Anodic electro-fermentation of 3-hydroxypropionic acid from glycerol by recombinant Klebsiella pneumoniae L17 in a bioelectrochemical system
© The Author(s) 2017
Received: 11 March 2017
Accepted: 10 August 2017
Published: 17 August 2017
3-Hydroxypropionic acid (3-HP) is an important platform chemical which can be produced biologically from glycerol. Klebsiella pneumoniae is an ideal biocatalyst for 3-HP because it can grow well on glycerol and naturally synthesize the essential coenzyme B12. On the other hand, if higher yields and titers of 3-HP are to be achieved, the sustained regeneration of NAD+ under anaerobic conditions, where coenzyme B12 is synthesized sustainably, is required.
In this study, recombinant K. pneumoniae L17 overexpressing aldehyde dehydrogenase (AldH) was developed and cultured in a bioelectrochemical system (BES) with the application of an electrical potential to the anode using a chronoamperometric method (+0.5 V vs. Ag/AgCl). The BES operation resulted in 1.7-fold enhancement of 3-HP production compared to the control without the applied potential. The intracellular NADH/NAD+ ratio was significantly lower when the L17 cells were grown under an electric potential. The interaction between the electrode and overexpressed AldH was enhanced by electron shuttling mediated by HNQ (2-hydroxy-1,4-naphthoquinone).
Enhanced 3-HP production by the BES was achieved using recombinant K. pneumoniae L17. The quinone-based electron transference between the electrode and L17 was investigated by respiratory uncoupler experiments. This study provides a novel strategy to control the intracellular redox states to enhance the yield and titer of 3-HP production as well as other bioconversion processes.
Keywords3-hydroxypropionic acid Electro-fermentation Bioelectrochemical system Klebsiella pneumoniae L17
3-hydroxypropionic acid (3-HP; C3H6O3) has attracted interest because of its wide applications in the synthesis of various value-added chemicals, such as acrylic acid, acrylamide, and propiolactone [1, 2]. According to a report by the U.S. Department of Energy, 3-HP is one of the top 12 value-added platform chemicals that can be produced biologically but the process requires urgent development . To date, many studies including the development of genetically and metabolically engineered microbial strains have been conducted to improve the yield and titer for the commercial production of 3-HP [4–7]. 3-HP can be produced from glucose and glycerol as the carbon sources, both of which are renewable and abundant.
Klebsiella pneumoniae is a natural 3-HP producer with several advantages in 3-HP production over other strains. The strain can grow well on glycerol to a high cell density at a fast rate even under anaerobic condition. In addition, it expresses a coenzyme B12-dependent GDHt (called DhaB) that is less sensitive to oxygen than the SAM-dependent GDHt. Furthermore, it can produce sufficient amounts of coenzyme B12 for the catalysis of DhaB under anaerobic conditions . In comparison, most well-known fermentative hosts, such as E. coli do not grow well on glycerol under anaerobic conditions and cannot produce coenzyme B12. Coenzyme B12 is very expensive ($531/g), making it unsuitable for addition directly to the culture medium. On the other hand, K. pneumoniae was reported to produce up to 83.8 g/L of 3-HP without the external supplementation of coenzyme B12, which provides a great advantage of mass production of 3-HP . For the successful production of 3-HP by K. pneumoniae, the overexpression and/or heterologous expression of highly active AldH is essential due to the low innate AldH activity in the wild-type strains .
The reaction by AldH generates NADH from NAD+ by the oxidation of 3-HPA to 3-HP; consequently, the continuous regeneration of NAD+ is crucial, as shown in Fig. 1. If NAD+ is not regenerated properly, this reaction would stop immediately. Furthermore, a high cellular NADH level due to its improper oxidation to NAD+ causes the accumulation of undesired byproducts, such as lactate and ethanol. The simplest and most inexpensive way for NAD+ regeneration is to accelerate the electron transport chain (ETC). However, NAD+ regeneration via aerobic respiration is not preferred when using K. pneumoniae as a host for 3-HP production from glycerol. Under aerobic conditions, expression of the DHA regulon, which includes dhaB, and the coenzyme B12 synthetic pathway are significantly suppressed. In addition, the DhaB enzyme and its cofactor, coenzyme B12, are unstable under aerobic conditions [11, 12]. To solve this problem, anaerobic respiration using a chemical electron acceptor, such as nitrate, has been attempted, but it is expensive and the reduction of nitrate yields nitrite, which is toxic and seriously inhibits the cellular metabolism [9, 13].
Some microorganisms, called exoelectrogens, can deliver respiratory electrons to solid electrodes under anaerobic conditions. The microbe–electrode interaction via extracellular electron transfer to an electrode is intriguing because it offers an alternative way to control the cellular redox states, and does not rely on ETC or fermentation (e.g., production of reduced metabolites) . The use of a bioelectrochemical system enables thermodynamically unfeasible metabolisms, i.e., unbalanced fermentation, to proceed. Proof-of-concept experimental results have already been presented for electrochemically active microbes, such as Geobacter sulfurreducens [15, 16], Shewanella oneidensis MR-1 [17, 18], and K. pneumoniae L17 . The production of biochemicals and biofuels with the bioelectrochemical system has also been investigated, e.g., butyrate production with Clostridium tyrobutyricum by instigating a cathodic reduction reaction  and the production of electron-dense metabolites (such as butanol and 1,3-propanediol) by C. pasteurianum . Nevertheless, most of these studies focused on cathode-based electro-fermentation rather than an anode-based process. For anode-based studies, the production of ethanol and acetate by engineered E. coli and the production of ethanol by a co-culture of G. sulfurreducens and C. cellobioparum have been attempted; however, the metabolite titers were neither reported nor enhanced significantly compared to those in the conventional, non-bioelectrochemical system [22, 23].
In this study, anodic electro-fermentation by recombinant K. pneumoniae L17 was investigated for the production of 3-HP from glycerol (see the Additional file 1: Figure S1). This paper reports that the conventional limitation of the redox imbalance in fermentation can be overcome using bioelectrochemical system approaches. The results show that overexpressed AldH and the use of an electrode is well coordinated via a microbial anaerobic respiratory module. To the best of the authors’ knowledge, this is the first report of the successful application of the anodic electro-fermentation, and an improvement of 3-HP production.
Bacterial strains and media composition
To develop efficient 3-HP producer strains, K. pneumoniae L17 (herein after L17W) and E. coli DH5ɑ were purchased from CCTCC (China Center for Type Culture Collection) and KCCM (Korean Culture Center of Microorganisms), respectively. The recombinant K. pneumoniae strain was prepared using the pUC19/KGSADH vector, which is well-developed for high rates of expression of aldehyde dehydrogenase (AldH), with KGSADH (ɑ-ketoglutaric semialdehyde dehydrogenase) . The transformation of pUC19/KGSADH to K. pneumoniae L17 (herein after L17K) was conducted using the method reported elsewhere . Additional file 1: Table S1 lists the bacterial strains and plasmids used in this study (Additional file 1: Table S1). For strain maintenance, all strains used in this study were grown in LB medium and stored at −80 °C. The modified M9 medium was used for the 3-HP fermentation experiments using the following composition (per liter): 1 g NaCl, 1 g NH4Cl, 0.25 g MgSO4·7H2O, 13.53 g K2HPO4, 3.03 g KH2PO4, 1 g yeast extract, 2 g glucose, 11.05 g glycerol, 12.5 ml vitamin solution , and 12.5 ml trace element solution . The medium was adjusted to pH 7.2 using 10% HCl and 5 N NaOH solutions. A 0.1 mM solution of filter-sterilized HNQ (2-hydroxy-1,4-naphthoquinone, neutral orange 6) was added to the anode chamber as an electron shuttle between the bacteria and electrode.
Bioelectrochemical system (BES) configuration
H-type BES reactors were constructed from two glass bottles (310 ml capacity each, Duran, USA) with a glass tube bridge (inner diameter: 1.25 cm) containing a proton exchange membrane (PEM, Nafion 117, Dupont, Del. USA). A 20 wt% wet-proof carbon cloth (Nara Cell-Tech Co., Korea) was used for both the anode and cathode electrodes (2 cm × 5 cm). A Ag/AgCl electrode was installed in the anode chamber as the reference electrode. The anode chamber was filled with 250 mL of modified M9 medium. A 100 mM potassium ferricyanide solution dissolved in a 100 mM potassium phosphate solution (pH = 7.5) was added to the cathode chamber. All the components were pre-washed with 10% of HCl and 5 N NaOH solutions. The medium and BES reactors were sterilized at 121 °C for 15 min by autoclaving. Before starting the experiments, all strains tested were pre-cultured overnight in LB medium, and incubated for 12 h in M9 medium for activation. The pre-cultivated cells were inoculated in the anode chamber to an initial cell concentration of OD600 = 0.05. A 100 μM solution of ampicillin (L17W) or 50 μM of kanamycin (L17K) was added to the anode and cathode chamber to prevent contamination and plasmid stabilization.
Both the anode and cathode electrodes were connected via a 1 kΩ external resistance or a potentiostat for closed circuit operation (BES operating condition), whereas in non-BES operation, the anode was not connected to the resistance and cathode electrode (i.e., open circuit). Hence, the anode electrode in non-BES reactors does not accept the respiratory electrons produced from the metabolic pathway. Both BES and non-BES reactors were placed in a shaking incubator at 37 °C at 100 rpm. Before starting the BES experiments, both the anode and cathode chambers were purged with 99.9% of nitrogen gas to remove the dissolved oxygen. In the recombinant strain experiments, 0.2 mM of IPTG was added to induce AldH expression. The poised potential was applied to the anode using chronoamperometry (+0.5 V vs. Ag/AgCl) and a potentiostat (VersaSTAT 3, AMETEK, USA). The average current was monitored at 1 min intervals during the BES operation for glycerol fermentation.
To determine the electron transfer mechanism between the anode electrode and bacterial anaerobic respiration for 3-HP production, the BES reactors were operated under spontaneous electron discharge to the anode with a fixed resistance (1 kΩ), instead of using a potentiostat. All the operating conditions were the same as those of the BES reactors described previously. The effect of the respiratory inhibitors such as rotenone (1 mM in final), antimycin A (0.5 μM), sodium azide (1 mM) were investigated in the BES reactor. The control BES reactor contained the same amount of ethanol and DI water, and was connected to a fixed resistance (1 kΩ). The current generation and 3-HP production with the different inhibitors were monitored.
Cell growth, pH change, NADH/NAD+ ratio, and metabolites production were determined by sampling the fermentation broth from the anode chamber at 0, 3, 6, 8, 12, 24, and 32 h. Planktonic cell growth and pH were determined by measuring the optical density (600 nm wavelength) and using a pH meter, respectively. The liquid samples were centrifuged at 5000 rpm for 10 min. The NADH/NAD+ ratio of the pellets was analyzed by colorimetric kit quantification (Biovision, USA), as described previously . The supernatants were filtered using a syringe filter (0.22 μm, Nylon membrane, Whatman, UK). The filtered samples were analyzed to identify the metabolite concentrations by high performance liquid chromatography (HPLC, HP 1160 series, Agilent Technologies, USA) equipped with a 300 × 7.8 mm Aminex HPX-87H (Bio-Rad, USA) column at 65 °C and a refractive index (RI) and photodiode array (PDA) detector, using 2.5 mM H2SO4 as the mobile phase (flow rate = 0.5 mL/s). The currents generated were analyzed by a computer-based data acquisition (DAQ) system (NI-USB6218; National Instruments, USA) with LabVIEW™ (National Instruments, USA).
Results and discussion
Electron transfer to the anode electrode by L17W and L17K
Glycerol consumption and production of metabolites in BES
Carbon and electron distributions of L17 under different operating conditions
Transferred electron to electrode (mmol)
Glycerol to 3-HPAa
3-HPA to 3-HPb
14.1 ± 2.1
27.4 ± 4.7
12.1 ± 1.1
26.9 ± 1.7
21.5 ± 2.2
9.5 ± 3.6
12.9 ± 3.2
15.4 ± 4.6
Shift of the cellular redox balance under BES conditions
The addition of HNQ to the culture medium can enhance the quinone shuttle-based electron transfer to the electrode, and activate the anaerobic respiratory pathways of K. pneumoniae L17 . The metabolic flux under anaerobic conditions proceeds in a similar manner to that under (micro) aerobic conditions. Similar results were obtained in Shewanella sp. under MFC conditions, as reported by Matsuda et al. . The introduction of AldH to K. pneumoniae increases electron transfer to the electrode significantly, as shown in Fig. 2. In a previous report, the K. pneumoniae DSMZ overexpressing AldH reduced more nitrate than the wild-type counterpart . The improvement of anaerobic respiration (via nitrate reduction) was attributed to the coordination of NAD+-dependent oxidase (i.e., AldH) and NADH oxidoreductase (i.e., NADH:Ubiquinone reductase).
In the other glycerol assimilation pathways, the dha modules consist of two reaction pathways involved in two associated enzymes, glycerol dehydrogenase (DhaD) with dihydroxyacetone kinase (DhaK), and glycerol dehydratase (DhaB) with propanediol oxidoreductase (DhaT). In the glycerol-reductive pathway catalyzed by DhaB, 3-HPA can be converted to either 3-HP or 1,3-PDO. The production of these two metabolites is conducted by controversial reactions, 3-HPA reduction for 1,3-PDO production (NADH-dependent propanediol dehydrogenase, dhaT) or 3-HPA oxidation for 3-HP production (NAD+-dependent aldehyde dehydrogenase, puuC). Therefore, the 1,3-PDO: 3-HP ratio was governed by the cellular redox states. The glycerol-reductive pathways are more highly activated under anaerobic conditions (i.e., high NADH/NAD+ ratio conditions); therefore, most of the 3-HPA would be transformed to 1,3-PDO in wild-type K. pneumoniae. In balanced fermentation (i.e., conventional fermentation), predominant 3-HP production from glycerol is practically difficult; therefore, co-production with 1,3-PDO was examined to simultaneously improve the titer and/or yield of 3-HP production by maintaining the cellular redox potential [27–30]. In this study, the electrode-based control of the cellular redox potential was applied to promote unbalanced fermentation with a decreased intracellular NADH level. These results suggest that the poised potential (+0.5 V vs. Ag/AgCl) can be applied to bioproduction not only for 3-HP biosynthesis, but also for the production of various biochemicals, which are required to overcome the thermodynamic barriers by changing the intracellular NADH/NAD+ level.
Effects of the respiratory inhibitors on current generation and 3-HP production
On the other hand, significantly less current and concurrently lower 3-HP production were obtained without HNQ, a quinone analogue (Fig. 5). This suggests that the electron shuttle (HNQ) pumps out the respiratory electron from putative quinone reductase on the cytoplasmic membrane, so that a lower NADH/NAD+ ratio can be maintained within the cell. These results suggest that shuttle-based electron transport is more dominant for 3-HP production in BES than direct electron transport. The NADH dehydrogenase II complex might act as an electron carrier between aldehyde dehydrogenase and the quinone pool, but it was not inhibited by the inhibitors tested.
BES-based electron transport chain for 3-HP production
To implement a BES-based cellular redox control strategy into a bioprocess, an understanding of the electron transfer mechanisms and the effects of an externally poised potential on the production rate (3-HP in this study) are needed. Although previous studies revealed various spontaneous electron transfer modules in exoelectrogens, the mechanisms of quinone-based electron transfer have not been examined extensively. In the present study, it was hypothesized that the externally added quinone derivative mediator (HNQ) might interact with the respiratory enzymes, e.g., NADH dehydrogenase complex I and quinone:cytochrome c oxidoreductase. Interestingly, no significant difference in current generation and 3-HP production rate were observed in the presence of rotenone and antimycin A, which are inhibitors used widely for NADH dehydrogenase complex I and quinone:cytochrome c oxidoreductase, respectively (Fig. 5).
The substitution of a petroleum-based chemical refinery with a sustainable biorefinery has been highlighted as one of the future goals of green technology. With the help of the recent advances in multi-OMICS and innovative bioprocesses, the biological production of various platform chemicals and an improvement of their yield/titer have become easier. Nevertheless, regulation and control of the cellular redox potential to improve the yield/selectivity and reduce the production cost, remains a challenge. Electro-fermentation is a promising alternative to traditional redox control methods, such as oxygen sparging, and the addition of co-substrates and chemical reagents . Furthermore, electro-fermentation can provide a tool to break the theoretical maximum productivity of conventional fermentation, which is set by the innate cellular metabolism. The strategy suggested in the present study can be also used as an energy storage and efficient utilization method for electrical energy from diverse electricity-based renewable energy and a carbon-neutral power plant with the simultaneous production of high value-added chemicals .
This paper is the first report on the enhancement of 3-HP bioproduction using electro-fermentation. The BES-based cellular redox control strategy demonstrated proof-of-principle, even though the 3-HP titer and volumetric productivity so far lack the levels for industrial relevance. To achieve industrial-scale application, further study will be needed to develop a large-scale and cost-effective BES reactor for electro-fermentation, by implementing electrode-based anodic and cathodic reactors. The membrane-based BES processes (e.g., electrodialysis) which proceed the production and separation of products simultaneously, have been extensively investigated, and are highly applicable to electro-fermentation [35–38]. The finely tunable electrochemical control strategy as well as genetic and metabolic engineering to redirect the metabolic fluxes and remove the byproduct production pathways, are also anticipated.
The application of a bioelectrochemical system facilitated the enhanced production of 3-HP via the activation of anaerobic respiration to regulate the NADH/NAD+ ratio. The overexpressed AldH and electrode-based respiration mediated by an electron shuttle resulted in higher 3-HP production under BES conditions. This study provides a novel strategy to control the cellular redox states to overcome the yield and titer limited in conventional fermentation, which can be applied not only to 3-HP production, but also to other bioconversion processes through altered cell redox states.
CK and JK designed the experiments and research. CK and MK performed experiments and analyses, and prepared the manuscript draft. CK, IM, BJ, GP, SP, and JK analyzed the results, and provided appropriate comments and revision. JK worked for manuscript completion and submission as corresponding author. All authors read and approved the final manuscript.
This study was supported by C1 Gas Refinery Program through the National Research Foundation of Korea (NRF) funded by the Ministry of Science, ICT & Future Planning (NRF-2016M3D3A1A01913248), and by the Mid-career Researcher Program (2013069183) through the National Research Foundation of Korea (NRF).
The authors declare that they have no competing interests.
Springer Nature remains neutral with regard to jurisdictional claims in published maps and institutional affiliations.
Open AccessThis article is distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution, and reproduction in any medium, provided you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons license, and indicate if changes were made. The Creative Commons Public Domain Dedication waiver (http://creativecommons.org/publicdomain/zero/1.0/) applies to the data made available in this article, unless otherwise stated.
- Della Pina C, Falletta E, Rossi M. A green approach to chemical building blocks. The case of 3-hydroxypropanoic acid. Green Chem. 2011;13:1624–32.View ArticleGoogle Scholar
- Kumar V, Ashok S, Park S. Recent advances in biological production of 3-hydroxypropionic acid. Biotechnol Adv. 2013;31:945–61.View ArticleGoogle Scholar
- Werpy T, Petersen G, Aden A, Bozell J, Holladay J, White J, Manheim A, Eliot D, Lasure L, Jones S. Top value added chemicals from biomass. New York: U.S. Department of Energy; 2004.Google Scholar
- Jung WS, Kang JH, Chu HS, Choi IS, Cho KM. Elevated production of 3-hydroxypropionic acid by metabolic engineering of the glycerol metabolism in Escherichia coli. Metab Eng. 2014;23:116–22.View ArticleGoogle Scholar
- Li Y, Wang X, Ge X, Tian P. High production of 3-hydroxypropionic acid in Klebsiella pneumoniae by systematic optimization of glycerol metabolism. Sci Rep. 2016;6:26932. doi:10.1038/srep26932.View ArticleGoogle Scholar
- Lim HG, Noh MH, Jeong JH, Park S, Jung GY. Optimum rebalancing of the 3-hydroxypropionic acid production pathway from glycerol in Escherichia coli. ACS Synth Biol. 2016;5:1247–55.Google Scholar
- Sankaranarayanan M, Ashok S, Park S. Production of 3-hydroxypropionic acid from glycerol by acid tolerant Escherichia coli. J Ind Microbiol Biotechnol. 2014;41:1039–50.View ArticleGoogle Scholar
- Jiang X, Meng X, Xian M. Biosynthetic pathways for 3-hydroxypropionic acid production. Appl Microbiol Biotechnol. 2009;82:995–1003.View ArticleGoogle Scholar
- Ashok S, Raj SM, Ko Y, Sankaranarayanan M, Zhou S, Kumar V, Park S. Effect of puuC overexpression and nitrate addition on glycerol metabolism and anaerobic 3-hydroxypropionic acid production in recombinant Klebsiella pneumoniae ΔglpKΔdhaT. Metab Eng. 2013;15:10–24.View ArticleGoogle Scholar
- Ko Y, Ashok S, Zhou S, Kumar V, Park S. Aldehyde dehydrogenase activity is important to the production of 3-hydroxypropionic acid from glycerol by recombinant Klebsiella pneumoniae. Process Biochem. 2012;47:1135–43.View ArticleGoogle Scholar
- Keuth S, Bisping B. Vitamin B12 production by Citrobacter freundii or Klebsiella pneumoniae during tempeh fermentation and proof of enterotoxin absence by PCR. Appl Environ Microbiol. 1994;60:1495–9.Google Scholar
- Ye K, Shijo M, Jin S, Shimizu K. Efficient production of vitamin B12 from propionic acid bacteria under periodic variation of dissolved oxygen concentration. J Ferment Bioeng. 1996;82:484–91.View ArticleGoogle Scholar
- Gonzalez P, Correia C, Moura I, Brondino C, Moura J. Bacterial nitrate reductases: molecular and biological aspects of nitrate reduction. J Inorg Biochem. 2006;100:1015–23.View ArticleGoogle Scholar
- Lovley DR, Nevin KP. A shift in the current: new applications and concepts for microbe-electrode electron exchange. Curr Opin Biotechnol. 2011;22:441–8.View ArticleGoogle Scholar
- Segura D, Mahadevan R, Juárez K, Lovley DR. Computational and experimental analysis of redundancy in the central metabolism of Geobacter sulfurreducens. PLoS Comput Biol. 2008;4:e36.View ArticleGoogle Scholar
- Yang TH, Coppi MV, Lovley DR, Sun J. Metabolic response of Geobacter sulfurreducens towards electron donor/acceptor variation. Microb Cell Fact. 2010;9:1.View ArticleGoogle Scholar
- Biffinger JC, Ray R, Little BJ, Fitzgerald LA, Ribbens M, Finkel SE, Ringeisen BR. Simultaneous analysis of physiological and electrical output changes in an operating microbial fuel cell with Shewanella oneidensis. Biotechnol Bioeng. 2009;103:524–31.View ArticleGoogle Scholar
- Tang YJ, Meadows AL, Kirby J, Keasling JD. Anaerobic central metabolic pathways in Shewanella oneidensis MR-1 reinterpreted in the light of isotopic metabolite labeling. J Bacteriol. 2007;189:894–901.View ArticleGoogle Scholar
- Kim C, Ainala SK, Oh Y-K, Jeon B-H, Park S, Kim JR. Metabolic flux change in Klebsiella pneumoniae L17 by anaerobic respiration in microbial fuel cell. Biotechnol Bioprocess Eng. 2016;21:250–60.View ArticleGoogle Scholar
- Choi C, Cui Y. Recovery of silver from wastewater coupled with power generation using a microbial fuel cell. Bioresour Technol. 2012;107:522–5.View ArticleGoogle Scholar
- Choi O, Kim T, Woo HM, Um Y. Electricity-driven metabolic shift through direct electron uptake by electroactive heterotroph Clostridium pasteurianum. Sci Rep. 2014;4:6961.View ArticleGoogle Scholar
- Speers AM, Young JM, Reguera G. Fermentation of glycerol into ethanol in a microbial electrolysis cell driven by a customized consortium. Environ Sci Technol. 2014;48:6350–8.View ArticleGoogle Scholar
- Sturm-Richter K, Golitsch F, Sturm G, Kipf E, Dittrich A, Beblawy S, Kerzenmacher S, Gescher J. Unbalanced fermentation of glycerol in Escherichia coli via heterologous production of an electron transport chain and electrode interaction in microbial electrochemical cells. Bioresour Technol. 2015;186:89–96.View ArticleGoogle Scholar
- Fournet-Fayard S, Joly B, Forestier C. Transformation of wild type Klebsiella pneumoniae with plasmid DNA by electroporation. J Microbiol Methods. 1995;24:49–54.View ArticleGoogle Scholar
- Kim JR, Premier GC, Hawkes FR, Rodríguez J, Dinsdale RM, Guwy AJ. Modular tubular microbial fuel cells for energy recovery during sucrose wastewater treatment at low organic loading rate. Bioresour Technol. 2010;101:1190–8.View ArticleGoogle Scholar
- Matsuda S, Liu H, Kouzuma A, Watanabe K, Hashimoto K, Nakanishi S. Electrochemical gating of tricarboxylic acid cycle in electricity-producing bacterial cells of Shewanella. PLoS ONE. 2013;8:e72901.View ArticleGoogle Scholar
- Ashok S, Raj SM, Rathnasingh C, Park S. Development of recombinant Klebsiella pneumoniae ∆dhaT strain for the co-production of 3-hydroxypropionic acid and 1, 3-propanediol from glycerol. Appl Microbiol Biotechnol. 2011;90:1253–65.View ArticleGoogle Scholar
- Huang Y, Li Z, Shimizu K, Ye Q. Simultaneous production of 3-hydroxypropionic acid and 1, 3-propanediol from glycerol by a recombinant strain of Klebsiella pneumoniae. Bioresour Technol. 2012;103:351–9.View ArticleGoogle Scholar
- Huang Y, Li Z, Shimizu K, Ye Q. Co-production of 3-hydroxypropionic acid and 1, 3-propanediol by Klebseilla pneumoniae expressing aldH under microaerobic conditions. Bioresour Technol. 2013;128:505–12.View ArticleGoogle Scholar
- Kumar V, Sankaranarayanan M, Jae KE, Durgapal M, Ashok S, Ko Y, Sarkar R, Park S. Co-production of 3-hydroxypropionic acid and 1, 3-propanediol from glycerol using resting cells of recombinant Klebsiella pneumoniae J2B strain overexpressing aldehyde dehydrogenase. Appl Microbiol Biotechnol. 2012;96:373–83.View ArticleGoogle Scholar
- Elbehti A, Brasseur G, Lemesle-Meunier D. First evidence for existence of an uphill electron transfer through the bc1 and NADH-Q oxidoreductase complexes of the acidophilic obligate chemolithotrophic ferrous ion-oxidizing bacterium Thiobacillus ferrooxidans. J Bacteriol. 2000;182:3602–6.View ArticleGoogle Scholar
- Rothery RA, Chatterjee I, Kiema G, Mcdermott MT, Weiner JH. Hydroxylated naphthoquinones as substrates for Escherichia coli anaerobic reductases. Biochem J. 1998;332:35–41.View ArticleGoogle Scholar
- Schievano A, Sciarria TP, Vanbroekhoven K, De Wever H, Puig S, Andersen SJ, Rabaey K, Pant D. Electro-fermentation-merging electrochemistry with fermentation in industrial applications. Trends Biotechnol. 2016;34:866–78.View ArticleGoogle Scholar
- Moscoviz R, Toledo-Alarcón J, Trably E, Bernet N. Electro-fermentation: how to drive fermentation using electrochemical systems. Trends Biotechnol. 2016;34:856–65.View ArticleGoogle Scholar
- Zhang Y, Olias LG, Kongjan P, Angelidaki I. Submersible microbial fuel cell for electricity production from sewage sludge. Water Sci Technol. 2011;64:50–5.View ArticleGoogle Scholar
- Zhang Y, Angelidaki I. Bioelectrochemical recovery of waste-derived volatile fatty acids and production of hydrogen and alkali. Water Res. 2015;81:188–95.View ArticleGoogle Scholar
- Kim C, Lee CR, Song YE, Heo J, Choi SM, Lim D-H, Cho J, Park C, Jang M, Kim JR. Hexavalent chromium as a cathodic electron acceptor in a bipolar membrane microbial fuel cell with the simultaneous treatment of electroplating wastewater. Chem Eng J. 2017;328:703–7. doi:10.1016/j.cej.2017.07.077.View ArticleGoogle Scholar
- Gildemyn S, Verbeeck K, Slabbinck R, Andersen SJ, Prévoteau A, Rabaey K. Integrated production, extraction, and concentration of acetic acid from CO2 through microbial electrosynthesis. Environ Sci Technol Lett. 2015;2:325–8. doi:10.1021/acs.estlett.5b00212.View ArticleGoogle Scholar