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Boon, C. Buisman, F. E-mail: blogan psu. When wastewater is used as the fuel for these systems, METs must also accomplish effective treatment. In this presentation, I show that MFCs can be used for domestic wastewater treatment, but the extent of treatment with current generation can be limited. As the concentration of organic matter, measured as chemical oxygen demand COD , decreases in the wastewater, current generation also decreases.

To accomplish effective wastewater treatment additional secondary treatment processes are therefore needed. The main advantage of the AFMBR was little fouling of the membrane over a two-month period no chemical cleaning was needed. The advances made in reducing the costs of MET electrodes, improved power densities over time, and now effective wastewater treatment using the AFMBR demonstrates that METs can be used for commercial wastewater treatment applications.

E-mail: la cornell. For a long time this ield of bioelectrochemistry has been the interest of mainly fundamental researchers. This has signiicantly changed during the last decade and microbial electrochemistry gained increasing interest from applied researchers and engineers. These researchers developed microbial fuel cells MFCs , i.

In addition, a plethora of derivative technologies, such as microbial electrolysis cells MECs , microbial desalination cells MDCs , photomicrobial fuel cells photoMFCs , and microbial batteries, have been introduced. The rapid growth in the development and the interdisciplinarity leads to an ever-growing number of concepts, applications and termini, making it increasingly dificult to classify the technologies under research.

Within this contribution we make the attempt to introduce a classiication of technologies based on interfacing microbiology and electrochemistry. E-mail: johannes. However, the number of exoelectrogenic organisms acting as potential biocatalysts for this type of application is rather limited due to their narrow substrate spectrum. Escherichia coli is the best understood microorganism so far.

It is metabolically versatile and genetically easy tractable. This study describes the process of reprogramming E. Electron transfer into the periplasm of E. STC was identiied as a target for heterologous expression by a two stage screening approach. First, mass spectrometric analysis was conducted to identify natively expressed periplasmic cytochromes in S.

Corresponding genes were cloned and tested for activity in E. Periplasmic electron transfer could be extended to a carbon electrode surface using methylene blue as redox shuttle. Results from irst MEC experiments revealed a shift in the fermentation product spectrum towards more oxidized end-products. In this context a new reactor setup was designed to optimize the analysis of volatile fermentation products. Previous experiments demonstrated that glycerol fermentation of E.

Although methanogens are undesirable in most MEC applications it was shown that the glycerol consumption during the described unbalanced fermentation process could be improved by co-cultivation. Furthermore relevant amounts of current and methane were produced. These results clearly demonstrate that the production of a new electron transport chain enables E. References: [1] Richter, K. FCC Aqualia, S. E-mail: sara. This interesting physiology has been also shown after exploring the interaction bioilm-electrode [2].

The authors have explored now the electron storage concept by using, for irst time, a luid-like anode and plantonik cells of Geobacter sulfurreducens in a Microbial Fluidised Electrochemical Bed Reactor M-FEBR. In this system, the anode is a conductive bed made of electrically conductive microparticles contacting by frequent collisions between them and a polarised current collector, performing continuous charging-discharging processes.

The M-FEBR maximizes the cell-electrode contact due to the proper mixing over other contacting methods in which the anode is fully suspended in a medium. The elimination of radial and axial concentration gradients also allows for better luid-solid contact, which is essential for reaction eficiency. The reactor consisted of a column of 0,6 L of working volume in which the conductive bed was luidised by a recirculation low.

The capacitor-like effect of the heme-network of cytochromes was explored by chronopotenciometry, chronoamperometry and cyclic voltametric analysis with plantonik cells of Geobacter sulfurreducens pre-cultured in a chemostat under electron acceptor-limitation, a condition where cells become electroactive. The recirculation low and consequently the bed expansion were correlated with the harvested current.

This electron storage phenomenon was proportional to the open circuit period charge period. Moreover, discharge kinetics of heme-network was calculated at different redox potential and it was shown to correlate with the heme-network content of the cells. Interestingly, the this effect was strongly inhibited when cytochrome C-free Geobacter cells were used in combination with the luidized conductive bed.

In conclusion, our result reveals the luidised conductive bed as a new tool for exploring electron transfer mechanisms in electrogenic plantonik bacteria in absence of a mature electroactive bioilm. Visconti and D.

Lovley Fluorescent properties of c-type cytochromes reveal their potential role as an extracytoplasmic electron sink in Geobacter sulfurreducens. Environ Microbiol, 10, [2] Schrott, G. Electrochimica Acta. E-mail: b. This process is fundamental in regulating natural geochemical cycles, and can have very detrimental consequences to man-made devices, for example in the case of microbiologically-inluenced corrosion. Notably, these organisms can be used in bioelectrochemical systems electrodes to transform chemical energy into electric energy, and viceversa.

While biomolecules and redox cofactors responsible for electron transfer have been to a great extent identiied, the actual mechanisms of electron transfer remains intensely debated. Here, I present a method based on Raman microscopy, a non-disruptive spectroscopy technique, which proves as very effective for investigations of cytochrome-based extracellular electron transfer reactions. When used in combination of other electrochemical methods, the technique is capable of: 1 characterize the morphology and biochemical composition of the bioilms [1]; and 2 probe variations of the redox state of the main redox cofactors in living electroactive bioilms in their physiological environment, without sample manipulation or ixation [2].

References: [1] Virdis, B. Energ Environ Sci , 5, — [2] Virdis, B. Lacroix 2 , S. Da Silva 2 , E. Trably 1 and N. Bernet 1 1. E-mail: alessandro. Therefore, the objective of this work was to assess the contribution on jmax by both surfaces of a two-side planar anode, i. SCE on which the growth of anodic bioilms of Geoalkalibacter subterraneus [2] was limited by insulating one of the two available surfaces of the anode material.

In multiple replicates, bioilm growth was clearly illustrated as an exponential-like current trend characteristic of high current producing bioilms. Here, jmax for A1 and A2 showed very similar values of 2. Therefore, it is strongly recommend that when utilizing planar anodes as part of the experimental set-up, the totality of the electrode surface is considered for the calculation of jmax.

References: [1] Sharma, M. Acta , In Press. PCCP , 15, 45 , Koch 2 , J. Colprim 1 , J. Harnisch 2 and S. Puig 1 1. E-mail: narcis. One of the most abundant and harmful inorganic ground water contaminants is nitrate. Until now, the microbial community at the cathode has solely been evaluated at the end of the experimental period. However, for future implementation of the technology a more detailed knowledge is required that allows revealing community parameters like stability and evenness.

Therefore, this study presents a continuous monitoring of microbial community, bioelectrochemical activity, and their dynamics during constant operation and stress-tests. The 1L cathode chamber of a BES was illed with granular graphite, decreasing the net volume to 0. The analyses were performed at different sampling points of the cathode. In addition bioelectrochemical characterization using cyclic voltammetry CV was performed to study the microbial extracellular electron transfer EET.

Stress conditions were also evaluated: i changes on low regime, ii starvation period, iii electron acceptor switches NO3-, NO2- , iv pH shifts 6. Structure- function relationships between the microbiome composition, the bioelectrochemical activity and the removal performance were found and the heterogeneity of the cathode chamber was revealed. In summary, the results allowed a better understanding of the underlying fundamentals of denitrifying-BES, which will clearly contribute to improve nitrate treatment in BES.

E-mail: xoch vito. A long trajectory exists on how microbes associate with metals in both natural and man-made environments, from heavy metal remediation to biocorrosion and now with the recent promise of resource recovery. In microbial electrochemical technologies METs , metal recovery is the result of synergistic interactions between metals and electrodes, in which the electron transfer chain associated with microbial respiration plays a key role.

METs can boost metal recovery through several mechanisms. For instance, microbial bioanodes can furnish the driving force totally or partially for abiotic metal recovery at the cathode e. Otherwise, cathodic electrochemically-active microbes may have a more direct role on the reduction of metal ions into solid material.

Thus far, recovery of different metals has been proven at laboratory scale, in both deined media and in wastewaters. U, Fe, Cr, Cu, Hg, Mg, and Ag have been addressed and, more recently, this has been extended to mixed metal solutions i. Cu, Pb, Cd, Zn. These cases will be presented.

This technology may eventually enable economically feasible extraction of metals in so far unprospected environments, as it can cope with low metal concentrations as well as with the presence of organics. Besides, it is not energy intensive as compared to classical electrochemical methods and does not require addition of solvents. Despite its advantages, our modern civilization inds some metals to be more critical than others at speciic times.

Some are critical from the economic perspective whereas for others the risk of supply interruption is paramount. Is MET addressing such metals? An overview of this issue will be also introduced. METs could largely contribute to sustainable recovery of critical metals and reduce the change of supply interruption for those regions where this is a critical matter. Box , FI Tampere, Finland. The sulfur compound containing water streams require treatment, because the biocatalyzed oxidation of RISCs releases protons and may thus cause acidiication of aquatic environments.

The use of reduced inorganic sulfur compounds as substrates in microbial fuel cells MFCs would enable the treatment of the streams with the simultaneous utilization of the energy stored in these compounds. In addition, RISCs could serve as an energy source for the cathodic bioelectrochemical deposition of metals from the same process or waste streams.

The mixed microbial cultures originated from biohydrometallurgical process waters from multimetal ore heap bioleaching. The cultures degraded tetrathionate bioelectrochemically with sulfate as the main reaction product. In addition, elemental sulfur deposited on the anode electrode indicating that the degradation of tetrathionate occurred via disproportionation.

The microbial community analysis showed that the dominant species both in the anolyte and on the anode electrode surface were Acidithiobacillus sp. Although the electricity yields remained low CE 2. C, km 12,1. E Caldes de Montbui, Barcelona, Spain. Abiotic experiments showed that the higher voltage applied, the higher ammonium migration though the cation exchange membrane.

Operating with mineral medium, after 56 hours at 0. Regarding pig slurry, ammonium migration was even higher, rising from Different organic and nitrogen loading rates were tested in stripping system and the highest nitrogen lux 7. Nitrogen lux increased to Under these conditions pH in the cathode chamber went up to The most abundant sequences were afiliated with the family Porphyromonadaceae and the total of OTUs belonging to Proteiniphilum sp.

Regarding the archaea population, under MEC mode a two-fold increase on relative predominance of hydrogenotrophic methanogens such as Methanomicrobiaceae and a non-methanogenic Fervidicoccaceae was oberved, while Methanosaetaceae and Methanosarcinaceae decrease in relative abundance under MEC mode. Buisman 2 and Deepak Pant 1 1. E-mail: suman. Reduction of CO2 to chemicals through microbial electrocatalysis was investigated by using a mixed culture of acetogenic and carboxydotrophic bacteria forming a microbial bioilm supported on a carbon based electrode, as biocathode, in a two chamber reactor.

The bioilm was developed after a start-up phase with fructose and later on, growing on bicarbonate as substrate at suficiently negative cathode potential hydrogen evolution in a couple of subsequent fed- batch operations.

CO2 reduction could occur via direct electron transfer from the electrode or indirectly via mediators or via hydrogen at more reductive potential. Predominantly, Acetic acid was produced along with other volatile fatty acids VFAs while applying Microbial analysis of catholyte at the end of the experiment showed that the bacterial community was dominated by Cellulomonas, Stappia and Pseudomonas spp.

These results suggest that the mixed culture enriched with acetogenic bacteria can catalyze the electro-reduction of CO2 into a number of chemicals like VFAs through direct or indirect electron transfer mechanisms. Gonzalez-Olmos, M. E-mail: pau. However this biogas always requires further treatment, especially to increase the methane CH4 content. Water scrubbing is a widely used biogas upgrading technique which generates an aqueous CO2-enriched low.

Instead of releasing it to the atmosphere, this low could be used to feed microbial electrosynthesis cells, contributing to reduce greenhouse gases emissions. The simulated efluent of a biogas scrubbing-based upgrading unit containing mainly CO2 as carbon source was used in this study to produce CH4 in a bioelectrochemical system BES performing electromethanogenesis.

Cathode potential was poised at mV vs SHE to drive the bioelectrochemical reduction of the absorbed CO2 fraction of the biogas. The highest CH4 production rate was 2. After 10 days, Open cell voltage OCV mode results and our previous studies suggested that methane was exclusively biologically produced using electrons as reducing power source.

As far as authors know this is the irst time that the coupling of biogas upgrading and BES has been studied. The results demonstrated the feasibility of treating the CO2-enriched low generated by a biogas upgrading unit as the inluent of a biocathode performing electromethanogenesis. The combined process could lead to increase the CH4 content of biogas and to implement a new carbon capture technology.

Grote 1 , J. Garrelfs 2 , F. Widdel 2 , M. Stratmann 1 and K. Mayrhofer 2 1. E-mail: p. Of those applications, the most promising microbe — electrode interaction for the conversion of renewable energy into chemical energy, is the direct supply of electrons in the absence of artiicial mediators to microorganisms at cathodes, a process called microbial electrosynthesis [1—3].

Biocatalysts, being highly speciic, are increasingly considered for electrosynthetic processes, for which whole microorganism approaches seem to be most favorable [3]. So far, only mixed environmental cultures have been shown to produce methane from carbon dioxide reduction in microbial electrocatalysis cells.

Moreover, this has for the most part been achieved by mediated electron transfer in which hydrogen obviously had a signiicant inluence on the electron transfer [1,3]. Recently it has been shown, that a newly isolated marine methanogenic Methanobacterium-like archaeon strain IM1 , originally studied for its inluence in microbially inluenced corrosion, has a direct access to electrons from elemental iron [4,5].

Therefore, the ability of strain IM1 to directly utilize electrons from negatively polarized surfaces like graphite electrodes has been investigated with regard to production yield and speciicity of carbon dioxide reduction. A speciic anaerobic bio-electrochemical cell has been connected online to gas chromatography. The combined study of electrochemical parameters and microbial activity for methanogenesis and hydrogen evolution clearly revealed the high eficiency of the process.

This helps to elucidate how the process might be further inluenced for future full — scale applications. References: [1] Lovley, D. A shift in the current: New applications and concepts for microbe- electrode electron exchange.

Microbial electrocatalysis to guide biofuel and biochemical bioprocessing. Biofuels 4, — Microbial electrosynthesis — revisiting the electrical route for microbial production. Iron corrosion by novel anaerobic microorganisms. Nature , — Marine sulfate-reducing bacteria cause serious corrosion of iron under electroconductive biogenic mineral crust. E-mail: stephen. Bio-reinery side streams and wastes tend to have a high organic fraction that is generally destined for anaerobic digestion and ultimately combustion.

Here we present a microbial electrochemical technology that valorises the thin-stillage from a bio-ethanol plant in a so-called Electro-Fermentation process, with simultaneous recovery of the carboxylic acids in a clean, acidic concentrate by membrane electrolysis.

We demonstrate a shift from acetate to butyrate production when current is applied. The shift in product outcome is a result of catholytic electrolysis, as hydrogen and hydroxide are generated from water electrolysis of the fermentation broth. The hydrogen gas can be utilised by the fermenting organisms to drive the reduction to short chain carboxylates such as butyrate, while the hydroxide mitigates the falling pH caused by acidogenic fermentation, as an alternative to pH control by dosing basic chemicals.

In the membrane electrolysis extraction process, the applied current drives the carboxylate products across an anion exchange membrane to a clean, acidic concentrate. In a fully realised system, Electro-Fermentation may enable the rapid fermentation of low value waste streams towards recoverable carboxylate products.

E-mail: marco. The rationale of this study was to couple carbon oxidation and ammonia removal in the anodic compartment to carbon dioxide removal and additional methane formation in the cathode compartment. To accomplish this objectives a bench-scale three-chamber continuous-low MEC was developed, where a biomass-free accumulation chamber was inserted between anodic and cathodic compartments and separated by either protonic or anionic exchange membrane, respectively.

The expected role of the intermediate chamber was to receive both ammonium and bicarbonate ions from the anodic and cathodic compartments respectively. The MEC was continuously operated in a potentiostatic mode with the typical three electrode coniguration, after having inoculated the anodic and cathodic compartments by an activated sludge and an anaerobic sludge, respectively. The MEC performance was assessed through COD and electron balance as well as through removal eficiency of ammonia and carbon dioxide.

E-mail: roberta. The process was mostly investigated in a bench- scale continuous-low reactor where cathodic and anodic compartments were separated by a proton exchange membrane Aulenta et al, Here, for the irst time, a micro-pilot scale reactor was developed as a low-through column with no separation membrane between cathodic and anodic compartments being the needed separation directly obtained by using the downgradient water low along the cathode- anode sequence.

The system was controlled in a galvanostatic mode by applying mA, in large excess of the required current for the RD. The micro-pilot reactor was previously started up with a synthetic medium; then it was also operated by using a real groundwater from a contaminated site in the North of Italy. In the latter step, main attention was given on competing reactions such as nitrate, sulfate and bicarbonate reduction. E-mail: marta.

Speciically, technologies to be developed do not only improve existing treatments in environmental terms even avoiding disposal but also in cost-effectiveness terms generating electricity in the MFC in order to power the sludge treatment. The objective is to develop a reliable, cost-effective and eficient alternative with minimum environmental impacts and without increasing energy consumption. E-mail: sven. To meet these, we envision a new concept in which the enzyme laccase is used to improve the cathode reaction of a microbial fuel cell [1] and to achieve the degradation of micropollutants [2].

As a irst step, we show that the laccase producing fungus T. For T. NHE, respectively. For comparison, signiicantly higher values of 1. Our results are a promising step towards the use of the laccase- secreting T. Further work will focus on the optimization of laccase production, the removal of further micropollutants from wastewater, and the combination of a microbial anode with the enzymatic cathode presented here.

References: [1] S. Shufan et al. E-mail: Jan. Several studies noted that inserting a membrane-less bioelectrochemical system BES inside an anaerobic digester can increase biogas output, however the mechanism behind this was not explored and primary controls were not executed. Lab-scale digesters were operated in the presence or absence of electrodes, and at various applied cell potentials 0, 0. After 91 days of operation, the now colonized electrodes were introduced in the failing AD reactors to evaluate their remediating capacity.

Although a current was generated in the BES operated in closed circuit, no direct effect of applied potential nor current was observed. A high abundance of Methanosaeta sp. This study demonstrates that, in addition to other studies reporting only an increase in methane production, a BES can also remediate AD systems that exhibited process failure.

However, the lack of difference between current driven and open circuit systems indicates that the key impact is most likely through biomass retention, rather than bio electrochemical interaction of the biomass with the electrodes. E-mail: Robert. Brown gmx. The scaling up process of bioelectrochemical systems BES is challenging [1,2] and requires improvements in multiple aspects of the core technology as well as emerging parameters resulting from increasing reactor dimensions.

Therefore a technical scale MEC was constructed and assessed in terms of its wastewater treatment eficiency, Coulomb eficiency and current generation. Synthetic wastewater and real wastewater from a local treatment plant WWTP were anodically treated. The technical scale MEC, when operated in continuous mode at a hydraulic retention time of 1.

We also describe and show a method for comprehensive performance evaluation which takes the above mentioned criteria into account and balances them against shifting loading rates. The model is a mathematical approach based on Gaussian error propagation. The technical scale MEC showed a combined performance factor of 0. While this means that further development is certainly required it also illustrates that it should be possible to develop BES to a state in which they can compete with standard wastewater treatment systems.

References: [1] Kim, D. Scaling-up microbial fuel cells: coniguration and potential drop phenomenon at series connection of unit cells in shared anolyte. ChemSusChem, 5, — Scaling up microbial fuel cells and other bioelectrochemical systems. Evaluating the effects of scaling up on the performance of bioelectrochemical systems using a technical scale microbial electrolysis cell.

E-mail: yifz env. The recent demonstration of nitrate reduction at the cathode of microbial fuel cell MFC provides an opportunity to develop a new technology for nitrogen removal from surface waters. In this study, a sediment-type MFC based on two pieces of bioelectrodes was employed as a novel in situ applicable approach for nitrogen removal, as well as electricity production from eutrophic lakes. The nitrogen removal was almost 4 times higher under close-circuit condition with biocathode, compared to either the open-circuit operation or with abiotic cathode.

The mass balance on nitrogen indicates that most of the removed nitrate and nitrite The nitrogen removal and power generation was limited by the dissolved oxygen DO level in the water and acetate level injected to the sediment. Excessive oxygen resulted in dramatically decrease of nitrogen removal eficiency and only 7. The power generation and nitrogen removal increased with acetate level and was nearly saturated at 0. This bioelectrode-based in situ approach is attractive not only due to the electricity production, but also due to no need of extra reactor construction, which may broaden the application possibilities of sediment MFC technology.

E-mail: Aulenta irsa. Chemical dispersants are frequently employed as a irst response option to an oil spill. While this approach makes the oil spill less visible, dispersants and dispersed oil under the ocean surface are hazardous for marine life. Particularly, once the dispersed oil reaches the sediments it tends to persist there for a very long time due to the prevailing anoxic conditions which drastically limit the occurrence of oxidative biodegradation processes.

The snorkel, takes advantage of the capability of certain bacteria, such as Geobacter spp. The electrons travel from the bottom part of the snorkel anode to the upper part of the snorkel cathode where they reduce oxygen to water. Here, we developed the proof-of-principle of the proposed approach, by using two sets of microcosms, setup using different contaminated marine sediments.

Each set of microcosms consisted of ive different treatments: live microcosms containing 1 or 3 graphite rods, the biotic control without graphite rods, and the abiotic autoclaved controls containing 1 or 3 graphite rods. With both types of sediments, live microcosms containing 1 or 3 graphite rods displayed higher respiratory activities oxygen consumption and carbon dioxide generation and higher rates of hydrocarbons n-alkanes degradation compared to live controls lacking the graphite rod s.

Results were corroborated by molecular analyses of the microbial communities possibly involved in hydrocarbons degradation. Rosenbaum rwth-aachen. Such phenomena have been observed in electro-active communities, where synergistic interactions are employed to enhance electron transfer and eficient substrate utilization.

Several reports have conirmed the evolution of such communities, and more recently, metabolites and fermentation products that are shared between the organisms have been identiied. In some of these reports, Pseudomonas aeruginosa has been found to be ubiquitously present, where it plays a crucial role of phenazine redox mediator production. However, the intricate communication network, especially Quorum Sensing QS in gram negative bacteria, and the physiological roles of these shared metabolites, are yet to be fully understood.

Our study endeavours to understand the role of fermentation products in synergistic interactions of P. We evaluate the performance of the different P aeruginosa type strains, under different ecological conditions and substrates, in bioelectrochemical systems. The QS activity, phenazine redox mediator production and resulting current production under these conditions have been determined.

Our indings provide insights into the optimisation of ecological conditions, to foster synergistic interactions towards increased current production. Since these interactions lead to an overall change in virulence factor generation in P.

E-mail: tristano. Particularly, electrodes can boost microbial metabolism in anaerobic systems as they can represent inexhaustible electron acceptors, with the advantage of providing a more easily modulated redox potential compared to standard, low- reducing redox species that generally drive these systems. This said, bacteria remain the real responsible of pollutants degradation, and Improving our understanding of how METs select speciic population is vital to reine the technology and bring it to the market.

The combination of MET with constructed wetlands have recently resulted in a powerful hybrid technology so-called METland for enhancing the biodegradation rates in wastewater treatment or for reducing the classical constructed wetland dimensions. The diversity of 16S sequences suggests that famous deltaproteobacteria, other metal- reducing microorganisms and syntrophic bacteria generally play an important role in anodic communities; while iron oxidising populations are selected at the cathode.

Furthermore, additional METlands were developed at smaller scale to compare 2 different electrochemical setups MEC-like and short circuit with a classical constructed wetland. Data from 6 more massively sequenced communities showed that the electrochemical circuit coniguration clearly inluenced the composition of bioilms, suggesting that each setup, or a combination of them, can be used to promote speciic microbial actions, where denitriication is of particular interest.

It is foreseen that reducing sequencing costs will allow real-time monitoring of microbial communities, therefore increasing our capacity of controlling their activities through the modulation of redox potential of conductive materials. E-mail: christin. Whereas microbiomes can only be optimized by unrevealing and steering the underlying structure- function relationships most often, however, BES are run on empirical experience and the microbial community is only analyzed sporadically.

This led to, so far, limited insights into the microbiome structure-function relationships in BES. In this contribution it will be demonstrated that cytometric ingerprinting is an excellent method to monitor microbiomes in BES with high resolution and in a fast and cheap manner. A sample speciic cytometric ingerprint typically based on the low-cytometric measurements of cells in 3 minutes is demonstrated to be representative for a microbial community structure and thus can mirror functional community changes.

In conclusion, it will be shown that cytometric ingerprinting allows revealing structure-function relationships of microbiomes in BES and thus its continuous monitoring will allow a steering of BES based on complex microbial communities in future. Investigating its effect is important when considering that mixed communities may also contain photosynthetic bacteria at undetectable levels but which can easily become the dominant members under the right conditions.

Bioanodes were grown as part of double chamber MFCs and in half cells on polarized electrodes both in the absence and presence of light. Results show that light inhibits current production and promotes biofoulling by growth of purple bacteria. It was also shown that bioanodes are inhibited by both oxygen and nitrate. Further to this, performance comparison and community analysis by ion torrent technology was used to build a bigger picture of microbial ecology electrogenic bioilms exposed to light.

These results can be explained by the principle of competitive exclusion which leads to a hierarchy of bacterial preferences for different types of metabolism with electrogenicity being placed at the bottom of this list. In bioelectrochemical systems the energy available for electrogenic bacteria is determined by the potential window between the donor and the anode potential.

In a mature bioanode this has a value of around Bacteria performing anoxygenic photosynthesis have the advantage because they can rely on organic substrate for biomass accumulation only while getting their energy from the light. The results here are applicable to MFCs that use waste water where the bioanodes are constantly exposed to the biodiversity therein. School of Civil Engineering and Geosciences 2. School of Chemical Engineering and Advanced Materials.

E-mail: m. The measurement is based on the amount of oxygen required for microbial oxidation of organic matter. The traditional BOD5 test takes ive days to complete and is unsuitable for process control, and online sensors developed for this purpose have stability and maintenance issues.

BOD measurement is a promising application for Microbial Fuel Cell MFC technology in which current or charge generated can be proportional to the substrate utilised. However, MFC- based sensors to date have had slow response times and limited dynamic range due to substrate saturation of the anode bioilm.

Single-chamber MFCs, batch-fed with artiicial wastewater containing glucose and glutamic acid were operated over several months. At high concentrations the time to reach peak current was on the order of days, which is not suitable for an online sensor. Measuring this parameter allowed BOD5 to be estimated within a response time of ive minutes irrespective of concentration.

A continuous low system with multiple MFCs which have been enriched hydraulically in series has also been developed and it is anticipated that this will allow BOD detection over a much larger dynamic range as substrate can be more completely consumed without saturating the anode.

Donose 2 , Alexander H. Patil 1 , Stefano Freguia 3 , J. E-mail: korneel. However, poor biocompatibility limits its successful application today. Here we report a simple and effective method to make SS electrodes biocompatible by means of lame oxidation. Physicochemical characterization of electrode surface indicated that iron oxide nanoparticles IONPs were generated in situ on SS felt surface by lame oxidation.

IONPs-coating dramatically enhanced the biocompatibility of SS felt and consequently resulted in a robust electroactive bioilm formation at its surface in BESs. These results demonstrate for the irst time that lame oxidized SS felts could be a good alternative to carbon-based electrodes for achieving high current densities in BESs. Most importantly, high conductivity, excellent mechanical strength, strong chemical stability, large speciic surface area, and comparatively low cost of lame oxidized SS felts offer exciting opportunities for scaling-up of the anodes for BESs.

Department of Civil Engineering and Architecture D. E-mail: daniele. The main limitations that delay their industrialization include low current and power densities achievable and high start-up time. This study evaluates the impact of a MPPT system applied to MFCs treating swine wastewater, in terms of start-up time and long-term performance. It was realized by means of an array of digitally controlled potentiometers acting as variable resistor. In this way it was possible to control and set the external electrical load applied to the MFC, in order to reach and follow the maximum power point.

The study demonstrated that the automatic load control was able to reduce the MFC start-up time of about one month with respect to the uncontrolled cell. A power density of 5. Power production and organic matter removal were not affected by the control system application after start-up was inished. To achieve high current and power densities, granular materials are attractive because they provide a cost-effective way to create a high electrode surface area.

At the same time, granular electrodes have limited conductivity, which in combination with electrode spacing result in a high internal resistance especially when used in a larger- scale system. Granular materials, like graphite or activated carbon, have been used to create a high surface area, mostly in a ixed bed reactor, in which the electric current is harvested via a current collector in the form of a graphite rod or a Ti-wire or mesh.

To enhance mass transport, granular materials have been used in a luidized bed reactor, where the electricity was harvested inside the anode compartment. We demonstrate new type of luidized bed reactor, in which the electrons derived from acetate are stored inside capacitive particles in a charging column, and the electricity is harvested in an external electrochemical cell. The reactor had a total anode volume of 2. We show that electricity was successfully harvested at the current collector from the charged particles.

The current density reached a maximum peak of 2. COD removal, Coulombic eficiency, and the performance during intermittent charging and discharging of this capacitive luidized bio-anode are analyzed. Finally, we discuss the merits of this system with external discharge compared to other systems with capacitive granules.

Katuri 1 , Craig M. Werner 1 , Rodrigo J. Amy 1 and Pascal E. E—mail: pascal. A combination of factors hydrogen bubble formation, low cathode potential and localized high pH at the cathode surface contributed to reduced membrane fouling in the AnEMBR compared to the control reactor open circuit voltage.

Jourdin 1,2 , V. Chen 3 , G. Wallace 3 , C. Bogdan 1,2 , S. Freguia 1,2 , and J. Keller 1 1. E-mail: jourdin awmc. Here we report on a novel biocompatible, highly conductive three-dimensional cathode synthesized by direct growth of multi-wall carbon nanotubes CNT on reticulated vitreous carbon, NanoWeb-RVC [1], for the improvement of MES from carbon dioxide.

The CNT surface appears as a ine roughness on the surface. NanoWeb-RVC allows for an enhanced bacterial attachment and bioilm development within its hierarchical porous structure. Moreover, 1. To the best of our knowledge, this is the irst study showing better intrinsic eficiency normalization by total surface area for a three-dimensional biocathode versus a lat electrode.

Unmodiied reticulated vitreous carbon lacking the nanostructure was also tested and found to be far less eficient for MES. The combination of the macrostructured RVC with the nanostructured surface modiication creates signiicant advantages. The high surface area to volume ratio of the macroporous RVC maximizes the available bioilm area while ensuring effective mass transfer to and from the biocatalysts.

The carbon nanostructure, in turn, enhances the microbe-electrode interaction and microbial extracellular electron transfer. When normalized by projected surface area, very high cathodic current density 3. This current density and acetate production rate are the highest reported to date for a cathodic MES. References: [1] Flexer, V. Energy and Environmental Science, E-mail: falk. BES may not only allow turning energy sinks like waste water into a resource, but also hold a promise for further applications like water desalination or production of chemicals.

The beating heart of BES are their bioelectrocatalytic electrodes, where microorganisms utilize different modes EET, that allow the connection of the low of electric current with the electron low of the microbial metabolism. Despite considerable improvement in the understanding as well as engineering of the microbial electrocatalysis, a uniform modelling framework connecting electrochemistry with microbial metabolism is still lacking.

Here such a framework is introduced for bioilms performing direct electron transfer, and benchmarked to experimental results of different researchers, yielding further insights into the principle energetics as well as kinetics of electroactive microorganisms. School of Civil Engineering and Geosciences. Faculty of Science, Agriculture and Engineering. E-mail: e.

At present, Pt is used to catalyse the reaction at the cathode; however its high cost and issues with long term stability could limit its application. To make the MFC technology cheaper and more sustainable, biocathode bioilms comprising mixed communities of aerobic bacteria can be used to catalyse the cathode reaction. Carbon electrodes modiied with these bacteria lower the over-potential required for ORR, but little is understood about the organisms that constitute these bioilms and their mechanisms of electron transfer.

The electrochemical behaviour of these bioilms was studied using Cyclic Voltammetry CV , a powerful method for studying electrochemical systems. A reversible redox feature was observed at the more negative potential of mV and in the absence of O2. This peak was determined to be diffusible by peak analysis, which suggests the use of an electron shuttle by the bacteria.

E-mail: csalgueiro fct. The best studied representative of the Geobacteraceae family is the bacterium Geobacter sulfurreducens Gs , which can transfer electrons towards extracellular acceptors through a process that requires extracellular electron transfer ETT. This is one the most remarkable features of Gs by which it can reduce toxic or radioactive metals and convert renewable biomass into electricity and prompt its selection as a target for practical biotechnological applications [1].

Gs displays a large and diverse number of c-type cytochromes [2], most of which are multihemic proteins that have been shown to be involved in the ETT pathways. Gene knockout and proteomic studies led to the identiication of several periplasmic and outer membrane c-type cytochromes involved in extracellular electron transfer in Gs.

Deletion mutants on these cytochromes revealed their involvement in the reduction of extracellular oxidized metals, such as Fe III , Mn IV or U VI or in electric current production in microbial fuel cells []. However, the elucidation of the extracellular electron transfer pathways in Gs is still in this infancy. New methodological approaches have been developed by our group to functional and structurally study Gs heme proteins, revealing their functional mechanism and key residues involved in their electron transfer capacity [6].

Bridier 1 , E. Rouillac 1 , C. Madigou 1 , E. Blanchet 2 , B. Erable 2 , A. Bergel 2 , A. Carmona 3 , E. Trably 3 , N. Bernet 3 , L. Aissani 4 , L. Giard 4 , L. Renvoise 5 , A. Bize 1 , L. Mazeas 1 and T. Bouchez 1 1. Avenue des Etangs Narbonne, France. Bioelectrochemical systems BES as microbial fuel cells take advantages of microorganisms to convert the chemical energy of organic waste into electricity.

Recently, the discovery that BES can also be used for the synthesis of biocommodities via microbial electrosynthesis MES has greatly expanded the horizons for their applications. Indeed, some microbes are able to use electrons and molecules such as CO2 to synthesize reduced products: volatile fatty acids, alcohols etc By combining both these processes, it should thus theoretically be possible to use the electrons of organic waste to synthesize bio-based chemicals in a clean and controlled compartment.

However, these technologies are only few years old and required scientiic data before they can be practically applied. In this context, we developed a dual-chamber reactor with both biotic anode carbon cloth and cathode stainless steel separated by a cation-exchange membrane. Bioanode was inoculated using an anodic bioilm sample formed in biological wastes and biocathode by injecting a suspension of a homoacetogen-enriched culture.

Chronoamperometry experiments were carried out with a multi-channel potentiostat in order to monitor electroactivity of the microbial communities. However, at the end of the second run, VFAs accumulated with a production rate of acetate reaching 11 g. Microbial diversity proiles showed a switch of archaeal and bacterial populations in cathodic compartment between run 1 and run 2 suggesting that VFAs production resulted from microbial adaptation to the addition of BES in the cathodic compartment.

Overall this work constitutes a irst step toward the utilization of MES systems for the conversion of organic wastes into biofuels and chemicals using coupled bioanode and biocathodes. It has been argued that fostering bioelectrochemical methane production rather than avoiding it, could help to solve these limitations, thus improving the technical and economic feasibility of MEC technology.

Therefore, methane production MECs could serve as an intermediate step that would facilitate the implementation of MEC technology at a commercial scale. We used a semi-pilot 3L membrane-less reactor provided with two independent MEC units connected electrically in parallel. In a second set of tests, the MEC was operated in continuous mode with three aims: to analyze the scalability of our set-up, to compare methane production with conventional hydrogen production in terms of energy consumption, energy recovery and WW treatment eficiency analyzing pro and cons of both approaches, and to determine the effect of the hydraulic retention time on methane production.

Rapid conversion of hydrogen to methane in our reactor allowed to curb problems associated PITCH PP to hydrogen management such as hydrogen recycling and as a consequence helped to improve the energy eficiency. However we also identiied additional limitations. For instance, relatively high solubility of methane in water limited energy recovery.

E-mail: sylvia. Whereas production rates are limited by product accumulation, reversely the still-low concentrations preclude conventional product recovery. Here we present a novel three-compartment electrochemical cell reactor design for simultaneous bioproduction and product extraction. This cell combines a cathode compartment for microbial electrosynthesis MES , a membrane electrolysis step for extraction of the produced acetate, and an acid-generating anode. The acetate is trapped in its acidic form in the low pH middle compartment and formation of chlorinated by-products at the anode is avoided using a second membrane.

E-mail: tatiana. A recent derivative of BES is microbial electrosynthesis. In this approach, microorganisms take up electrons from a cathode and reduce carbon dioxide to yield industrially relevant organic compounds that can readily be stored and utilized.

So far, only few electrosynthetic microorganisms have been identiied. For an effective electrochemical screening and identiication of such organisms, this study aimed to develop a time-saving medium-throughput BES system in order to evaluate microbial ability to accept reducing equivalents from a cathode and later perform a characterization of the potential candidates. A six-well disposable reactor was designed and developed for the anaerobic potentiostatic screening experiments.

From the screening, the two most promising cathode-active strains were Desulfosporosinus orientis and Sulfurimonas denitriicans with produced currents in the range of In order to characterize these strains, the current experiments are performed in ml bench-top reactors from which liquid and gas samples are analyzed. Quantitative essays of sessile and planktonic cells together with speciic electrochemical techniques are being performed to better understand the underlying mechanisms.

The ability of microorganisms to take up electrons from a cathode has a wide range of potential applications. However, further studies about the rate and the route of electrons transfer between electrodes and microorganisms are crucial for any successful application.

Centro de Desarrllo Urbano Sustentable, Santiago. Chile 3. E-mail: itvargas ing. Santiago, Chile. Telephone: 56 2 , Fax: In recent years, acid mine drainage AMD treatment is a major focus of interest for the mining industry worldwide. AMD occurs when sulphide minerals are exposed to air and water, producing runoff with high acidity and high concentrations of metal and non-metal ions.

The low pH and high concentrations of metal ions have adverse effects on ecosystems, polluting ground and surface waters. Northern Chile is known for its rich mining. It also represents a privileged site for the study of complex and extreme microbiological systems. High concentrations of dissolved metals, low pH, high metal concentration in soils and sediments, and extreme climatic conditions represent the opportunity to explore novel electroactive microorganisms able to reduce or oxidize extracellular substrates.

We investigated the potential of acid-tolerant microorganisms extracted from an AMD-affected soil in Northern Chile to generate current in microbial fuel cell MFC systems. The results showed that under anaerobic conditions the microorganisms were able to survive between pH 3. Hence, MFC performance, together with microscopy and molecular analysis, suggested the presence of acid-tolerant anodic microbial community.

The results presented in this study are signiicant because they represent an initial approach to characterize and understand the potential of acid-tolerant microorganisms in MFC systems. E-mail: david. These authors contributed equally to this work. Microbial fuel cells can be operated with oxygen reducing biocathodes. Several mixed microbial communities have been reported to show robust bioelectrocatalysis of oxygen reduction over time at applicable operation conditions.

Still, clariication of electron transfer mechanism s and identiication of essential micro-organisms have not been realised. Objective of this study was to shape oxygen reducing biocathodes with different microbial communities by means of surface modiication in order to clarify the relation of microbial composition and performance. Resulting mixed culture biocathodes included complex bacterial bioilms as well as protozoa. The best performing biocathode reached a high current density 0.

A remarkable correlation was found between performance and enrichment of the dominating micro-organisms. Members of this group can likely be considered as key-players for high performing oxygen reducing biocathodes. This study shows that the open environment of oxygen reducing cathodes is selective for effective microbial catalysts.

University of Alcala. Madrid, Spain. E-mail: ainara. However, the availability of suitable electron acceptors to sustain microbial respiration can reduce the microbial detoxiication activity. The concept of using electrodes to overcome this metabolic limitation led recently to the concept of Microbial Electroremediating Cells MERCs 1. In contrast with standard environmental applications as sedimentary Microbial Fuel Cells sMFC , MERCs do not aim power production but to maximize biodegradation rates around the electrode by offering a never-ending electron sink.

Our work demonstrates that natural population can be effectively stimulated by MERCs in order to bioremediate a soil polluted with the herbicide atrazine 2-chloroethylamino isopropyl amino-1,3,5-triazine. Residual concentration of atrazine was ca. Furthermore, the effective removal of pollutants was supported by ecotoxicological analysis, based on algal growth assays, with a severe reduction in soil toxicity ca. References: [1] Rodrigo, J.

Rodrigo, J. In this study, we developed a novel hybrid system, consisted of a submersed microbial resource recovery cell SMRC and a continuous stirred tank reactor CSTR , to prevent ammonia toxicity during anaerobic digestion by in-situ ammonia recovery and electricity production. In batch experiment, the ammonia concentration in the CSTR decreased from 6 to 0. Meanwhile, a maximum power density of 0. With an increase in initial ammonia concentration and a decrease in external resistance, the SMRC performance was enhanced.

In addition, the coexistence of other cations in CSTR or cathode had no negative effect on the ammonia transportation. High-throughput molecular sequencing analysis showed an impact of PITCH PP ammonia recovery on the microbial community composition in the integrated system.

Results clearly indicate the great potential of the SMRC-CSTR-coupled system for eficient and cost-effective ammonia recovery, energy production and treatment of ammonia-rich residues. Sleutels 1 , R. Saakes 1 , A. E-mail: Pau. RodenasMotos wetsus. Copper and other metals are getting scarcer on new mining ores, but everyday more present in water and soils. We report high currents and high power densities with a Microbial Fuel Cell MFC for copper recovery using acetate as electron donor and copper sulphate solution as electron acceptor.

The cell was constructed using an Anion Exchange Membrane AEM , carbon felt and a lat copper electrode all of them with a surface of cm2. Current density of A stable current of 19 Am-2 was achieved and maintained for days with a power output of 3. The recovery eficiency of copper was In this presentation we will show that the membrane and the eficiency of the anode are the limiting steps inside the MFC. These Limiting processes, like: presence of methanogen bacteria, side reactions and scaling on membrane surface will be further explained and analysed.

Sire 2 , E. Trably 1 , N. Bernet 1 and J. Steyer 1 1. E-mail: antonella. This industry generates large volumes of olive brine wastewater OBWW which is rich in organic matter and contains a considerable amount of salt together with a signiicant content of polyphenolic compounds. Therefore OBWWs are dificult to treat through conventional technologies. Specially, since polyphenolic compounds are toxic for biological processes and microbial inhibition is known to occur due to the high salt content.

Thus, the most current treatment of OBWWs is their direct discharge into evaporation ponds. The objective of this work is to demonstrate the possibility to apply bioelectrochemical systems to recover energy from OBWWs. The experiments were conducted in single chamber potentiostatically controled systems fed with real OBWW provided from a regional olive cooperative, using a moderate halophilic consortium sediments from a salt plant as biocatalyst.

Chronoamperometry CA was used to monitor the transfer of charge to the anode while successful electroactive bioilm growth and electrochemical behavior were evaluated using cyclic voltammetry CV. Biogas production mainly CH4 and polyphenol degradation were also evaluated. It will provide new insights into the knowledge of anode respiring communities which are able to degrade OBWWs.

In comparison the control reactor, with no applied potential, showed no CH4 production. Moreover, in order to improve the eficiency of the process, an enrichment procedure of electroactive bioilm was evaluated. Three consecutive CA cycles using acetate as substrate were performed before exposing the formed bioilms to real OBWW.

After the enrichment strategy, despite the maximum current density obtained 5. The MFC performance was evaluated in terms of power density, substrate degradation, energy conversion eficiency and shifts in system redox state with operation time and organic loading rate OLR.

The pH showed initial rapid drop and luctuations initially when shifted to DFE but adapted over time. DFE consisted of residual sugars from irst stage process along with the volatile fatty acids and alcohols, which contributed for the generation of organic acids with their simultaneous consumption and lead to VFA increment in spite of COD removal. Cyclic voltammograms along with the derived electro-kinetics supported the observed shifts. E-mail: august. And on the other hand, thanks to the diffusion from anode to cathode compartment, ammonium can be removed and recovered.

A series of batch assays were performed using a pair of identical two-chamber cells operated in MFC and MEC mode, equipped with a cation exchange membrane. Results of the MFC operation phosphate buffer solution as catholyte when was fed with raw pig slurry showed a COD removal in 24 hours of The ammonium removal was COD removals decreased to 6.

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The best answers are voted up and rise to the top. Stack Overflow for Teams — Start collaborating and sharing organizational knowledge. Create a free Team Why Teams? Learn more. Frequency shifting of a quadrature mixed signal Ask Question. Asked 6 years ago. Modified 2 years, 3 months ago. Viewed 11k times. Improve this question. Peter K. Sumbul Sumbul 1 1 gold badge 4 4 silver badges 15 15 bronze badges.

Add a comment. Sorted by: Reset to default. Highest score default Date modified newest first Date created oldest first. Further details for the very interested to understand complex frequency translation: The following additional figures and content were added to help answer the question on the subsequent down-conversion and to build a better understanding of the complex positive and negative frequency domain in describing frequency translation implementations.

Improve this answer. Dan Boschen Dan Boschen 37k 2 2 gold badges 39 39 silver badges bronze badges. Thank you for catching that; I made the correction. Jason R Jason R Your answer still applies without the baseband restriction. Perhaps better stated :If you have a quadrature-mixed signal, I assume you mean that you have two real signals in 90 degree phase to each other" Of course it's not necessary to implement it that way, but it shows that any quadrature modulation needs something that can be viewed as a complex baseband signal.

You always need two signals to modulate the two orthogonal carriers. It's just not limited to what would typically be called baseband signals; complete modulations at carrier frequencies can also be translated with the same process. Viewing this in the complex, meaning positive and negative frequency spectrum makes this very easy to follow what is happening, knowing that a real signal is replicated conjugate symmetric in the positive and negative frequency, and a complex signal can exist in just one or the other or both and be different.

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Hot Network Questions. Design an FIR bandpass filter with passband between 0. The first stopband goes from 0 to 0. The second stopband goes from 0. Compute the frequency response. Plot its magnitude in both linear units and decibels. Highlight the passband. Design a 3rd-order highpass Butterworth filter having a normalized 3-dB frequency of 0. Compute its frequency response.

Express the magnitude response in decibels and plot it. Its operation is similar to that of freqz ; you can specify a number of frequency points to use, supply a vector of arbitrary frequency points, and plot the magnitude and phase response of the filter. This example shows how to compute and display analog frequency responses.

Design a 5th-order analog Butterworth lowpass filter with a cutoff frequency of 2 GHz. Compute the frequency response of the filter at points. Design a 5th-order Chebyshev Type I filter with the same edge frequency and 3 dB of passband ripple.

Design a 5th-order Chebyshev Type II filter with the same edge frequency and 30 dB of stopband attenuation. Design a 5th-order elliptic filter with the same edge frequency, 3 dB of passband ripple, and 30 dB of stopband attenuation. The Chebyshev Type I and elliptic filters roll off faster but have passband ripple.

The frequency input to the Chebyshev Type II design function sets the beginning of the stopband rather than the end of the passband. Choose a web site to get translated content where available and see local events and offers. Based on your location, we recommend that you select:. Select the China site in Chinese or English for best site performance.

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