- Open Access
“NiCo Buster”: engineering E. coli for fast and efficient capture of cobalt and nickel
- Alexandre Duprey1, 3,
- Viviane Chansavang1,
- Franck Frémion1,
- Clémence Gonthier1,
- Yoann Louis2,
- Philippe Lejeune3,
- Fanny Springer2,
- Valérie Desjardin2,
- Agnès Rodrigue†3 and
- Corinne Dorel†2Email author
© Duprey et al.; licensee BioMed Central Ltd. 2014
- Received: 18 February 2014
- Accepted: 13 July 2014
- Published: 1 August 2014
Metal contamination is widespread and results from natural geogenic and constantly increasing anthropogenic sources (mainly mining and extraction activities, electroplating, battery and steel manufacturing or metal finishing). Consequently, there is a growing need for methods to detoxify polluted ecosystems. Industrial wastewater, surface water and ground water need to be decontaminated to alleviate the contamination of soils and sediments and, ultimately, the human food chain. In nuclear power plants, radioactive metals are produced; these metals need to be removed from effluents before they are released into the environment, not only for pollution prevention but also for waste minimization. Many physicochemical methods have been developed for metal removal from aqueous solutions, including chemical coagulation, adsorption, extraction, ion exchange and membrane separation; however, these methods are generally not metal selective. Bacteria, because they contain metal transporters, provide a potentially competitive alternative to the current use of expensive and high-volume ion-exchange resins.
The feasibility of using bacterial biofilters as efficient tools for nickel and cobalt ions specific remediation was investigated. Among the factors susceptible to genetic modification in Escherichia coli, specific efflux and sequestration systems were engineered to improve its metal sequestration abilities. Genomic suppression of the RcnA nickel (Ni) and cobalt (Co) efflux system was combined with the plasmid-controlled expression of a genetically improved version of a specific metallic transporter, NiCoT, which originates from Novosphingobium aromaticivorans. The resulting strain exhibited enhanced nickel (II) and cobalt (II) uptake, with a maximum metal ion accumulation of 6 mg/g bacterial dry weight during 10 min of treatment. A synthetic adherence operon was successfully introduced into the plasmid carrying the improved NiCoT transporter, conferring the ability to form thick biofilm structures, especially when exposed to nickel and cobalt metallic compounds.
This study demonstrates the efficient use of genetic engineering to increase metal sequestration and biofilm formation by E. coli. This method allows Co and Ni contaminants to be sequestered while spatially confining the bacteria to an abiotic support. Biofiltration of nickel (II) and cobalt (II) by immobilized cells is therefore a promising option for treating these contaminants at an industrial scale.
- Synthetic biology
Metals are commonly used by industry but are generally harmful for the environment . Consequently, liquid effluents need to be decontaminated, not only when heavy metal concentrations are high but also when concentrations are low to avoid bioaccumulation because these substances display long-term persistence in sediments. Chemical and physical methods (for example, chemical precipitation and ionic exchange resins) can be ineffective or extremely expensive when the metals ions are present at micromolar concentrations . In the context of nuclear power plants, radioactive hazard adds to the natural toxicity of the metals used; thus, their removal from effluents is critical. Among the metals released by the types of steel alloy used in pipes, two are of particular importance: (i) nickel, which is present in low concentrations (approximately 1 mM)  and (ii) cobalt, notably its activated radioisotope 60Co, which is present in trace quantities (approximately 20 nM ) but is particularly harmful due to its long half-life (5.27 years) and emission of high energy γ rays (1.17 and 1.33 MeV) . Current methods of removing these metals ions involve the use of ion-exchange resins, which, although efficient, are non-selective, expensive and require the use of high volumes to decontaminate metals at low concentrations, especially cobalt, resulting in high treatment costs . The removal and concentration of these metals is achieved using large volumes of resin, which then have to be treated as radioactive waste involving long-term storage in dedicated centers until the radioisotopes have decayed. Thus, the need for space is critical in radioactive waste storage, and demand is high for cheaper, more specific solutions that reduce the volumes involved.
For decades, the use of biological tools has been suggested as an efficient and cost-effective solution for metal remediation . Non-living biomass biosorbents (algae, fungal, yeast or bacterial biomass) can be used to immobilize heavy metals with low selectivity [2, 4, 7]. Engineered and non-engineered bacteria (e.g., Escherichia coli, Deinococcus radiodurans, Citrobacter sp.) have been tested for use in the remediation of metals such as mercury  and uranium . Indeed, bacteria grow rapidly in liquid media, can use a wide variety of nutrients and have developed many efficient mechanisms to resist and detoxify harmful metals . Some bacteria can live under extreme conditions, such as D. radiodurans, which can grow in the presence of 60 Gy/h; thus, this organism exhibits potential for use in treating liquid radioactive waste. Another important issue in bioremediation is the recovery of the biosorbent that contains the heavy metals. Developing a process that minimizes costs while efficiently separating solids from liquid is challenging. Flocculent S. cerevisiae cells and calcium alginate beads containing D. radiodurans bind metals ions efficiently and can be removed easily from the treated solution [7, 11]. Magnetic chitosan, a modified biopolymer, has been used successfully to remove Cu(II), Co(II) and Ni(II) ions from aqueous solutions; however, this approach requires multi-step extraction and modification processes to prepare the chelating resin .
It has been extensively documented that some species of bacteria contain dedicated transporters that favor the uptake of Ni(II) and Co(II). These transporters include the nikABCDE system found in E. coli, the NiCoT family found in eubacteria, archaea and fungi  and some ABC transporters [15, 16]. Using genetic techniques, it has been proven that such transporters, which differ in their specificity towards Co(II) and Ni(II) [15, 17, 18], can be expressed in various bacterial species [17, 19]. However, the metal accumulation properties of these bacteria are counterbalanced by the presence of efflux pumps, which expel these metals ions out of the cell. The rcnA system is the only known Ni(II) and Co(II) efflux pump in E. coli. The genes encoding these efflux pumps can be disabled, leaving the imported metals trapped inside the cytoplasm and unable to exit the cell membranes.
Based on these two principles, a Co-accumulating E. coli strain has been engineered ; however, this strain had a major disadvantage: bacteria could not be recovered easily from the decontaminated effluent. However, several bacteria have the ability to attach strongly to surfaces using various polymers, thereby forming biofilms. Among these polymers are E. coli curlis, adhesion factors that belong to the amyloid fiber family . Curlis mediate adhesion to a wide range of biological or inert surfaces . This study focused on whether the adherence of a metal-accumulating bacterium could be enhanced to form a functional biofilter.
For this purpose, we engineered the previously described Ni- and Co- accumulating bacteria  by adding a metal-inducible curli overproduction system . The adherence and the metal accumulation capacities of the engineered strain were assessed using various qualitative and quantitative methods. The increased ability of the engineered strain to stick to inert surfaces facilitates its immobilization on a solid support and its removal from the decontaminated effluents. Hence, this strain might be a promising candidate for use in an industrial-scale biofilter.
Conception and design of the engineered strain
Our rational design of the Ni/Co Buster strain was aimed at modifying three cell functionalities. First, a constitutive fluorescent version of the MG1655 strain (SCC1, referred to as S29 in this manuscript) was used as a basic chassis to facilitate the monitoring of bacterial dispersion and biomass formation. Then, Ni/Co(II) capture optimized at two levels: preventing metal efflux and increasing metal uptake, as described below. Wild-type E. coli contains a Co and Ni efflux system, called Rcn (Ni and Co Resistance); this system is present inside the MC4100 strain, preventing the accumulation of Co(II) and Ni(II) . As described in the Methods section, this system was disabled by transferring a rcnA::uidA-kan cassette to the fluorescent MG1655 strain S29 by P1 transduction. As expected, the resulting rcnA strain (S48) showed increased sensitivity to the toxic effects of Ni(II) and Co(II) compared to the parental strain. This result indicates that the P1 transduction procedure successfully inactivated the rcnA gene (data not shown). To further improve the performance of this Co- and Ni-accumulating strain, a genetic device was designed that allowing enhanced uptake of these metals. A synthetic metal uptake gene encoding the Ni(II) and Co(II) transporter (NiCoT) from Novosphingobium aromaticivorans, which is optimized for expression in E. coli, was placed under the control of the strong promoter Ptac, as described in the Methods section. This transporter was chosen due to its outstanding Co(II) accumulation and average Ni(II) accumulation capacities compared to other transporters of the NiCoT family .
The pIG50 plasmid confers enhanced adherence of the MG1655 rcnA mutant to polystyrene
Bacterial strains and plasmids used in this study
SCC1 = S29
MG1655 (PA1/04/03 gfpmut3*Cm)
MG1655 (PA1/04/03 gfpmut3*Cm) rcnA::uidA-kan,
S61 “NiCo buster”
1137 = S71
MG1655 malT::Tn 10 ompR234 csgA::uidA-kan
pUC19-derived pMB1 (copy number: 100–300) CmR
pUC19-derived pMB1 (copy number: 100–300) TetR
rcn-csgBAEFG inserted at sites Eco RI/Pst I of pUC57
Ptac-nicoTB in pSB1C3
Ptac-nicoTB-rcn-csgBAEFG in pSB1T3
Taken together, these results show that the engineered strain S61 constitutively forms biofilms and that the thickness of these biofilms is moderately but significantly enhanced in the presence of Ni(II) or Co(II). This outcome is consistent with previous experiments showing that the rcn promoter is leaky . The Prcn promoter was preferred over the curli promoter to reduce the complexity of the genetic regulation of curli-mediated adherence. The curli endogenous promoter is not only regulated by Ni(II) but is one of the most complex promoters in E. coli[26, 30] and is affected by a wide range of physiochemical signals, including temperature and osmolarity, and numerous regulators are known to modulate its expression [31, 32]. Prcn is more stable with respect to environmental modification [23, 29] and increases the ability of cells to bind to their support in the presence of these metals. Both of these properties are expected to make the engineered strain more attractive for industrial application.
Cell immobilization is important for bioremediation for three reasons: it increases resistance to pollutants, confines the bacteria, and facilitates removal from the water phase, thereby facilitating the recovery of pollutant metals (reviewed in ). Immobilization can be achieved by adsorption, or by entrapment in a polymer network such as an alginate (methods reviewed in ). Intrinsic entrapment in a biofilm matrix, as designed and realized in this work, is a promising solution that limits the costs associated with immobilization.
Efficiency of the engineered metal uptake transporter
The specific uptake of Ni(II) or Co(II) was catalyzed by the Ni/Co uptake transporter from Novopshingobium aromaticivorans. This transporter is a single permease that belongs to the class II family of NiCoT transporters  and has been previously been shown to import both Ni(II) and Co(II), although Co(II) is imported with higher efficiency [2, 10]. In the engineered strain, the amino acid sequence of the NiCoT transporter was optimized for expression in E. coli (see methods).
The physiological effects of metal uptake by the engineered strain were then investigated. Considering that an intracellular accumulation of metal would increase the sensitivity of the strain to metal , we assessed the sensitivity of the engineered strain towards Ni(II) and Co(II). In the absence of metal, the growth of the engineered strain was comparable to that of the S29 parental strain or the S48 rcnA chassis (Figure 3B). In contrast, distinct phenotypes are observed for the three strains in the presence of 20 μM Ni(II) (a subinhibitory concentration). Whereas the growth of the parental strain was not affected and the growth of the rcnA strain was slightly affected by nickel, a dramatic loss of viability of the engineered strain occurred in the presence of the metal, indicating metal poisoning. Similar results were obtained in the presence of Co(II) at a lower concentration (1 μM). These results are consistent with previous studies that have shown that Co(II) is toxic at lower concentrations than Ni(II) [20, 29]. This increase in Co(II) and Ni(II) sensitivity further demonstrates the functionality of the NiCoT transporter.
Capture of nickel and cobalt by the engineered “NiCo buster” strain
To evaluate the fraction of metal ions that bound nonspecifically to extracellular structures and the contribution of the NiCoT transporter, experiments like those presented in Figure 4A were performed. In this set of experiments, a single metal concentration was used (10 μM), and the contact time between the bacteria and the metal was 30 min to enable equilibrium to be reached. The experiment was repeated using three independent biological replicates. Half of the bacteria were subjected to ICP measurements without any previous treatment, and the remaining half was washed with EDTA before being titrated (see the Methods section). The treatment of intact bacteria with EDTA should remove most of the extracellularly bound metal. Comparing the EDTA-washed and unwashed fractions of the S61 strain showed that 80% of the captured Ni(II) or 90% of the captured Co(II) are bound by the extracellular matrix (Figure 4B). The comparison between the EDTA-washed WT strain (S29) and the EDTA-washed engineered strain (S61) should demonstrate the contribution of the NiCoT transporter and the absence of the RcnA efflux pump. In the experiment, the S61 strain accumulated 1.6-fold more Ni(II) than did the WT strain, and the S61 strain accumulated 1.9-fold more Co(II) than did the WT strain (Figure 4C). These results are consistent with those shown in Figure 4A and clearly show the importance of the NiCoT transporter to the capture of the metals.
In conclusion, the E. coli bacteria accumulated 4.8 to 6 mg/g dry weight in only 10 minutes when the cells were exposed to 50 μM Ni(II) or 50 μM Co(II), respectively, and accumulated 1.8 to 3 mg/g of bacterial dry weight when exposed to 20 μM Ni(II) or 20 μM Co(II), respectively. The performance obtained was better than that achieved using transgenic tobacco (Nicotiana tabacum) expressing a bacterial NiCoT; in that experiment, the tobacco accumulated 0.6 to 1.5 mg/g of plant dry weight in 30 days when the pre-cultivated, hydroponically grown plants were exposed to 20 μM Ni(II) or 20 μM Co(II), respectively . Metal hyperaccumulator plants, such as Thlaspi caerulescens, have been reported to accumulate 2.8 mg of Ni/g of whole plant dry weight in hydroponic culture when grown for 3 weeks in presence of 10 μM metal [21, 22] (representing slightly better performance, which was achieved at the cost of strongly increased decontamination times). Direct decontamination of wastewater containing low concentrations of non-radioactive Ni(II) and Co(II) might be achieved more rapidly and at lower cost using our engineered bacteria rather than plants that require weeks to grow. Highly contaminated effluents (e.g., from mining and electroplating industries) could first be treated using conventional chemical or physical methods or using new biopolymer biosorbents [7, 12]. Bacteria could then be used to polish the wastewater in an additional treatment step to attain very low heavy metal ions concentrations that would comply with increasingly restrictive laws that regulate the maximum acceptable concentrations of metal in water. Our results show that Ni(II) and Co (II) metals are mainly captured by non-specific binding mechanisms. The NiCo Buster design, however, allows to increase the metal internalization by a factor of 1.6 (Ni) to 1.9 (Co), compared to the parental strain. This is of special interest when treating complex effluents, which often contain large amounts of iron and traces of other divalent cations.
The engineered E. coli “Co/Ni Buster” strain appears therefore as a promising candidate for the depollution and retrieval of these metals in radioactive effluents due to the rapidity of its action, achieving comparable results to existing systems with at least a 2000-fold reduction of incubation time. In processes using our immobilized strain, the amount (volume) of material necessary to remove radioactive Ni(II) and Co(II) material should be less important, and the removal of these two metals could have a positive impact on the classification of these radioactive wastes. Furthermore, in the future, our genetic construct could be transferred to other organisms, such as Deinococcus radiodurans, a very radioresistant strain in which genes from E. coli can be successfully expressed . The NiCo Buster system would however require optimization before industrial usage. One limitation is the presence of antibiotic resistant genes in the engineered strain. This raises the possibility for horizontal transfer antibiotic resistance genes from the engineered strain to environmental bacteria. Genome editing would permit to integrate all the exogenous sequences in the chromosome and remove the superfluous sequences.
The two most important issues related to metallic waste processing are 1) reducing the environmental degradation resulting from disposal and 2) recycling the metals of economic interest, such as Co(II) and Ni(II). Due to the high cost of conventional physicochemical methods, microorganisms and plants have been already achieved wide application, for example, in sewage treatment. Successful uses of microbial bioremediation have been reviewed in [36, 37]. Our study shows that the development of synthetic biology may play a role in the improvement of bioremediation processes, especially regarding their time requirements. Another important issue is that bacteria can be immobilized on solid supports to allow easy removal of “metal-loaded” bacteria from the bioreactor. This issue was addressed here by enhancing the natural adhesiveness of E. coli in response to the presence of the metal to be refined. If not total, adherence was significantly improved in our synthetic construct, thus paving the way for future developments. Concerning the metal-binding capacities of the strains, we showed here that most of the bound metal was present in the outer envelope. Nevertheless, the presence of the NiCoT transporter enhanced metal internalization by a factor of 1.6 to 1.9. This is of special interest when treating complex contaminated effluents, which often contain large amounts of iron and traces of other divalent cations. We showed here that the tested bacterial cells act as a non-specific metal sponge and that the transporter is able to selectively uptake trace metals.
In brief, genetically improved metal accumulation and adherence were successfully implemented, as demonstrated in this work. We suggest that the “Ni/Co Buster” strain could be used to create a new generation of biofilters that are designed for the remediation of Ni(II) and Co(II).
Bacterial strains and media
The E. coli K-12 MG1655 derivatives used in this study are described in Table 1. The bacteria were grown in either LB (Luria-Bertani ) or M63G (M63 , supplemented with glucose 0.2% and LB 1:100 v/v) media. When appropriate, Co(II) or Ni(II) were added to the media as CoCl2 or NiSO4, respectively. The antibiotics chloramphenicol (20 μg/mL), kanamycin (50 μg/mL) and tetracycline (10 μg/mL) were purchased from Sigma and used in the experiments. The media were inoculated at a final bacterial concentration of 107 cells/mL. Stock metal solutions were prepared in sterile water. Short incubations of biofilm with metal (less than 30 min) were carried out using metal solutions diluted in water.
Phage P1 transductions of strains SCC1 and MG1655 were carried out as described by Miller . Strains ARY023  and HYD720  were used as donors for rcnA::uidA-kan and ΔnikA-kan cassettes, respectively. rcnA::uidA-kan was transduced in strain SCC1 to generate strain S48. ΔnikA-kan was transduced in strain MG1655 to construct strain S59. Transformations were performed using the TSS transformation protocol described in . All synthesized genes were obtained from Genecust Europe, Luxembourg. Enzymes and buffers were supplied by Fermentas (Germany), and enzymatic reactions were performed according to the supplier’s instructions. All BioBrick assemblies were performed using the RFC10 standard. BioBrick assemblies used either the standard or the 3A assembly method . Briefly, standard assembly is performed by digesting the insert using XbaI and PstI, digesting the vector using SpeI and PstI, and then ligating both. 3A assembly is performed by digesting the upstream insert using EcoRI and SpeI, digesting the downstream insert using XbaI and PstI, digesting the vector using EcoRI and PstI, and ligating the products.
Construction of Ptac-nicoTB and construction of the engineered plasmid pIG50
Ptac and nicoTB were obtained by direct synthesis. Ptac uses the promoter sequence found in the plasmid pKK233-2 (Clontech). nicoTB comprises a strong RBS , the nicoT coding sequence found at locus Saro_0344 in the genome of Novopshingobium aromaticivorans DSM 12444 [GenBank:NC_007794] and the bidirectional terminator BBa_B0014 . nicoTB was codon-optimized for expression in E. coli using The Optimus  and the RCBSPC formula. Both genes were synthesized to contain the BioBrick prefix and suffix. nicoTB was then cloned downstream of Ptac by standard assembly, yielding the construct pIG49. Ptac-nicoTB (pIG49) was cloned upstream of rcn-csgBAEFG (pIG2, ) via a 3A assembly in pSB1T3, yielding pIG50.
Visualization of biofilms using fluorescence microscopy
In each well of a 96-well plate, overnight cultures of fluorescent S29 (WT) and S61 (engineered) strains were diluted to an OD600 of 0.03 in a solution containing M63G medium, the appropriate antibiotic and metal at the appropriate concentration. Non-adherent bacteria were discarded after 1 hour of incubation at 30°C. M63G (0.2 mL) supplemented with the appropriate antibiotic and metal was then added to each well. The plates were then incubated at 30°C for 5 hours, after which the adherent bacteria were directly observed in the wells using a fluorescence inverted microscope (IX81, Olympus, Japan) operating at excitation and emission wavelengths of 488 nm and 507 nm, respectively. The cells were observed again in this way after a further 24-hour incubation.
Visualization and quantification of biofilm thickness using confocal microscopy
In parallel with the fluorescence microscopy observations, the biofilm architecture and thickness was evaluated using a confocal microscope (LSM 510 META, Zeiss, Germany) operating at excitation and emission wavelengths of 488 nm and 507 nm, respectively. Images were then analyzed using ImageJ (National Institutes of Health, USA) and Imaris x64 (Bitplane, UK) software.
Quantification of biofilms using spectrofluorimetry
S29 and S61 cells were grown at 30°C in 96-well plates in the presence of a range of Ni(II) or Co(II) concentrations (0, 0.05, 0.1, 0.3, 0.5, 1, 2 and 5 μM). The fluorescence intensity was measured using a Plate CHAMELEON™V fluorimeter (Hidex, Finland). Measurements were performed after 5- and 24-hour incubations in the presence or absence of the culture supernatant. Data were analyzed using MikroWin 2000 data reduction software (Mikrotek, Germany). Fluorescent intensities were converted to the number of cells/mm2 using standard calibration data established based on a viable S29 cell count.
Metal sensitivity assay
Cultures in early stationary phase were diluted to concentrations of 108, 107, 106, 105,104 and 103 cells/mL. Five microliters of each culture were then spotted on plates containing M63G supplemented with metal ions at various concentrations (1, 10, and 20 μM) and incubated at 37°C for 48 h.
Nickel uptake assay
The nickel uptake assay was adapted from . Bacteria were cultured in LB medium to an OD600 of 0.6. Cells were harvested and washed once in phosphate buffer (50 mM NaH2PO4-Na2HPO4, pH 7.2). Bacteria were resuspended (1:5 v/v) in phosphate buffer supplemented with 0.2% glucose and 10 mM MgCl2. Transport was initiated by the addition of 63NiCl2 (Amersham biosciences, UK) at a final concentration of 150 nM. Bacterial cells were collected by filtration on nitrocellulose filters (0.45 μm pore size, Millipore, Germany) for the times indicated in Figure 3. The filters were washed twice with the same phosphate buffer, supplemented with 10 mM EDTA. Radioactivity was counted by using a Tri-Carb 2100TR scintillation counter (Canberra Packard, Austria) and the results were converted to pmole of Ni/mg of bacterial dry weight using an external standard curve.
Metal titration using the ICP-MS technique
Overnight cultures were inoculated into 20 mL M63G medium supplemented with the appropriate antibiotic in Petri dishes. After 24 hours at 30°C, the supernatant was discarded, retaining the biofilm. To the biofilms, 10 mL of Ni(II) or Co(II) solutions (0, 5, 10, 12, 20 and 50 μM) were added. After a 10- (Figure 4A) or 30-minute contact period (Figure 4B and C), metallic supernatants were discarded and the biofilms were recovered. Each biofilm was scraped off into 1 mL of diluted M63 medium (1/4). The suspension was homogenized by vortexing for 20 s. To estimate the cell concentration in this biofilm fraction, 100 μL were removed for OD600 analysis. To the remaining biofilm suspension, 1.4 mL of 12 M nitric acid was added. Each sample was then incubated in a water bath at 80°C for 1 hour. Samples were stored at 4°C before analysis. For the ICP analysis, which was performed on a 7500cx mass spectrometer (Agilent, USA), the samples were diluted 100 times in a 0.5 M HNO3/2 μg/L rhodium solution. Rhodium was used as an internal standard.
We would like to thank the rest of the iGEM 2011 Lyon-INSA-ENS team for laying the foundations of this work: Mélanie Geffroy, Margaux Jaulin, Pierre-Yves Zundel, Julie Soula, Thomas Poinsot, Gaël Chambonnier, Philippe Thomas, Béryl Royer-Bertrand, Aurélie Haag, Goki Ly, Michaël Vonsy, Mathilde Dumond, Soufiane Boumahdi, Auriane Kroiss, Arnaud Rondelet, Laura Izard, Benoît Drogue and Laurent Balvay. Confocal microscopy was performed with the help of Claire Prigent-Combaret (Ecologie Microbienne UMR CNRS 5557) and with the help of Beatrice Burdin at the “Centre Technologiques des Microstructures”. We thank the UMR INRA/INSA “Biologie Fonctionnelle, Insectes et Interactions” for the kind use of their fluorescence microscope and Philippe Oger for organizing the ICP-MS use at the “Laboratoire de Géologie de Lyon”. This work was partly supported by the INSA Foundation, bioMérieux and Assystem.
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