Removal of pharmaceuticals in aerated biofilters with manganese feeding
Graphical abstract
Introduction
Various pharmaceutical active compounds (PhACs) have been detected in water bodies. Although at trace concentrations, they still have a potential impact on the aquatic ecological system (Brausch et al., 2012). This impact could become complex within the interactions of various species. For instance, the antibiotics would lead to an increased resistance of microorganisms who can spread their resistance genes into other microbes (Baquero et al., 2008). It was also reported that the dramatic population decline of vultures in the India subcontinent was resulted from the residue of diclofenac (DFC) in livestock bodies which held an important position in the food chain of vultures (Green et al., 2004). Main sources of PhACs are the human and veterinary applications. PhACs from the former source would mostly enter wastewater treatment plants (WWTPs) via a sewage system while those from the latter are normally diffused. Therefore, one important strategy to control the contamination of PhACs is to upgrade the current WWTPs which currently cannot effectively eliminate all PhACs (Zhang and Geißen, 2010).
Many technologies have been studied for the removal of PhACs, including AOP, ozonation, membrane separation, sorption, etc (Basile et al., 2011). Among them, ozonation and activated carbon adsorption are most promising and have been installed at full scale (Reungoat et al., 2010, Zimmermann et al., 2011). However, those chemical/physical methods mostly require high investment and/or operation costs. Therefore, the development of a cost-efficient method is of great concern.
Iron/manganese oxidizing bacteria (IMOB) can mediate the oxidation of Fe2+ and Mn2+ to their high-valency states and thus play an important role in the natural cycle of iron and manganese (Emerson et al., 2010). IMOB widely exist in natural water bodies and technical water systems. For example, Cerrato et al. (2010) detected several strains of IMOB in the sediment of surface water, on the filter materials of drinking water treatment, and in the water distribution pipes even with the presence of chlorine. IMOB have been widely involved in the removal of Fe2+ and Mn2+in the drinking water treatment (Gouzinis et al., 1998).
Recently, researchers found that IMOB are also capable of degrading PhACs. One degradation mechanism is the in vitro adsorption and oxidation by the biogenic manganese oxides (Bio-MnOx). Sabirova et al. (2008) studied the removal of 17α-ethinylestradiol (EE2) with several IMOB strains and they found that IMOB can effectively degrade EE2 with the presence of Mn2+. When a bacteriostatic agent (sodium azide) was applied to inhibit the manganese-oxidizing activity of IMOB, the authors still observed 80% removal of EE2. Thus they concluded that the degradation was initiated by the attack of biogenic manganese oxides (Bio-MnOx). This is in accordance with the fact that manganese oxides hold a high redox potential and both synthetic and biogenic MnOx are able to oxidize many organic and inorganic pollutants (Hennebel et al., 2009, Zaman et al., 2009, Zhang et al., 2008a). However, it was also found that the participation of active IMOB was beneficial and sometimes essential for pollutant oxidation. Murray and Tebo (2007) found that IMOB Bacillus sp. strain SG-1 can accelerate the oxidation of Cr3+ compared to both synthetic and biogenic MnOx. Forrez et al. (2010) reported that the addition of either sodium azide or lysozyme (a cell lysis agent) resulted in a significant inhibition of DFC oxidation by Bio-MnOx of IMOB Pseudomonas putida. Meerburg et al. (2012) further reported that the heat inactivated Bio-MnOx of P. putida cannot remove DFC. Our previous study also observed that several IMOB strains can remove DFC but the heat inactivated biomass resulted in no removal (Zhu et al., 2012). Therefore, other mechanisms may exit to initiate the pollutant removal which occurs with the active manganese-oxidizing metabolism of IMOB, e.g. via the involvement of a ligand-bound Mn3+ intermediate (Meerburg et al., 2012). Therefore, for real applications, the active involvement of IMOB should be guaranteed.
However, only few of studies have been published on the removal PhACs with IMOB in technical systems. De Rudder et al. (2004) used a MnO2 mineral as a packing material in a filter for the removal of EE2 from tap water. They noticed that the loaded EE2 on MnO2 was significantly beyond its adsorption capacity and thus they proposed that a self-regeneration process may occur. Forrez et al. (2009) compared two filters packed with the same mineral and plastic polyethylene rings. The filter with plastic rings was additionally fed with Mn2+ and therefore the rings were expected to be covered with Bio-MnOx. Both filters can successfully remove EE2 but the biofilter with plastic rings failed to recover the effective removal after an increase of EE2 loading and also resulted in a higher Mn2+ level in effluent than the filter with MnO2 mineral. Recently, Forrez et al. (2011) added Bio-MnOx (160 mg Mn4+ L−1) into the membrane module of a bioreactor and achieved an effective removal of many PhACs. However, such a configuration is complex to operate and may have some negative impacts on the membrane performance, e.g. fouling, permeability, etc.
In the present study, aerated biofilters were studied, with natural MnOx ore and zeolite as packing materials. Mn2+ was additionally spiked into the feeding wastewater to promote the growth of IMOB. Therefore, a simple configuration and active IMOB were expected with the studied aerated biofilters and the removal of three widely detected PhACs, including DFC, carbamazepine (CBZ) and sulfamethoxazole (SMX), was investigated with both synthetic and real wastewater.
Section snippets
Materials
MnOx ore (Aqua-mandix®) and natural zeolite (Bigadia®) were supplied by Aqua-Techniek, Netherlands, and EgeZeolit, Turkey, respectively. Their chemical compositions and physical properties are shown in Table 1. Diclofenac sodium, carbamazepine, sulfamethoxazole (all with analytical grade), and manganese(II) sulfate monohydrate with ReagentPlus® grade were purchased from Sigma Aldrich, Germany.
Biofilter and operation
The MnOx ore and zeolite were used to pack two biofilters, named Mn-Biofilter and Zeo-Biofilter,
Removal of PhACs
Fig. 2a shows the removal efficiencies of SMX, CBZ, and DFC in Mn-Biofilter at different operation phases. About 95% of DFC was removed immediately after starting the biofilter. On the contrary, only 10% of SMX was removed in the starting period of 3 months. However, thereafter the removal of SMX rapidly increased to >90% in several days (defined as the start of operation Phase B) and kept stable. The removal of both SMX and DFC was dropped to 70% and 80% (median value), respectively, after
Discussion
Current WWTPs cannot effectively remove SMX and DFC (Larcher and Yargeau, 2011, Zhang et al., 2008b). Our results provide an alternative solution to remove both substances with a simple reactor and an ease operation. However, adaptation is required for both biofilters to effectively remove SMX: 1 month in Mn-Biofilter, 1.5 month in Zeo-Biofilter. It might be related to the development of some SMX-degrading IMOB since the removal of SMX should be a result of biological manganese oxidation as
Conclusions and outlook
The following conclusions can be made from this study:
- 1)
SMX and DFC can be effectively removed in the aerated biofilter packed with natural MnOx and zeolite. However, Zeo-Biofilter required a long adaption time (∼1 year) to remove DFC. Mn-Biofilter and Zeo-Biofilter can also effectively eliminate the aromatic contents of DFC and SMX, respectively.
- 2)
DFC was mainly removed by the oxidation of MnOx while SMX during the biological oxidation of manganese. The bioactivity was also beneficial for the
Acknowledgment
This study is part of the project TransRisk (grant No. 02WRS1276J) financed by the German BMBF within the program of RiskWa. We also appreciate the work of Dr. Wolfram Seitz, Zweckverband Landeswasserversorgung at Langenau and Ms. Elena Kaiser, Bundesanstalt für Gewässerkunde (BfG) at Koblenz, for the analysis of pharmaceuticals.
References (37)
- et al.
Antibiotics and antibiotic resistance in water environments
Curr. Opin. Biotechnol.
(2008) - et al.
Long term laboratory column experiments to simulate bank filtration: factors controlling removal of sulfamethoxazole
Water Res.
(2011) - et al.
Manganese-oxidizing and -reducing microorganisms isolated from biofilms in chlorinated drinking water systems
Water Res.
(2010) - et al.
Biogenic metals for the oxidative and reductive removal of pharmaceuticals, biocides and iodinated contrast media in a polishing membrane bioreactor
Water Res.
(2011) - et al.
Influence of manganese and ammonium oxidation on the removal of 17α-ethinylestradiol (EE2)
Water Res.
(2009) - et al.
Removal of Mn and simultaneous removal of NH3, Fe and Mn from potable water using a trickling filter
Water Res.
(1998) - et al.
Biogenic metals in advanced water treatment
Trends Biotechnol.
(2009) - et al.
Oxidative decarboxylation of diclofenac by manganese oxide bed filter
Water Res.
(2013) - et al.
Coupled biotic–abiotic Mn(II) oxidation pathway mediates the formation and structural evolution of biogenic Mn oxides
Geochim. Cosmochim. Acta
(2011) - et al.
Ozone and biofiltration as an alternative to reverse osmosis for removing PPCPs and micropollutants from treated wastewater
Water Res.
(2012)
Removal of micropollutants and reduction of biological activity in a full scale reclamation plant using ozonation and activated carbon filtration
Water Res.
Ozonation and biological activated carbon filtration of wastewater treatment plant effluents
Water Res.
Application of ozone based treatments of secondary effluents
Bioresour. Technol.
Characterization of the manganese oxide produced by Pseudomonas putida strain MnB1
Geochim. Cosmochim. Acta
Degradation characteristics of secondary effluent of domestic wastewater by combined process of ozonation and biofiltration
J. Hazard. Mater.
Heavy metal desorption kinetic as affected by of anions complexation onto manganese dioxide surfaces
Chemosphere
Prediction of carbamazepine in sewage treatment plant effluents and its implications for control strategies of pharmaceutical aquatic contamination
Chemosphere
Carbamazepine and diclofenac: removal in wastewater treatment plants and occurrence in water bodies
Chemosphere
Cited by (39)
Marine bacteria-mediated abiotic-biotic coupling degradation mechanism of ibuprofen
2022, Journal of Hazardous MaterialsRemoval and transformation of sulfamethoxazole in acclimated biofilters with various operation modes – Implications for full-scale application
2021, ChemosphereCitation Excerpt :The removal of SMX in that study was 88% and was achieved after an adaptation period. Zhang et al. (2015, 2017a, 2017b) observed that SMX was removed after at least one-month adaptation period and attributed the elimination of SMX to the activity of manganese-oxidizing bacteria, but they did not ruled out the contribution of other groups of microbiota. The knowledge gaps regarding the degradation of SMX in biofilters include the combined effect of aeration, constant presence of readily biodegradable organic carbon and the presence of reactive medium such as MnOx.
Biologically mediated abiotic degradation (BMAD) of bisphenol A by manganese-oxidizing bacteria
2021, Journal of Hazardous MaterialsA review on the role of plant in pharmaceuticals and personal care products (PPCPs) removal in constructed wetlands
2021, Science of the Total Environment