Introduction

Many microorganisms possess a wide range of extraordinary physiological abilities for production of bioactive molecules that show resistance against and transform highly toxic compounds (Bhatnagar and Kim 2010). Of great interest are bacteria, which can convert deleterious forms of metalloids from one oxidation state to another through reduction and/or oxidation (Yurkov et al. 1996; Li et al. 2009; Arenas et al. 2014; Bonificio and Clarke 2014). In recent years, there has been more interest in these microbes due to increased environmental contamination from industrial and agricultural activities (Fujii et al. 1988; Macy et al. 1993; Prakash et al. 2001; Li et al. 2009; Yang et al. 2014). Te is a metalloid element related to oxygen and sulfur in group 16 of the periodic table. It possesses stable oxidation states of VI (tellurate), IV (tellurite), 0 (elemental tellurium), and II (telluride). Se parallels Te in many instances. It also belongs to group 16 and is related to sulfur and oxygen with similar oxidation states of VI (selenate), IV (selenite), 0 (elemental selenium), and II (selenide). Reduction of tellurite, selenite and/or selenate, under both aerobic and anaerobic conditions, results in detoxification (Yurkov and Beatty 1998; Soudi et al. 2009; Li et al. 2014a, b; Javed et al. 2016); hence, heavy metalloid oxyanion reducers have an important role in nature. The removal of toxic metalloid contaminants from environments with elevated concentrations can allow many biological species to inhabit these locales (Yurkov et al. 1999; Rathgeber et al. 2002; Csotonyi et al. 2006; Bajaj and Winter 2014; Epelde et al. 2015; Maltman et al. 2015). The details of microbial interactions with very high levels of tellurite, selenite, and/or selenate are still not well–understood; however, some unique physiological properties possessed by microbes may provide a means for bioremediation (Soudi et al. 2009; Maltman and Yurkov 2014, 2015; Maltman et al. 2017a, b).

The increased environmental concentration of toxins has led to the search for removal methods, which will not in turn cause more pollution or other related consequences. Some chemicals and resins have been used to neutralize and/or remove oxyanions (Kim et al. 2004; Elwakeel et al. 2009). However, they can be expensive and their use may result in increased release of xenobiotic compounds, which is often problematic. More attraction to biological approaches of dealing with metalloids has arisen, as it would lead to a ‘greener’, environmentally friendlier clean-up of pollutants (Gadd 2010). Microbes reducing oxyanions from highly toxic oxidation states to less toxic elemental forms have been in the spotlight as a possible means to remediate contaminated locations. Bioremediation has been explored for removal of xenobiotics, metals, and radioactive compounds (Pieper and Reineke 2000; Ruggiero et al. 2005; Shah and Nongkynrih 2007; Gadd 2010; Jadhav et al. 2010; Yong and Zhong 2010; Dogan et al. 2011; Wasi et al. 2013), but much less attention has been given to tellurite, selenite, and/or selenate treatments. The use of Thauera selenatis for removal of selenite/selenate from drainage water (Macy et al. 1993; Cantafio et al. 1996), and tellurite/tellurate clean-up from waste using Pseudomonas mendocina, strain MCM B-180 (Rajwade and Paknikar 2003) and Pseudoalteromonas sp., EPR3 (Bonificio and Clarke 2014) and Bacillus STG-83 for removal of tellurite and selenite/selenate in the presence of nitrate (Soudi et al. 2009) have been studied, along with using mixed complex microbial communities for remediation (Luek et al. 2014; Ramon-Ruiz et al. 2016). While all these approaches did result in removal of the majority of contaminants, initial concentrations of the oxyanions were low, required substantial time before significant remediation occurred, and involved many other factors which needed to be adjusted and controlled, making the process either complicated or expensive (Cantafio et al. 1996; Hunter and Kuykendall 2005; Staicu et al. 2017). Another major issue, especially related to selenite/selenate remediation, is recovery of the elemental end-product (Staicu et al. 2017). Hence, currently used strains and technologies leave much room for optimization. Bacteria possessing greater resistance, faster rates of reduction, and the ability to internalize the elemental Se and Te, may prove to be more efficient and effective, allowing for feasible detoxification and possible recovery/recycling.

In this study, we set out to ascertain the bioremediation potential of several bacterial strains with the ability to reduce high levels of tellurite, selenite, and selenate to elemental form (Fig. 1) (Maltman and Yurkov 2014, 2015; Maltman et al. 2016). The elemental Te [~ 100–500 nm particles, comprising up to 20–30% of cell volume (Yurkov et al. 1996; Kim et al. 2012)] and Se [~ 100 nm particles (Rathgeber et al. 2002; Li et al. 2014a)] produced is contained within the cells, providing a possible means for removal, preventing re-release into the environment, possibly resulting in further issues, and recovery/recycling of these elements. Removal processes under both aerobic and anaerobic conditions were investigated to define their prospective for future remediation applications.

Fig. 1
figure 1

a Aerobic reduction resulting in visible reduction of TeO32− by strain KR99 (similar appearance for E5, ER-V-8, and AV-Te-18) and SeO32− by strain ER-V-8 (similar for E5, KR99, and AV-Te-18). b Anaerobic reduction resulting in visible reduction of TeO32− by strain AV-Te-18 (similar results for ER-V-8), SeO32− by strain ER-V-8 (similar for AV-Te-18), and SeO42− by strain ER-V-8. For TeO32− supplemented cultures, black coloration indicates reduction to elemental Te. Dissolved Se oxyanion color change from clear to red is due to reduction to elemental Se

Materials and methods

Strains, growth conditions and oxyanion reduction

Strains selected for study included the aerobic anoxygenic phototrophs Erythromonas ursincola, KR99 (Yurkov et al. 1997) and Erythromicrobium ramosum, E5 (Yurkov et al. 1994), which possess membrane-associated reduction (Maltman and Yurkov 2015) and the heterotrophic facultative anaerobes Pseudoalteromonas relative, AV-Te-18, and Shewanella relative, ER-V-8 (Maltman et al. 2016). For aerobic remediation, E5 and KR99 were grown under their optimal conditions, as published (Maltman and Yurkov 2015), in the presence of either 500 µg/ml tellurite or selenite. ER-V-8 and AV-Te-18 were grown in rich organic (RO) liquid medium containing 2% NaCl (Maltman and Yurkov 2014) on an incubator shaker at 200 rpm in the presence of 250 µg/ml (AV-Te-18) or 150 µg/ml (ER-V-8) tellurite or 250 µg/ml selenite, at 28 °C, pH 7.8, in the dark. For anaerobic experiments, AV-Te-18 and ER-V-8 were initially grown aerobically at 28 °C in the dark on RO NaCl agar plates, re-suspended, and used to inoculate 120 ml crimp-sealed anaerobic bottles, containing 100 ml of AMR medium (Maltman et al. 2015) amended with 100 µg/ml of tellurite, selenite, or selenate, under a headspace of N2. Samples were taken at various time intervals with the amount of protein and oxyanion monitored. Tellurite, selenite, and selenate concentrations were determined as previously described (Desai and Paul 1977; Molina et al. 2010) and protein by the Bradford assay (Bradford 1976). All experiments were performed in triplicate.

Results and discussion

Tellurite removal

Pseudomonas mendocina, strain MCM B-180, is currently considered the most effective bacterium for aerobic tellurite (TeO32−) bioremediation; however, optimal reduction takes place at a concentration of only 10 µg/ml and it takes 72 h to remove 100 µg/ml (1.4 mg/l/h) (Rajwade and Paknikar 2003). All strains in our study were able to remove similar levels of tellurite very quickly, requiring 6 h or less (Fig. 2a). Over 48 h, KR99 and E5 removed 203 and 244 µg/ml tellurite (4.2 and 5.1 mg/l/h), respectively, which is a significantly higher level than reported for P. mendocina (Table 1), with the elemental end-product contained within the cell (Yurkov et al. 1996). For AV-Te-18 and ER-V-8, removal of 98 and 93 µg/ml, (2.1 and 2.0 mg/l/h) respectively (Table 1), did require somewhat more time (48 h) than measured for KR99 and E5, but even with this increase, they were still much faster than P. mendocina (Fig. 2a). Anaerobic resistance and reduction of tellurite has been investigated, but not in terms of remediation potential. However, some future applications may require the absence of oxygen due to the logistics of aeration. Therefore, if a bacterium can detoxify oxyanions under both aerobic and anaerobic conditions, it would be of great benefit and advantage. To this end, strains ER-V-8 and AV-Te-18 are both capable of tellurite reduction under anoxic conditions (Fig. 3a). Amounts of converted TeO32− were lower compared to the aerobic experiments, but this is expected since toxicity is generally increased in the absence of oxygen (Moore and Kaplan 1992; Borghese et al. 2004; Csotonyi et al. 2006), confirmed by decreased tellurite minimum inhibitory concentration (MIC) values for both ER-V-8 (150 vs. 250 µg/ml) and AV-Te-18 (150 vs. 500 µg/ml). Nevertheless, both strains could remove 10 µg/ml tellurite, the same concentration P. mendocina functions optimally at aerobically, with ER-V-8 taking 48 h (0.2 mg/l/h) and AV-Te-18 only requiring 24 h (0.4 mg/l/h) (Table 1). For strain AV-Te-18, the total removal can be as high as 51 µg/ml after 5 days (0.4 mg/l/h) (Fig. 3a). Under both anaerobic and aerobic conditions, Pseudoalteromonas relative, AV-Te-18 and Shewanella relative ER-V-8 cells converted colorless tellurite into elemental Te internally, supported by a change in cell color into black (Fig. 1). The growth media remained clear after centrifugation, confirming Te is not released from the cells. This is similar to published results observed for related microorganisms (Rathgeber et al. 2002; Kim et al. 2014).

Fig. 2
figure 2

Aerobic removal of a tellurite and b selenite by: dark gray triangle—AV-Te-18, black square—E5, light gray square—ER-V-8, and dark gray diamond—KR99

Table 1 Amount of tellurite, selenite, and selenate removed (mg/l/h) under aerobic and anaerobic conditions
Fig. 3
figure 3

Anaerobic removal of a tellurite, b selenite, and c selenate by: light gray diamond—AV-Te-18 and black square—ER-V-8

Specific removal rates varied depending on strain and conditions (Table 2). In the presence of oxygen, all four strains demonstrated different rates, with the most efficient detected for E5 (2.26 µg tellurite reduced/µg protein/day), followed by KR99 (1.45), AV-Te-18 (0.78), and ER-V-8 (0.65). Anaerobically, removal was constant at 0.81–0.82 µg tellurite reduced/µg protein/day, regardless of the strain (Table 2). Although AV-Te-18 removed approximately fivefold more tellurite than ER-V-8 over 5 days, the specific rate of reduction remained similar.

Table 2 Specific removal rates (µg oxyanion/µg protein/day) of tellurite, selenite, and selenate under aerobic and anaerobic conditions

Selenite and selenate conversion

Removal of Se oxyanions has been attempted using a variety of approaches (Cantafio et al. 1996; Hunter and Kuykendall 2005; Staicu et al. 2017). While successful, there is still much room for improvement, as in almost all cases, the time needed for removal is significant, the concentrations involved are relatively low (ng/µl) (Cantafio et al. 1996), and the reclamation of the elemental Se remains a major concern (Staicu et al. 2017). Therefore, microbes capable of removing higher amounts in less time, while internalizing the Se0 produced, may prove to be beneficial. As with tellurite, strains in this study could detoxify large quantities of selenite aerobically, with E5 removing 98 (2.0 mg/l/h), KR99 100 (2.1 mg/l/h), AV-Te-18 103 (2.2 mg/l/h), and ER-V-8 103 µg/ml (2.2 mg/l/h) (Table 1), accumulating elemental Se internally, which is revealed by a cellular color change from the original appearance to deep red (Fig. 1) (Yurkov and Beatty 1998; Rathgeber et al. 2002; Li et al. 2014b). The growth media color remained clear. Under anaerobic conditions, selenite removal was quite significant, 46 µg/ml (1.0 mg/l/h) for AV-Te-18 and 25 µg/ml (0.5 mg/l/h) for ER-V-8 after 48 h (Table 1; Fig. 3b). Strain ER-V-8 was also capable of anaerobic selenate removal, with 14 µg/ml (0.12 mg/l/h) reduced after 5 days (Table 1; Fig. 3c). As one can see, the amount of Se oxyanions removed is orders of magnitude greater than the amounts reported in previous studies and within a much shorter time frame (Macy et al. 1993; Cantafio et al. 1996; Hunter and Kuykendall 2005; Luek et al. 2014). Of note, all Se0 produced from reduction was contained inside the cells, potentially providing a means of removal (Rathgeber et al. 2002; Li et al. 2014a, b).

Unlike for tellurite, specific removal rates do not vary as much between strains in the presence of oxygen (0.62–0.77 µg selenite reduced/µg protein/day) (Table 2). This is not surprising as all bacteria had removed similar amounts and possessed similar removal profiles (Fig. 2b). However, under anaerobic conditions, removal rates differed greatly between AV-Te-18 and ER-V-8 (0.33 and 0.72 µg selenite reduced/µg protein/day, respectively) (Table 2). As ER-V-8 was the only strain capable of anaerobic selenate reduction, it is premature to make any comparative conclusions about its effectiveness of removal (0.59 µg selenate reduced/µg protein/day) (Table 2). Clearly these bacteria are much more effective and efficient at removal of Se oxyanions than any others currently proposed (Macy et al. 1993; Cantafio et al. 1996; Hunter and Kuykendall 2005; Luek et al. 2014; Staicu et al. 2017).

Conclusion

With ‘green’ technologies becoming main stream, the attractiveness of using bacteria is increasing for development of future applications. Since tellurite, selenite, and selenate contamination is becoming of great concern, bioremediation has been increasing in popularity, but the main areas in which improvement is required must be actively addressed (Cantafio et al. 1996; Hunter and Kuykendall 2005; Gadd 2010; Bonificio and Clarke 2014; Staicu et al. 2017). The strains investigated in this work appear to have potential to improve upon all aspects of removal and are excellent candidates for the development of bioremediation processes and are promising as a means of biorecovery of the elements (Hunter and Kuykendall 2005; Gadd 2010; Bonificio and Clarke 2014; Maltman et al. 2016). Further research will undoubtedly fine tune and deliver a practical and economically viable process of pollutant bioremediation and Te and Se bioreclamation.