| Literature DB >> 26788124 |
Okkyoung Choi1, Byoung-In Sang1.
Abstract
Extracellular electron transfer in microorganisms has been applied for bioelectrochemical synthesis utilizing microbes to catalyze anodic and/or cathodic biochemical reactions. Anodic reactions (electron transfer from microbe to anode) are used for current production and cathodic reactions (electron transfer from cathode to microbe) have recently been applied for current consumption for valuable biochemical production. The extensively studied exoelectrogenic bacteria Shewanella and Geobacter showed that both directions for electron transfer would be possible. It was proposed that gram-positive bacteria, in the absence of cytochrome C, would accept electrons using a cascade of membrane-bound complexes such as membrane-bound Fe-S proteins, oxidoreductase, and periplasmic enzymes. Modification of the cathode with the addition of positive charged species such as chitosan or with an increase of the interfacial area using a porous three-dimensional scaffold electrode led to increased current consumption. The extracellular electron transfer from the cathode to the microbe could catalyze various bioelectrochemical reductions. Electrofermentation used electrons from the cathode as reducing power to produce more reduced compounds such as alcohols than acids, shifting the metabolic pathway. Electrofuel could be generated through artificial photosynthesis using electrical energy instead of solar energy in the process of carbon fixation.Entities:
Keywords: Bioelectrochemical synthesis; Cathodic electron; Electrofuel; Extracellular electron transfer
Year: 2016 PMID: 26788124 PMCID: PMC4717640 DOI: 10.1186/s13068-016-0426-0
Source DB: PubMed Journal: Biotechnol Biofuels ISSN: 1754-6834 Impact factor: 6.040
The application of bioelectrochemical reduction
| Application | Product | Reaction conditions | Key outcomes | Ref. |
|---|---|---|---|---|
| Direct reduction | Cr6+ → Cr3+ |
| U(VI) was removed and recovered using poised electrode | [ |
|
| Lactate and the electrode as the electron donors for Cr(VI) reduction | [ | ||
| Fumarate → succinate |
| Fumarate reduction dependent on current supply | [ | |
|
| Similar comparison under chromate reducing condition | [ | ||
| Nitrate reduction | Nitrifying and denitrifying microorganisms at +197 mV vs. SHE | Simultaneous occurrence of nitrification and denitrification at a biocathode | [ | |
| Denitrifying microorganisms at −123 mV vs. SHE | Long-term stability, carbon-free operation | [ | ||
| Indirect reduction | Caproate and caprylate production from acetate | Acetate fed at −0.9 V vs. NHE | In situ-produced hydrogen as electron donor, low concentration and reaction rates | [ |
| Ethanol production from acetate | −550 mV vs. NHE, artificial mediator tested | Methyl viologen increased ethanol production but inhibited butyrate and methane formation, still hydrogen was coproduced at the cathode | [ | |
| Alcohol formation from glycerol | Open circuit operation | Changes in microbial community and product outcomes after current supply | [ | |
| Reduction of acetate and butyrate to mainly alcohols and acetone | −820 mV vs. Ag/AgCl | Halotolerant mixed sulfate-reducing bacteria culture | [ | |
| Polyhydroxyalkanoates (PHA) from glucose | 512 mV, the biocathode coupled to a bioanode in an MEC | Microaerophilic microenvironment at cathode enhanced PHA synthesis as alternative pathway to re-oxidize the NADH | [ | |
| Butyraldehyde to butanol | Immobilized alcohol dehydrogenase at −400 mV vs. Ag/AgCl | Reduction to alcohol by current without supplement of NADH | [ | |
| Hydrogen production | −700 mV vs. Ag/AgCl | Increased cathodic hydrogen efficiency on microbial biocathode based on a naturally selected mixed culture | [ | |
| 500 mV, the biocathode coupled to a bioanode in an MEC | Operated for a long period with high current density but phosphate precipitation on the biocathode | [ | ||
| −700 mV vs. SHE |
| [ | ||
| Methane production | −700 mV vs. Ag/AgCl | Methane production directly from current | [ | |
| −550 mV vs. NHE | CO2 reduction to CH4, need to reduce the internal resistance | [ | ||
| Improved 1,3-propandiol production from glycerol | −900 mV vs. SHE | Electrical current as the driving force for a mixed population fermenting glycerol in the cathode | [ | |
| Improved butanol production from glucose | +0.045 V vs. SHE | Increased alcohol production in electrofermentation with increased a ratio NADH/NAD+ | [ | |
| Electrofuel from CO2 and electricity | Butyrate | −800 mV vs. SHE | Production of organic compounds from CO2 by hydrogen driven by a cathode | [ |
| Acetate | −590 mV vs. SHE | Higher acetate production than on unmodified graphite | [ | |
| Acetate, 2-oxobutyrate | −400 mV vs. SHE | The production of organic acids by current consumption | [ |
Fig. 1Cathodic electron transfer mode. Electrons from a cathode flow into a microbe directly, through direct contact, nanowire, and endogenous mediator; or indirectly, through an artificial mediator, by-product, or EPS
Fig. 2The broad range of redox potential in c-type cytochromes. Considering the possibility of bidirectional electron flow (cathodic, anodic), the broad redox potential suggests the direction of electron flow would be flexible in an electron transfer channel consisting of cytochrome C. The number in a square bracket represents the citation number in the reference list
Predicted electron transfer proteins associated in extracellular electron transfer
| Predicted electron transfer proteins | Active sites | Candidate microorganism associated in extracellular electron transfer | Microorganism used in bioelectrochemical system |
|---|---|---|---|
| Cytochrome C | Heme protein | Metal-reducing bacteria ( |
|
| Ferredoxin | Fe-S protein | Clostridia, acetogens, methanogens |
|
| Rubredoxin | Fe-S protein without acid–labile sulfur | Sulfate-reducing bacteria |
|
| Hydrogenase | [NiFe] or [FeFe] or [Fe]-only | Sulfate-reducing bacteria, methanogen |
|
| Formate dehydrogenase | Molybdenum or tungsten | Sulfate-reducing bacteria |
|
Fig. 3Analogy between metal-utilizing bacteria and direct extracellular electron transfer in a bioelectrochemical system. The left side of the dotted line shows the electron flow with metals in metal-utilizing bacteria and the right side indicates interaction with the electrode
Fig. 4The microbial metabolic pathway of NADH-consuming compound production. One arrow indicates one step of reaction. The butyrate is NADH-balanced and generally produced more than butanol. The NADH reduction (inset) by electricity increases the flux of electron for butanol formation, more NADH-consuming pathway. Fe oxidized form of ferredoxin, Fe reduced form of ferredoxin
Fig. 5The upgrade of waste into value-added biofuels. The acetate from wastes, such as waste activated sludge, food waste, and animal manure, was feed stocks for biofuel production by electroactive microorganisms. The extracellular electron transfer from cathode to microbe via electron transfer protein could be used for the reduction of acetate to butanol. NADH the reduced form, NAD+ the oxidized form of nicotinamide adenine dinucleotide, respectively
Fig. 6The application of bioelectrochemical reduction for cathodic electron transfer from a cathode to a microbe