Elsevier

Water Research

Volume 183, 15 September 2020, 116008
Water Research

Microbial selenate reduction in membrane biofilm reactors using ethane and propane as electron donors

https://doi.org/10.1016/j.watres.2020.116008Get rights and content

Highlights

  • Microbial Se(VI) reduction was achieved using C2H6 or C3H8 as electron donors.

  • Zero valent Se was the final product formed from Se(VI) bio-reduction.

  • PHAs generated in the biofilms contributed to Se(VI) bio-reduction.

  • Mycobacterium/Rhodococcus and potential Se(VI) reducers were enriched.

Abstract

Selenate (Se(VI)) contamination in groundwater is one of major concerns for human health, in particular in shale gas extraction sites. Microbial selenate reduction coupled to methane (CH4) oxidation has been demonstrated very recently. Little is known whether ethane (C2H6) and butane (C3H8) are able to drive selenate reduction, although they are also important components in shale gas. In this study, we demonstrated Se(VI) bio-reduction could be achieved using C2H6 and C3H8 as electron donors and carbon sources. Scanning electron microscopy coupled to energy dispersive X-ray spectroscopy (SEM-EDX) confirmed elemental Se (Se0) was the major final product formed from Se(VI) bio-reduction. Polyhydroxyalkanoates (PHAs) were generated in the biofilms as the internal electron-storage materials, which were consumed for sustaining Se(VI) bio-reduction in absence of C2H6 and C3H8. Microbial community analysis showed that two genera capable of oxidizing gaseous alkanes dominated in the biofilms, including Mycobacterium (in both C2H6 and C3H8-fed biofilms) and Rhodococcus (in C3H8-fed biofilm). In addition, several potential Se(VI) reducers (e.g., Variovorax) were detected in the biofilms. Investigation of Communities by Reconstruction of Unobserved States analysis supported that predictive genes associated with alkanes oxidation, denitrification and PHAs cycle were enriched in the biofilms. These findings offer insights into the process of selenate reduction driven by C2H6 and C3H8, which ultimately may help to develop a solution to use shale gas for groundwater remediation, especially near shale gas exploitation sites.

Introduction

Shale gas has attracted increasingly commercial interests and become economically recoverable over the last decades (Gregory et al., 2011). It is globally estimated that shale gas reserves are up to 7.3 × 103 trillion ft3 (U.S. EIA et al., 2013). The price of shale gas is decreasing continuously due to new horizontal drilling and efficient extraction technologies. Shale gas is composed of various saturated gaseous alkanes, including methane (CH4), ethane (C2H6), and propane (C3H8) (Ambrose et al., 2011; Jackson et al., 2013). While shale gas contains CH4 as the primary component, the amounts of C2H6 and C3H8 could reach up to 20% and 10%, respectively, in shale gas (Umukoro and Ismail, 2017). However, accompanied with the exploitation, shale gas is readily to migrate to surrounding water systems including drinking water (Jackson et al., 2013; Osborn et al., 2011), groundwater (Llewellyn et al., 2015), and surface water (Zeng et al., 2013). For example, 23 times higher C2H6 was detected in drinking water wells when Marcellus shale gas was exploited (Jackson et al., 2013). The leakage of shale gas has become a public concern because the contained gaseous alkanes were potent greenhouse gases and they may cause photochemical pollution (Etiope and Ciccioli, 2009).

On the other hand, the shales commonly contain selenium (Se) (up to 50 mg/kg) (Tourtelot, 1962). The enrichment of Se in the shales could be a big risk of Se contamination to the surrounding water systems (especially when shale gas is exploited), which has been reported in Cretaceous black shales in Montana and Barnett Shales in Texas, USA (Mayland et al., 1989; Fontenot et al., 2013), and Bowland Shales in the north of England (Parnell et al., 2016). The concentration of dissolved Se in water systems near drilled shales (e.g., Colorado shale in central Montana) could reach up to 1 mg/L (Mayland et al., 1989). However, dissolved Se in aquatic ecosystems is a critical concern because of its acute toxicity. Se can replace sulfur (S) in proteins, reshape the structure of the proteins and damage their normal function (Lemly, 1998), thus disturbing normal metabolisms of organisms. There has been a serious Se pollution incident in Kesterson Reservoir, California, where high level of Se led to the deaths, deformities, and birth defects of a large number of waterfowls and fishes (Presser, 1994). In addition, Se could also cause cancer, cardiovascular disease, diabetes, and nervous disorder to human bodies (Sun et al., 2014). The U.S. Environmental Protection Agency (EPA) has set the maximum contaminant level (MCL) of Se at 50 μg Se/L (USEPA., 2015). In particular, selenate (SeO42−, Se(VI)) in the shales, with high toxicity and water solubility, is usually formed by weathering (Tuttle et al., 2014; Zawislanski et al., 2003). Butler et al. (1994) found Se(VI) was the dominant Se species (>97%) in groundwater samples from weathered Mancos Shale. Transformation of Se(VI) to elemental selenium (Se0) is beneficial for lowering Se toxicity and contamination, since Se0 formes as precipitates in aqueous phase thus can be easily removed.

Se(VI) could be microbially reduced to Se0 by phylogenetically diverse microorganisms. Specific selenate-reducing bacteria, e.g., Thauera selenatis (Schroeder et al., 1997), Enterobacter cloacae SLD1a-1 (Watts et al., 2003), and Sulfurospirillum barnesii (Watts et al., 2005), are capable of reducing Se(VI) to Se(IV) using their periplasmic selenate reductases or membrane-bound selenate reductase. Some nitrate reducers, e.g., Paracoccus pantotrophus and Ralstonia eutropha, could also carry out Se(VI) reduction using their periplasmic (Nap) or membrane-bound (Nar) nitrate reductases (Sabaty et al., 2001). Se(IV) could be further reduced to Se0 by periplasmic nitrite reductase (Nir) (DeMoll-Decker & Macy, 1993) or hydrogenase I (Yanke et al., 1995).

Electron donors are required to drive microbial selenate reduction. To date, lactate (Lenz et al., 2009), acetate (Navarro et al., 2015), and hydrogen (Lai et al., 2014) have been used as electron donor to reduce Se(VI). Very recently, Lai et al. (2016) found Se(VI) could be reduced to Se0 using methane (CH4) as the sole electron donor and carbon source. They proposed methanotrophs could oxidized CH4, in which intermediates such as organic metabolites would be released and used by methanotrophs or other selenate-reducing bacteria for converting Se(VI) to Se0. In another study, Luo et al. (2018) reported Se(VI) reduction could be mediated by nitrite/nitrate-dependent anaerobic methane oxidation microorganisms (including Candidatus Methanoperedens and Candidatus Methylomirabilis) in a CH4 based membrane biofilm reactor (MBfR).

Although microbial selenate reduction coupled to methane oxidation has been reported (Lai et al., 2016; Luo et al., 2018), it is still unknown whether C2H6 and C3H8 are able to drive selenate reduction as electron donors. It has been well known that C2H6 and C3H8 can be aerobically oxidized in a similar metabolic pathway of CH4 oxidation, in which C2H6 and C3H8 can be oxidized into ethanol or propanol, followed by conversion to aldehydes and acids (Shennan, 2006). Considering the highly positive redox potential of Se(VI)/Se(IV) (+440 mV) and Se(IV)/Se0 (+210 mV) (Nancharaiah and Lens, 2015; Doran, 1982), and the negative redox potential of C2H6 (−270 mV) and C3H8 (−277 mV) (Rittmann and McCarty, 2001), C2H6 or C3H8 coupled to Se(VI) reduction is energetically feasible. Thus, it is proposed that proper application of these C2H6 and C3H8 might be beneficial to develop solutions to utilize shale gas to eliminate selenate contamination in aquatic systems near shale gas exploitation sites. In addition, the application of shale gas as electron donor could be a preferred alternative for bio-reduction of Se(VI), since shale gas is much cheaper (∼$0.08–1.00/m3) (Markets Insider., 2020) than pure CH4 (∼$1.34/m3) (Global Petrol Prices, 2020).

Thus, the objective of this study was to test the feasibility of Se(VI) bio-reduction using C2H6 and C3H8 in shale gas as the electron donors. For proving the concept, we set up two independent MBfRs, in which non-porous polypropylene fibers were used to deliver C2H6 or C3H8 directly to the biofilms attaching on the fiber walls. By utilizing MBfR systems, a high gaseous electron donor utilizing efficiency can be achieved (e.g., 96% of methane utilization efficiency in Cai et al., 2018), thus minimizing the off-gassing (Liu et al., 2019; Rittmann et al., 2014; Zhou et al., 2019). Both long-term operation and batch tests were conducted to study Se(VI) removal pattern with these two gaseous alkanes. The dominant microorganisms involved in C2H6 or C3H8 oxidation and selenate reduction were analyzed by using high-throughput 16S rRNA gene sequencing. In addition, key functional genes involved in C2H6/C3H8 oxidation and selenate bio-reduction were predicted by applying Phylogenetic Investigation of Communities by Reconstruction of Unobserved States (PICRUSt) pipeline.

Section snippets

Reactor setup and operation

Two laboratory-scale MBfRs, similar to that used by Lai et al. (2018a), were set up in this study (Fig. S1). Briefly, each reactor contained two glass tubes with total volume of 100 mL, in which 96 composite hollow fibers (model MHF-200TL, Mitsubishi, Ltd., Japan) were installed with a total membrane surface area of 141 cm2 C2H6 or C3H8 was separately delivered into each MBfR at the fixed gas pressure of 10 psi (165 kpa) controlled by gas-pressure regulators (Coregas, Australia). A peristaltic

Microbial Se(VI) reduction using C2H6 and C3H8 as electron donors

The performance of the two MBfRs supplied with C2H6 or C3H8 for reducing Se(VI) was monitored for 105-days’ operation (Fig. 1). The C2H6 based MBfR did not show any obvious Se(VI) reduction within the first 20 days. Se(VI) was partially converted to Se(IV) during Day 21–30. Se(VI) removal rate continuously increased up until Day 42, in which almost all of Se(VI) in influent was removed (>99%), along with the accumulation of Se(IV). Afterwards, the effluent Se(IV) concentration diminished until

Mechanisms for microbial Se(VI) reduction driven by C2H6 and C3H8

This study demonstrated that Se(VI) could be microbially converted into elemental selenium by using C2H6 or C3H8 as the sole electron donor. The complete Se(VI) removal during long-term operation (Fig. 1), together with the simultaneous C2H6/C3H8 consumption and Se(VI) reduction in Batch test C (Fig. 5), collectively suggest that these gaseous alkanes are driving factors for Se(VI) bio-reduction. SEM-EDX confirmed Se0 was the final product of Se(VI) reduction in the biofilms, indicating

Conclusions

In this study, we demonstrated Se(VI) bio-reduction using C2H6 or C3H8 as electron donors and carbon sources. The major reduction product was Se0 nanospheres. PHAs were synthesized in the biofilms in presence of C2H6 or C3H8, while they would be degraded for supporting Se(VI) reduction when these gaseous alkanes were absent. Mycobacterium seems to play a role in oxidizing C2H6, while Rhodococcus was likely involved in oxidizing C3H8. In addition, it seems that some Se(VI) reducers (e.g.,

Declaration of competing interest

The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.

Acknowledgements

This work is supported by Australian Research Council through Australian Laureate Fellowship (FL170100086) awarded to Prof Zhiguo Yuan. Associate Prof Jianhua Guo is a recipient of the Australian Research Council Future Fellowship via FT170100196. We thank Mr. Nathan Clayton and Ms. Jianguang Li for assistance with IC measurement.

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