) replacing PEM.
Modification with CNF-CFO catalyst effectively improved the catalytic and anti-fouling (membrane foulants) property of membrane cathode. The optimal activity of CM-MFC was achieved under 36 h (HRT), with the COD decreasing from 4325.0-5074.3 mg L−1 to 50.0-92.8 mg L−1, and the stable output voltage of ∼0.40 V. The high-throughput sequencing results clarified that the enriched electrogenic bacteria coexisted with other anaerobic bacteria in the anodic chamber and functioned for electron transfer and organics removal. Integrating with the catalysis and filtration processes of membrane cathode, the effluent quality after primary treatment in the anodic chamber was further enhanced.
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ISSN: | 1876-1070 1876-1089 |
DOI: | 10.1016/j.jtice.2021.10.017 |