| Literature DB >> 32050646 |
Li Guang1,2, Desmond Ato Koomson3, Huang Jingyu3, David Ewusi-Mensah3, Nicholas Miwornunyuie3.
Abstract
The tri-functional purpose of Microbial Desalination Cell (MDC) has shown a great promise in our current scarcity of water, an increase in water pollution and the high cost of electricity production. As a biological system, the baseline force that drives its performance is the presence of exoelectrogens in the anode chamber. Their presence in the anodic chamber of MDC systems enables the treatment of water, desalination of seawater, and the production of electrical energy. This study reviews the characteristics of exoelectrogens, as a driving force in MDC and examines factors which influence their growth and the performance efficiency of MDC systems. It also addresses the efficiency of mixed cultures with certain predominant species as compared to pure cultures used in MDC systems. Furthermore, the study suggests the need to genetically modify certain predominant strains in mixed cultures to enhance their performance in COD removal, desalination and power output and the integration of MDC with other technologies for cost-effective processes.Entities:
Keywords: electron transport chain; exoelectrogens; microbial desalination cell; mixed culture; predominant species; pure cultures; tri-functional process
Year: 2020 PMID: 32050646 PMCID: PMC7037215 DOI: 10.3390/ijerph17031121
Source DB: PubMed Journal: Int J Environ Res Public Health ISSN: 1660-4601 Impact factor: 3.390
Figure 1Schematic diagram of a conventional Microbial Desalination Cell (MDC) system with Anode Exchange Membrane (AEM) and Cathode Exchange Membrane (CEM) depicting the general procedure of transfer of electrons from an exo-electrogenic cell after the oxidation of organic matter (substrate) by the cell.
Figure 2A general schematic diagram of the catabolic and respiratory pathway in exoelectrogens.
Figure 3A Schematic diagram of a magnified view of the exoelectrogen’s cell membrane showing Extra-cellular Electron Transfer (EET) NADH-dependent catabolic pathway consisting of Pyruvate Dehydrogenase (PDH) and NADH. UQ is oxidized form of ubiquinone; UQH2 is reduced form of ubiquinone.
Figure 4Main recognized mechanisms of electron transfer from exoelectrogens. (A) Direct electron transfer with c-type cytochromes (CTCs). (B) Soluble electron shuttles. (C) Electro-active biofilm formation. (D) Solid conductive matrix with nanowires or pili.
Differences in the performance of pure cultures and mixed cultures used in MDC Systems [17,30,40].
| Pure Cultures | Mixed Cultures |
|---|---|
| Substrate specificity | Predominant species dependent on substrate |
| Uses one or few of the electron transfer mechanism | Combines several electron transfer mechanism |
| Very costly in isolating and preparation | Less costly in obtaining and preparation |
| Less efficient in electricity generation | More efficient in electricity generation |
| Known electron transfer mechanism which can be engineered for optimum performance | Unknown electron transfer mechanism being used. |
Taxa of exoelectrogens and performance in MDC Systems.
| Exoelectrogens At Anode Chamber | Substrate | Mode of Operation | COD Removal at Anode Chamber | Desalination | pH of Anolyte | Temp. (°C) of Anolyte | Power Output | Configuration | References |
|---|---|---|---|---|---|---|---|---|---|
|
| Glucose | Batch | - | 55.03% | 6.5 | - | 488 mW/m3 | Conventional MDC | [ |
| Biofilm predominantly | Domestic Waste Water | Fed-Batch | 55% | <66% | - | - | 3.6 W/m3 | Conventional MDC | [ |
| Biofilm predominantly | Municipal Waste Water | Batch | 52% | 66% | 6.0 ± 0.1 | - | 8.01 W/m3 | Conventional MDC | [ |
| Steel Plant Waste Water | Batch | 70 ± 1.8% | - | 7.0 ± 0.2 | - | 10.2 mW/m2 | Multi-Chambered MDC | [ | |
|
| 0.1% yeast extract with Malachite green dye | Fed-Batch | Complete de-colorization | 62.2 ± 0.4% | 4.0–8.0 | 30.0 | 0.15 ± 0.05 W/m3 | Conventional MDC | [ |
|
| 0.1% yeast extract with Sunset yellow dye | Fed-Batch | Complete de-colorization | 57.6 ± 0.2% | 4.0–8.0 | 30.0 | 0.14 ± 0.03 W/m3 | Conventional MDC | [ |