| Literature DB >> 33916302 |
Eivydas Andriukonis1,2,3, Raimonda Celiesiute-Germaniene1,4, Simonas Ramanavicius1,2,3, Roman Viter1,5,6, Arunas Ramanavicius1,2,3.
Abstract
This review focuses on the overview of microbial amperometric biosensors and microbial biofuel cells (MFC) and shows how very similar principles are applied for the design of both types of these bioelectronics-based devices. Most microorganism-based amperometric biosensors show poor specificity, but this drawback can be exploited in the design of microbial biofuel cells because this enables them to consume wider range of chemical fuels. The efficiency of the charge transfer is among the most challenging and critical issues during the development of any kind of biofuel cell. In most cases, particular redox mediators and nanomaterials are applied for the facilitation of charge transfer from applied biomaterials towards biofuel cell electrodes. Some improvements in charge transfer efficiency can be achieved by the application of conducting polymers (CPs), which can be used for the immobilization of enzymes and in some particular cases even for the facilitation of charge transfer. In this review, charge transfer pathways and mechanisms, which are suitable for the design of biosensors and in biofuel cells, are discussed. Modification methods of the cell-wall/membrane by conducting polymers in order to enhance charge transfer efficiency of microorganisms, which can be potentially applied in the design of microbial biofuel cells, are outlined. The biocompatibility-related aspects of conducting polymers with microorganisms are summarized.Entities:
Keywords: bioelectronics; cell membrane/wall modifications; conducting polymers; direct electron transfer; enzyme-based biofuel cells; extracellular electron transfer; microbial biofuel cells; microbial biosensors; whole cell-based biosensors; yeast
Mesh:
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Year: 2021 PMID: 33916302 PMCID: PMC8038125 DOI: 10.3390/s21072442
Source DB: PubMed Journal: Sensors (Basel) ISSN: 1424-8220 Impact factor: 3.576
Figure 1General scheme of microbial biofuel cell with direct and mediated electron transfer.
The description of microbial biofuel cells (MFCs) anode modification method and MFC performance. Abbreviations provided below the table.
| Electricigen | Anode Modification Method | Anode Material | Electron Donor | PD, mW m-2 | Other Remarks | Ref. |
|---|---|---|---|---|---|---|
|
| Physical absorption of CNTs, followed by physical adhesionof the cells | PU | Glucose/ | 100 | After first 24 h PD reduces to 70% of the maximum, and remains constant with continuous substitution of glucose/MB for long periods. | [ |
|
| Graft-polymerization of PANI and layer by layer self-assembling of carbon nanotubes | APTES/ | Sodium lactate | 34.5 | Maximal current density was 6.98 μA cm−2, 26 times higher than plain ITO electrode. | [ |
|
| Dip-coating of PEI and seed-mediated green synthesis growth of AuNPs followed by the biofilm formation during 72 h | CF | Glucose | 2771 | The single chamber architecture played a role in reducing the number of chemicals and costs. | [ |
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| Physical adsorption of alginate film with entrapped yeast cells | CF | Glucose | - | Current density was 0.326 A m−2 (CF-Yeast -algae electrode) and 0.185 A m−2 (CF-Yeast- Neutral Red beads electrode). Operation time was 44 days. | [ |
| Classes of | MWCNTs blended with biogenic Au and evenly spreading the paste followed by the biofilm formation | CF | Sludge | 178 | Start-up time 6.75 days. | [ |
|
| Dip coating of PEI, SDBS mediated chemical growth of FeMnNPs followed by the biofilm formation | CF | Glucose | 5838 | Controlled FeMnNP surfactant-mediated growth was performed within a single vial under ambient conditions Relationship between the surfactant-mediated FeMnNPs and yeast biofilm development was revealed. | [ |
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| Dip coating of PEI followed by dipcoating of one of the QS molecules (phenylethanol, tryptophol and tyrosol). Biofilm growth. | CF | Glucose | 159 * | Start-up time 3 days | [ |
|
| Electrochemical deposition of the biofilm | CF | APAP | 6.5 | A mature biofilm was obtained at day 7 | [ |
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| Electrochemical deposition of the biofilm | CF | APAP | 50 | A mature biofilm was obtained at day 7. The power density in presence of lignin of 16 mW m−2 lasted 200 h. | [ |
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| Cross-linking and hydrophobic interaction of yeast, PEI and CNTs | CNTs | Glucose | 344 | Membraneless MFC. MPD was maintained to 86% of initial value even after 8 days | [ |
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| Drop coating of PQ and drop coating of MWCNTs | Graphite | Glucose | 1.13 10−4 | The application of MWCNTs in anode of biofuel cell increased generated power by 69 times and generated voltage by 8 times. | [ |
|
| Self-assembly of aldrithiol monolayer, drop coating of OsRP solution, drop coating of | Gold | Succinate | - | The maximum current density response was ~5 μA cm−2. Stability test showed slight decrease response in current with time and reached approximately 73% of the initial response after 6 h. | [ |
*-power densities for MFCs based on phenylethanol, tryptophol and tyrosol, respectively. APAP—acetaminophen. APTES—γ-aminopropyltriethoxysilane. CF—carbon felt. ITO—indium tin oxide. MB—methylene blue. MWCNTs—multi-walled carbon nanotubes. NPs—nanoparticles. OsRP—osmium redox polymer.PANI—polyaniline. PD—power density. PEI—polyethyleneimine. PU—polyurethane. PQ—9,10-phenanthrenequinone. QS—quorum sensing.
Figure 2Electrochemical deposition of conducting polymer–polypyrrole and entrapment of proteins within formed Ppy layer, while potential pulses are applied. Adapted from [62].
Figure 3(a) Chrono-amperogram, which was registered during electrodeposition of Ppy, using pulsed-potential-based mode. (b) Dependence of anodic peaks, which are presented in Figure 3a, on the pulse number during electrochemical deposition. Adapted according to data presented in [69].
Figure 4Enzymatic biofuel cell powered by glucose, cathode of this biofuel cell is based on co-immobilized horseradish peroxidase (HRP) and glucose oxidase (GOx) and anode is based on immobilized glucose oxidase. On anode electrons from GOx are transferred to the electrode via redox mediator power density (PD) and in cathode hydrogen peroxide created during enzymatic reaction of GOx is consumed by HRP and electrons from cathode are transferred directly to HRP.
Figure 5Schematic representation of Ppy synthesis in cell wall of yeast [10]; Redox enzymes that are located in plasma membrane are oxidizing [Fe(CN)6]4− into [Fe(CN)6]3− that is inducing polymerization reaction of pyrrole [135].
Figure 6(a) Schematic representation of cell modification by agent formation principle. Cells can by modified using pre-synthesized compounds (I), assembled/ synthesized in situ with living cells are present (II) and in situ when cell assists/catalyzes synthesis assembly of modification agent; (b) schematic representation of modifying agent localization in MFC applications: (I) surface interactions as adsorption, electrostatic interactions etc.; (II) modifying agent is either covalently bonded or forms interlacing and inseparable structures with cell walls or other similar structures; (III) when modifying agent forms aggregates from its matrix and cells; (IV) higher agglomerate organization onto surfaces; (V) internalization of modification agent.