Thea Bursac, Jeffrey A. Gralnick, Johannes Gescher

Biotechnology and Bioengineering • 2017

This study describes the realization of an anoxic acetoin production process using the proteobacterium Shewanella oneidensis. Fermentative processes are of high biotechnological relevance since they offer high productivity and a low percentage of substrate consumption for anabolic processes. Nevertheless, the range of compounds that can be produced as sole end product of a fermentative process is limited, since the average oxidation state of substrate and products has to be identical in the absence of an external electron acceptor. This limitation could be overcome by the transfer of the surplus of electrons to a poised electrode surface, which of note is the only known anaerobic electron acceptor that cannot be depleted. In the first genetic engineering step, deletion mutants were developed that are devoid of either one, two, or all three prophages in their genome with the aim to construct a more stable chassis strain for microbe-electrode interaction, due to less prophage induced cell lysis (Gödeke et al., 2011). Current production in a bioelectrochemical system together with the analysis of cells on the anode surface were used as surrogate for the stability assessment. The λ-prophage deletion mutant produced overall 1.34fold more current (6.7 μA cm -2 ) than the wild type and all other constructed strains and showed with 1.1 × 10 11 cells the highest cell density on the anode surface (2.3fold more than the wild type). The strain was further modified to contain codon optimized versions of acetolactate synthase and acetolactate decarboxylase derived from Bacillus subtilis. This allowed for the production of a mixture of acetoin and acetate from lactate in an almost 0.4:1 ratio. Further process improvement was reached by the deletion of the acetate kinase and phosphotransacetylase genes ackA/pta. The acetoin yield increased in this mutant from 40 to 86% of the theoretical maximum and acetoin was the only detectable end product. Biotechnol. Bioeng. 2017;114: 1283-1289. © 2017 Wiley Periodicals, Inc.

Francisco Lopez Moruno, Juan E. Rubio, Plamen Atanassov et al.

Bioelectrochemistry • 2018

Microbial desalination cell (MDC) is a bioelectrochemical system capable of oxidizing organics, generating electricity, while reducing the salinity content of brine streams. As it is designed, anion and cation exchange membranes play an important role on the selective removal of ions from the desalination chamber. In this work, sulfonated sodium (Na + ) poly(ether ether ketone) (SPEEK) cation exchange membranes (CEM) were tested in combination with quaternary ammonium chloride poly(2,6-dimethyl 1,4-phenylene oxide) (QAPPO) anion exchange membrane (AEM). Non-patterned and patterned (varying topographical features) CEMs were investigated and assessed in this work. The results were contrasted against a commercially available CEM. This work used real seawater from the Pacific Ocean in the desalination chamber. The results displayed a high desalination rate and power generation for all the membranes, with a maximum of 78.6±2.0% in salinity reduction and 235±7mWm -2 in power generation for the MDCs with the SPEEK CEM. Desalination rate and power generation achieved are higher with synthesized SPEEK membranes when compared with an available commercial CEM. An optimized combination of these types of membranes substantially improves the performances of MDC, making the system more suitable for real applications.

Zheng Xiaomei, Rujing Lin, Xu Jun et al.

Chemical Engineering Journal • 2022

Siddharth Gadkari, Mobolaji Shemfe, J. Annie Modestra et al.

Physical Chemistry Chemical Physics • 2019

This study describes and evaluates a dynamic computational model for a two chamber microbial electrosynthesis (MES) system. The analysis is based on redox mediators and a two population model, describing bioelectrochemical kinetics at both anode and cathode. Mass transfer rates of the substrate and bacteria in the two chambers are combined with the kinetics and Ohm's law to derive an expression for the cell current density. The effect of operational parameters such as initial substrate concentration at the anode and cathode and the operation cycle time on MES performance is evaluated in terms of product formation rate, substrate consumption and coulombic efficiency (CE). For a fixed operation cycle time of 3 or 4 days, the anode and cathode initial substrate concentrations show linear relationship with product formation rate; however MES operation with a 2 day cycle time shows a more complex behaviour, with acetic acid production rates reaching a plateau and even a slight decrease at higher concentrations of the two substrates. It is also shown that there is a trade-off between product formation rate and substrate consumption and CE. MES performance for operation with cycle time being controlled by substrate consumption is also described. Results from the analysis demonstrate the interdependence of the system parameters and highlight the importance of multi-objective system optimization based on targeted end-use.

Dmitry Pankratov, Galina Pankratova, Lo Gorton

Current Opinion in Electrochemistry • 2019

Xuejun Yan, Hyung‐Sool Lee, Nan Li et al.

Renewable and Sustainable Energy Reviews • 2020

M. Engel, Dirk Holtmann, Roland Ulber et al.

Biotechnology Journal • 2018

A future bio-economy should not only be based on renewable raw materials but also in the raise of carbon yields of existing production routes. Microbial electrochemical technologies are gaining increased attention for this purpose. In this study, the electro-fermentative production of biobutanol with C. acetobutylicum without the use of exogenous mediators is investigated regarding the medium composition and the reactor design. It is shown that the use of an optimized synthetic culture medium allows higher product concentrations, increased biofilm formation, and higher conductivities compared to a synthetic medium supplemented with yeast extract. Moreover, the optimization of the reactor system results in a doubling of the maximum product concentrations for fermentation products. When a working electrode is polarized at -600 mV vs. Ag/AgCl, a shift from butyrate to acetone and butanol production is induced. This leads to an increased final solvent yield of Y ABE = 0.202 g g -1 (control 0.103 g g -1 ), which is also reflected in a higher carbon efficiency of 37.6% compared to 23.3% (control) as well as a fourfold decrease in simplified E-factor to 0.43. The results are promising for further development of biobutanol production in bioelectrochemical systems in order to fulfil the principles of Green Chemistry.

Bin Lai, Hans Schneider, Jenny Tschörtner et al.

Biotechnology and Bioengineering • 2021

A carbon-free energy supply is essential to sustain our future. Biophotovoltaics (BPV) provides a promising solution for hydrogen supply by directly coupling light-driven water splitting to hydrogen formation using oxygenic photoautotrophic cyanobacteria. However, BPV is currently limited by its low photon-to-current efficiency, and current experimental setups at a miniaturized scale hinder the rational investigation of the process and thus system optimization. In this article, we developed and optimized a new technical-scale (~250 ml working volume) BPV platform with defined and controllable operating parameters. Factors that interfered with reproducible and stable current output signals were identified and adapted. We found that the classical BG11 medium, used for the cultivation of cyanobacteria and also in many BPV studies, caused severe interferences in the bioelectrochemical experiments. An optimized nBG11 medium guaranteed a low and stable background current in the BPV reactor, regardless of the presence of light and/or mediators. As proof-of-principle, a very high long-term light-dependent current output (peak current of over 20 µA) was demonstrated in the new set-up over 12 days with living Synechocystis sp. PCC6803 cells and validated with appropriate controls. These results report the first reliable BPV platform generating reproducible photocurrent while still allowing quantitative investigation, rational optimization, and scale-up of BPV processes.

Yu-Li Yang, Xiaojin Li, Xiao-Li Yang et al.

Bioresource Technology • 2017

Erick M. Bosire, Miriam A. Rosenbaum

Frontiers in Microbiology • 2017

Pseudomonas aeruginosa has gained interest as a redox mediator (phenazines) producer in bioelectrochemical systems. Several biotic and abiotic factors influence the production of phenazines in synergy with the central virulence factors production regulation. It is, however, not clear how the electrochemical environment may influence the production and usage of phenazines by P. aeruginosa . We here determined the influence of the electrochemical potential on phenazine production and phenazine electron transfer capacity at selected applied potentials from -0.4 to +0.4 V (vs. Ag/AgCl sat ) using P. aeruginosa strain PA14. Our study reveals a profound influence of the electrochemical potential on the amount of phenazine-1-carboxylate production, whereby applied potentials that were more positive than the formal potential of this dominating phenazine (E ° ' PCA = -0.24 V vs. Ag/AgCl sat ) stimulated more PCA production (94, 84, 128, and 140 μg mL -1 for -0.1, 0.1, 0.2, and 0.3 V, respectively) compared to more reduced potentials (38, 75, and 7 μg mL -1 for -0.4, -0.3, and -0.24 V, respectively). Interestingly, P. aeruginosa seems to produce an additional redox mediator (with E ° ' ∼ 0.052 V) at applied potentials below 0 V, which is most likely adsorbed to the electrode or present on the cells forming the biofilm around electrodes. At fairly negative applied electrode potentials, both PCA and the unknown redox compound mediate cathodic current generation. This study provides important insights applicable in optimizing the BES conditions and cultures for effective production and utilization of P. aeruginosa phenazines. It further stimulates investigations into the physiological impacts of the electrochemical environment, which might be decisive in the application of phenazines for electron transfer with P. aeruginosa pure- or microbial mixed cultures.

Theresia Desy Askitosari, Santiago T. Boto, Lars M. Blank et al.

Frontiers in Microbiology • 2019

Phenazine-1-carboxylic acid (PCA) and its derivative pyocyanin (PYO) are natural redox mediators in bioelectrochemical systems and have the potential to enable new bioelectrochemical production strategies. The native producer Pseudomonas aeruginosa harbors two identically structured operons in its genome, which encode the enzymes responsible for PCA synthesis [ phzA1-G1 (operon 1), phzA2-G2 (operon 2)]. To optimize heterologous phenazines production in the biotech host Pseudomonas putida KT2440, we compared PCA production from both operons originating from P. aeruginosa strain PAO1 ( O1.phz1 and O1.phz2 ) as well as from P. aeruginosa strain PA14 ( 14.phz1 and 14.phz2 ). Comparisons of phenazine synthesis and bioelectrochemical activity were performed between heterologous constructs with and without the combination with the genes phzM and phzS required to convert PCA to PYO. Despite a high amino acid homology of all enzymes of more than 97%, P. putida harboring 14.phz2 produced 4-times higher PCA concentrations (80 μg/mL), which resulted in 3-times higher current densities (12 μA/cm 2 ) compared to P. putida 14.phz1. The respective PCA/PYO producer containing the 14.phz2 operon was the best strain with 80 μg/mL PCA, 11 μg/mL PYO, and 22 μA/cm 2 current density. Tailoring phenazine production also resulted in improved oxygen-limited metabolic activity of the bacterium through enhanced anodic electron discharge. To elucidate the reason for this superior performance, a detailed structure comparison of the PCA-synthesizing proteins has been performed. The here presented characterization and optimization of these new strains will be useful to improve electroactivity in P. putida for oxygen-limited biocatalysis.

Max Hackbarth, Tobias Jung, Johannes Eberhard Reiner et al.

Chemical Engineering Journal • 2020

Feng Li, Lei Wang, Chen‐Guang Liu et al.

Current Opinion in Electrochemistry • 2018

Gunda Mohanakrishna, Riyadh I. Al‐Raoush, Ibrahim M. Abu-Reesh

Bioresource Technology • 2018

Yanzhuang Liu, Changfei Gao, Lifen Liu et al.

Water Research • 2025

Douglas M. Hodgson, Ann Smith, Sonal Dahale et al.

Frontiers in Microbiology • 2016

Metabolic interactions within microbial communities are essential for the efficient degradation of complex organic compounds, and underpin natural phenomena driven by microorganisms, such as the recycling of carbon-, nitrogen-, and sulfur-containing molecules. These metabolic interactions ultimately determine the function, activity and stability of the community, and therefore their understanding would be essential to steer processes where microbial communities are involved. This is exploited in the design of microbial fuel cells (MFCs), bioelectrochemical devices that convert the chemical energy present in substrates into electrical energy through the metabolic activity of microorganisms, either single species or communities. In this work, we analyzed the evolution of the microbial community structure in a cascade of MFCs inoculated with an anaerobic microbial community and continuously fed with a complex medium. The analysis of the composition of the anodic communities revealed the establishment of different communities in the anodes of the hydraulically connected MFCs, with a decrease in the abundance of fermentative taxa and a concurrent increase in respiratory taxa along the cascade. The analysis of the metabolites in the anodic suspension showed a metabolic shift between the first and last MFC, confirming the segregation of the anodic communities. Those results suggest a metabolic interaction mechanism between the predominant fermentative bacteria at the first stages of the cascade and the anaerobic respiratory electrogenic population in the latter stages, which is reflected in the observed increase in power output. We show that our experimental system represents an ideal platform for optimization of processes where the degradation of complex substrates is involved, as well as a potential tool for the study of metabolic interactions in complex microbial communities.

Suman Bajracharya, Karolien Vanbroekhoven, Cees J.N. Buisman et al.

Faraday Discussions • 2017

The recent concept of microbial electrosynthesis (MES) has evolved as an electricity-driven production technology for chemicals from low-value carbon dioxide (CO 2 ) using micro-organisms as biocatalysts. MES from CO 2 comprises bioelectrochemical reduction of CO 2 to multi-carbon organic compounds using the reducing equivalents produced at the electrically-polarized cathode. The use of CO 2 as a feedstock for chemicals is gaining much attention, since CO 2 is abundantly available and its use is independent of the food supply chain. MES based on CO 2 reduction produces acetate as a primary product. In order to elucidate the performance of the bioelectrochemical CO 2 reduction process using different operation modes (batch vs. continuous), an investigation was carried out using a MES system with a flow-through biocathode supplied with 20 : 80 (v/v) or 80 : 20 (v/v) CO 2 : N 2 gas. The highest acetate production rate of 149 mg L -1 d -1 was observed with a 3.1 V applied cell-voltage under batch mode. While running in continuous mode, high acetate production was achieved with a maximum rate of 100 mg L -1 d -1 . In the continuous mode, the acetate production was not sustained over long-term operation, likely due to insufficient microbial biocatalyst retention within the biocathode compartment (i.e. suspended micro-organisms were washed out of the system). Restarting batch mode operations resulted in a renewed production of acetate. This showed an apparent domination of suspended biocatalysts over the attached (biofilm forming) biocatalysts. Long term CO 2 reduction at the biocathode resulted in the accumulation of acetate, and more reduced compounds like ethanol and butyrate were also formed. Improvements in the production rate and different biomass retention strategies (e.g. selecting for biofilm forming micro-organisms) should be investigated to enable continuous biochemical production from CO 2 using MES. Certainly, other process optimizations will be required to establish MES as an innovative sustainable technology for manufacturing biochemicals from CO 2 as a next generation feedstock.

Yanping Hou, Yuanyuan Gan, Zebin Yu et al.

Journal of Power Sources • 2017

Luís F. M. Rosa, Steffi Hunger, Carla Gimkiewicz et al.

Engineering in Life Sciences • 2016

The reactor systems used for microbial electrosynthesis, i.e. bioelectrochemical systems for achieving bioproduction so far reported in literature are relatively small in scale and highly diverse in their architecture and modes of operation. The often diverging requirements of the electrochemical and the biological processes and the interdisciplinarity of the field make the engineering of these systems a special challenge. This has led to multiple, differently optimized approaches of reactor vessels, designs and operating conditions making standardization and normalization or even a systematic engineering almost impossible. Overcoming this lack of standardization, scalability and knowledge-driven engineering is the driving force for this work introducing an upgrade kit for bioreactors transforming these reversibly to bioelectroreactors. The prototypes of the bioreactor upgrade kit were integrated with commercial bioreactor (fermentor) systems and performances compared to a classic, small-scale bioelectrochemical glass cell system. The use of the upgrade kit allowed interfacing with the existing infrastructure of the conventional bioreactors for growing electroactive microorganisms in pure culture conditions, with the added electrochemical control and further process monitoring. The results of growing Shewanella oneidensis MR-1 clearly show that these systems can be used to control, monitor, and scale microbial bioelectrochemical processes, providing better resolution of the data for the tested experimental conditions.

Shuai Luo, John A. Berges, Zhen He et al.

Algal Research • 2016

Chuanqi Liu, Jiewen Xiao, Haoyong Li et al.

Water Research • 2021

Zhengwen Zhang, Yuxing Han, Chunyan Xu et al.

Bioresource Technology • 2019

Weining Sun, Zhufan Lin, Qingzi Yu et al.

Frontiers in Microbiology • 2021

The low efficiency of extracellular electron transfer (EET) is a major bottleneck for Shewanella oneidensis MR-1 acting as an electroactive biocatalyst in bioelectrochemical systems. Although it is well established that a periplasmic c -type cytochrome ( c -Cyt) network plays a critical role in regulating EET efficiency, the understanding of the network in terms of structure and electron transfer activity is obscure and partial. In this work, we attempted to systematically investigate the impacts of the network components on EET in their absence and overproduction individually in microbial fuel cell (MFC). We found that overexpression of c -Cyt CctA leads to accelerated electron transfer between CymA and the Mtr system, which function as the primary quinol oxidase and the outer-membrane (OM) electron hub in EET. In contrast, NapB, FccA, and TsdB in excess severely impaired EET, reducing EET capacity in MFC by more than 50%. Based on the results from both strategies, a series of engineered strains lacking FccA, NapB, and TsdB in combination while overproducing CctA were tested for a maximally optimized c -Cyt network. A strain depleted of all NapB, FccA, and TsdB with CctA overproduction achieved the highest maximum power density in MFCs (436.5 mW/m 2 ), ∼3.62-fold higher than that of wild type (WT). By revealing that optimization of periplasmic c -Cyt composition is a practical strategy for improving EET efficiency, our work underscores the importance in understanding physiological and electrochemical characteristics of c -Cyts involved in EET.

Hou-Yun Yang, Jing Liu, Yixuan Wang et al.

Bioelectrochemistry • 2019

Steven Chu, Yi Cui, Nian Liu

Nature Materials • 2016

Rohan Kumar, Tuhin Banerji

Biomass and Bioenergy • 2026

A‐Andrew D. Jones, Cullen Buie

Scientific Reports • 2019

Electroactive bacteria such as Geobacter sulfurreducens and Shewanella onedensis produce electrical current during their respiration; this has been exploited in bioelectrochemical systems. These bacteria form thicker biofilms and stay more active than soluble-respiring bacteria biofilms because their electron acceptor is always accessible. In bioelectrochemical systems such as microbial fuel cells, corrosion-resistant metals uptake current from the bacteria, producing power. While beneficial for engineering applications, collecting current using corrosion resistant metals induces pH stress in the biofilm, unlike the naturally occurring process where a reduced metal combines with protons released during respiration. To reduce pH stress, some bioelectrochemical systems use forced convection to enhance mass transport of both nutrients and byproducts; however, biofilms' small pore size limits convective transport, thus, reducing pH stress in these systems remains a challenge. Understanding how convection is necessary but not sufficient for maintaining biofilm health requires decoupling mass transport from momentum transport (i.e. fluidic shear stress). In this study we use a rotating disc electrode to emulate a practical bioelectrochemical system, while decoupling mass transport from shear stress. This is the first study to isolate the metabolic and structural changes in electroactive biofilms due to shear stress. We find that increased shear stress reduces biofilm development time while increasing its metabolic rate. Furthermore, we find biofilm health is negatively affected by higher metabolic rates over long-term growth due to the biofilm's memory of the fluid flow conditions during the initial biofilm development phases. These results not only provide guidelines for improving performance of bioelectrochemical systems, but also reveal features of biofilm behavior. Results of this study suggest that optimized reactors may initiate operation at high shear to decrease development time before decreasing shear for steady-state operation. Furthermore, this biofilm memory discovered will help explain the presence of channels within biofilms observed in other studies.

Chi‐Wen Lin, Yao-Long Fan, Wenfei Huang et al.

Journal of Industrial and Engineering Chemistry • 2025

Guiqin Yang, Lingyan Huang, Zhen Yu et al.

Water Research • 2019

Ningyuan Zhu, Jun Tang, Cilai Tang et al.

Chemical Engineering Journal • 2018

Felix Tetteh Kabutey, Qingliang Zhao, Liangliang Wei et al.

Renewable and Sustainable Energy Reviews • 2019

Nyambane Clive Ontita, Emmanuel Konadu Sarkodie, Richmond Anaman et al.

Journal of Water Process Engineering • 2024

Thi Thu Ha Nguyen, Giang T.H. Le, Sung-Gwan Park et al.

The Science of The Total Environment • 2024

Ruggero Rossi, Xu Wang, Bruce E. Logan

Journal of Power Sources • 2020

Zhou Fang, Xian Cao, Xuexiao Li et al.

International Biodeterioration & Biodegradation • 2018

Adam Oodally, Mohamedjaffer Gulamhussein, D.G. Randall

Journal of Water Process Engineering • 2019

Dan‐Dan Zhai, Zhen Fang, Hongwei Jin et al.

Bioresource Technology • 2019

Jun Yan, Xuebin Hu, Qiang He et al.

Water Research • 2021

Olga Tkach, Thangavel Sangeetha, Spiridonova Maria et al.

Journal of Environmental Sciences • 2016

Indrajit Chakraborty, Gourav Dhar Bhowmick, Debanjali Ghosh et al.

Sustainable Energy Technologies and Assessments • 2020