Current intensities altered the performance and microbial community structure of a bio-electrochemical system
Graphical abstract
Introduction
Groundwater is one of the important sources of drinking water all over the world. However, the contamination of NO3−-N and phosphorus in groundwater has become an increasingly serious problem in recent years, resulting from discharge of industrial effluents, over fertilization in farms, animal and human wastes. High NO3−-N and phosphorus concentrations in drinking water could cause serious illnesses, such as blue baby syndrome, methemoglobinemia and gastric cancer (Zhao et al., 2012; Liu et al., 2019). Accordingly, the contamination of NO3−-N and phosphorus in groundwater has received great attentions all over the world. For example, the World Health Organization stipulates that the maximum allowable concentration of NO3−-N in drinking water is 10 mg L−1 (Liu et al., 2015). The Standards for Drinking Water Quality (GB5749-2006) proposed by China is 20 mg L−1 (Peng et al., 2018). Consequently, it’s necessary to develop effective technologies to remove NO3−-N and phosphorus from polluted groundwater.
NO3−-N removal technologies are classified into physical, chemical and biological approaches (Chen et al., 2017, 2019bib_Chen_et_al_2017; Qian et al., 2018bib_Chen_et_al_2019), among which biological denitrification is considered as low-cost and environmentally friendly. Heterotrophic denitrification is the most common biological nitrogen removal process, and has been widely used in municipal wastewater treatment plants (WWTPs) for nitrogen removal (Hao et al., 2013). However, the scarcity of carbon sources greatly circumscribed the performance of heterotrophic denitrification in WWTPs. To address this limitation, additional organic compounds like methanol and glucose are recurrently added as carbon sources (Zhai et al., 2018a). While this not only adds additional operating costs, but also increases the organic load of WWTPs. In contrary, autotrophic denitrifying microorganisms could utilize inorganic carbon source or some energy source like H2, Fe2+, sulfur or sulfur-reduced compounds as electron donor to achieve NO3−-N removal. Consequently, some researchers preferred to apply autotrophic denitrification instead of heterotrophic denitrification to treat low C/N wastewater.
The bio-electrochemical method is a relatively emerging technology for facilitating NO3−-N removal by autotrophic denitrification process (Qian et al., 2018). On the one hand, the production of H2 in the electrolysis process can be directly utilized by hydrogen autotrophic denitrifying microorganisms as electron donors to reduce NO3−-N (Sultana et al., 2015). On the other hand, the electrical stimulation in bio-electrochemical system may improve the activity of microorganisms, promote the transfer of electron, and enhance the metabolism of microorganisms, so as to improve the NO3−-N removal performance (Liu et al., 2015; Lin et al., 2019). Therefore, the bio-electrochemical system and their integrated processes have been widely studied and applied to removal NO3−-N from groundwater (Cecconet et al., 2018; Liu et al., 2019), drinking water (Zhao et al., 2012), and treated effluent (Hao et al., 2016). However, there are still some limitations in the conventional bio-electrochemical systems. For example, it is difficult for conventional bio-electrochemical systems to achieve efficient denitrification and phosphorus removal simultaneously (Hao et al., 2018). Electrocoagulation process has been recognized as a high-efficiency and rapid phosphorus removal with lower sludge production (Deng et al., 2017; Bakshi et al., 2020). Recently, the removal of NO3−-N and phosphorus simultaneously by bio-electrochemical system coupled with electrocoagulation process from wastewater has received increasing attention (Kłodowska et al., 2016; Deng et al., 2017; Ziouvelou et al., 2019). However, previous researches have focused on the construction of bio-electrochemical system and the optimization of operating parameters such as temperature, pH value and C/N ratio (Sultana et al., 2015; He et al., 2016; Jiang et al., 2018). Few studies reported the effect of wastewater nutrients removal efficiencies in bio-electrochemical system along with a current intensity gradient. Furthermore, the impacts of current intensity gradient on microbial communities in bio-electrochemical systems still remain unclear.
In this work, to achieve better simultaneous nitrogen and phosphorus removal performance, granular active carbon (GAC) and sponge iron (SI) were used as mixed fillers to construct a lab-scale BESAD-EC system. Our primary objectives of this research were to (i) investigate the performance of the integrated system for NO3−-N and phosphorus removal under different current intensities, (ii) reveal the response of microbial communities to a current intensity gradients, and (iii) analysis the possible mechanism of NO3−-N and phosphorus removal in the system.
Section snippets
Experimental apparatus
As shown in Fig. S1, the reactor of BESAD-EC was conical cylinder, made of cylindrical plexiglass (d = 20 cm, H = 50 cm). The system had a total effective volume of 8 L. Both the anode and cathode were made of graphite plates with diameter and height of 19 and 1 cm, respectively, and they were installed in parallel from top to bottom of system. A large number of microscopic holes were in two electrode plates for wastewater to pass through. A double layer polyacrylonitrile activated carbon fiber
Effects of current intensities on the performance of BESAD-EC system
As show in Fig. S2, the BESAD-EC system was started-up for 39 days with a gradually increase current intensity from 10, 30, 45–60 mA, and the effluent quality achieved a steady state. Fig. 1(A) reveals the impacts of current intensity on effluent NO3−-N concentration and removal efficiency in the BESAD-EC system. NO3−-N effluent concentration slightly decreased from 2.38 to 2.03 mg L−1 when the current intensity increased from 20 to 200 mA, and the corresponding removal efficiency improved from
Conclusions
In a bio-electrochemical system, NO3−-N and TP could be effectively removed with maximum NO3−-N and TP removal efficiencies of 94.2% and 75.8% at current intensities of 200 and 400 mA, respectively. Lower current intensities improved the removal efficiencies of NO3−-N (≤200 mA) and TP (≤400 mA), while higher current intensity (600 mA) decreased their removal performance. MiSeq sequencing analysis revealed that low electrical stimulation improved the diversity and richness of microbial
Credit author statement
Minghan Zhu: Conceptualization, Methodology, Visualization, Writing – original draft, Writing – review & editing, Investigation. Jingkai Fan: Software, Visualization, Writing – original draft. Minglu Zhang: Resources, Supervision. Zhenyang Li: Resources. Jingdan Yang: Investigation, Formal analysis. Xiaotong Liu: Methodology. Xiaohui Wang: Conceptualization, Validation, Supervision, Project administration, Funding acquisition, Writing – review & editing.
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.
Acknowledgments
This study was supported by Beijing Municipal Science and Technology Project (Z181100002418017) and the Open Research Fund Program of Key Laboratory of Cleaner Production and Integrated Resource Utilization of China National Light Industry (CP-2020-YB1).
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