| Literature DB >> 35518611 |
Yajing Guo1, Jiao Wang1, Shrameeta Shinde2, Xin Wang2, Yang Li1, Yexin Dai1, Jun Ren1, Pingping Zhang3, Xianhua Liu1.
Abstract
The development of microbial fuel cell (MFC) makes it possible to generate clean electricity as well as remove pollutants from wastewater. Extensive studies on MFC have focused on structural design and performance optimization, and tremendous advances have been made in these fields. However, there is still a lack of systematic analysis on biocatalysts used in MFCs, especially when it comes to pollutant removal and simultaneous energy recovery. In this review, we aim to provide an update on MFC-based wastewater treatment and energy harvesting research, and analyze various biocatalysts used in MFCs and their underlying mechanisms in pollutant removal as well as energy recovery from wastewater. Lastly, we highlight key future research areas that will further our understanding in improving MFC performance for simultaneous wastewater treatment and sustainable energy harvesting. This journal is © The Royal Society of Chemistry.Entities:
Year: 2020 PMID: 35518611 PMCID: PMC9055303 DOI: 10.1039/d0ra05234e
Source DB: PubMed Journal: RSC Adv ISSN: 2046-2069 Impact factor: 4.036
Fig. 1Schematic of using MFC for simultaneous wastewater treatment and energy recovery.
Fig. 2Advantages and disadvantages of MFC technology for treating wastewater.[10]
Fig. 3Proposed mechanisms for simultaneous pollutants removal and energy recovery by using MFC.
Fig. 4Research tendencies of wastewater treatment by MFC from 2001 to 2019.
Fig. 5Co-occurrence network analysis of keywords in publications on wastewater treatment by MFC from 2017 to 2019. Each keyword on the map is displayed as a node, with size determined by the occurrence. Keyword relationships are shown as edges of varying thickness determined by the co-occurrence.
Studies regarding organic carbon pollutants removal in MFCa
| MFC type | Organic pollutant | Source of inoculation | Substrates | Microorganisms | Electrode | Performance | Ref. | |
|---|---|---|---|---|---|---|---|---|
| Removal efficiency |
| |||||||
| SCMFC | COD | Anaerobic sludges | Effluent from the primary sedimentation tank | Not mentioned | Anode: air-cathode, cathode: ammonia-treated graphite fiber brush | COD removal: 25.8% | 422 mW m−2 |
|
| Tubular DCMFC | 2,4,6-Trichlorophenol | Anaerobic digester | Wastewaters |
| Anode: graphite fiber, cathode: graphite felt | 0.10 mol m−3 d−1 | 2.6 W m−3 |
|
| DCMFC | Dichlorophenol |
| Dichlorophenol |
| Anode and cathode: carbon cloth | Over 60% | 9.5 mW m−2 |
|
| DCMFC | COD | Anaerobic sludge | Glucose | Not mentioned | Proton exchange membranes, electrode: graphite plates | 72% | 60 mW m−2 |
|
| SCMFC | COD | Municipal sludge | Synthetic wastewater | Not mentioned | Anode: carbon felt and cathode: carbon clothe, graphene oxide hybridized MgO | COD removal: 79.5% | 755.63 mW m−2 |
|
| P-MFC | COD |
| Swine-farming wastewater | Cathode: | Anode: carbon cloth, cathode: activated carbon/PTFE mixture | COD removal: 89% | 850 mW m−2 |
|
| SCMFC | COD and phosphorus | Anaerobic sludge | Synthetic wastewater |
| Anode: carbon felt, cathode: air-cathode | More than 97% | 4.38 W m−3 |
|
| DCMFC | 2,4-Dichlorophenol | Domestic wastewater | Synthetic wastewater |
| Anode: carbon cloth, cathode: platinised titanium (Pt/Ti) plate | 62% | 66 mW m−2 |
|
| Photo-SCMFC | 2,4,6-Trichlorophenol | Municipal wastewater | Municipal wastewater |
| Anode: carbon felt with photocatalyst, cathode: air-cathode | 79.3% of TCP removal | 19.8 W m−3 |
|
SCMFC: single-chamber microbial fuel cells; DCMFCs: dual-chamber microbial fuel cells; P-MFC: photoautotrophic microbial fuel cells; photo-MFC: photocatalytic microbial fuel cells; COD: chemical oxygen demand.
Varied research on nitrogen and phosphate removal by using MFCa
| MFC type | Pollutant | Source of inoculation | Substrates | Microorganisms | Electrode | Performance | Ref. | |
|---|---|---|---|---|---|---|---|---|
| Removal efficiency |
| |||||||
| FA-MFC | Organic and nitrogen compounds | Activated sludge | Domestic wastewater |
| Anode: 30% wet-proof carbon cloth with a platinum (Pt) catalyst, cathode: air cathode | COD: 85%, TN: 94% | 6.3 W m−3 |
|
| DCMFC | NO3− and ClO4− | Activated sludge and excess sludge mixed in 1 : 1 vol ratio | NO3− and ClO4− mixed in 1 : 1 molar ratio | β-Proteobacteria, | Anode and cathode: carbon felts | ClO4−: 40.97%, NO3−: 86.03% | 2.2 W m−3 |
|
| SCMFC | Nitrogen compounds | Aerobic nitrifying sludge | Synthetic ammonia-contaminated wastewater |
| Anode and cathode: active-carbon felt | Ammonia 99.34%, total nitrogen (TN) 99.34%, COD 90.79% | 104 mW m−3 |
|
| SCMFC | NH4+-N | Aerobic denitrifying sludge | Synthetic wastewater | Anode: | Anode: carbon felt and cathode: air cathode, MnO2-catalyst | COD: 90%, ammonia: 98%; TN: 95% | 1270 mW m−2 |
|
| DCMFC | NH4+-N and PO43−-P | Anaerobic sludge | Municipal wastewater | Not mentioned | Anode: graphite felt, cathode: carbon-fiber brush coated with a titanium bar | NH4+-N: >97.58%, PO43−-P: >94.9% P | Not mentioned |
|
| DCMFC | Nitrogen, phosphorus and COD | Anaerobic active sludge | Mustard tuber wastewater |
| Anode and cathode: carbon cloth | Total phosphorus (TP): 80.8 ± 1.0%, COD: >90 | Not mentioned |
|
| DCMFC | Nitrogenous compounds |
| Swine wastewater |
| Anode: carbon felt, cathode: carbon fiber cloth | Ammonia nitrogen: 85.6%, TN: 70.2% | 3720 mW m−3 |
|
| P-MFC | Nitrogenous compounds and phosphate |
| Municipal wastewater |
| Anode and cathode: carbon brushes | NH4+: 95.9%, TN: 95.1%, PO43−-P: 82.7% | 466.9 mW m−3 |
|
| AD-MFC | Nitrate nitrogen | Cow manure and soil | Municipal wastewater |
| Anode and cathode: graphite felt | NO3−: 0.118 kg m−3 d−1 | 4.45 W m −3 |
|
| HD-MFC | Nitrate nitrogen | Cow manure and soil | Municipal wastewater |
| Anode and cathode: graphite felt | NO3−: 2.06 kg m−3 d−1 | 3.02 W m−3 |
|
FA-MFC: flat-panel air-cathode microbial fuel cells; SCMFC: single-chamber microbial fuel cells; DCMFCs: dual-chamber microbial fuel cells; P-MFC: photoautotrophic microbial fuel cells; AD-MFC: autotrophic cathodic denitrification microbial fuel cells; HD-MFC: heterotrophic cathodic denitrification microbial fuel cells; COD: chemical oxygen demand; TN: total nitrogen.