Engineered nanomaterials are widely used in water and wastewater treatment processes, and minimizing their adverse effects on biological treatment processes in wastewater treatment plants has become the primary focus. In this study, activated carbon fiber (ACF)-loaded manganese oxide nanomaterials (MnOx@ACF) were synthesized. A small-scale sequencing batch reactor (SBR) was constructed to simulate the synergistic degradation of pollutants by nanomaterials and microorganisms and the effects of nanomaterials on the structure of the microbial community in a wastewater treatment plant. The MnOx@ACF exhibited efficient removal of pollutants (98.7% in 30 cycles) and chemical oxygen demand (COD 96.4% in 30 cycles) through the formation of Mn-microbial complexes and enhanced cycling between Mn(III) and Mn(II) over 30 operating cycles. Metagenome analysis results showed that the microbial population composition and functional abundance increased when the SBR was exposed to different dosages of MnOx@ACF for a long time, among which 0.2 g/L MnOx@ACF exhibited the highest stimulation and influence on the functional abundance of microorganisms, which showed optimum ecological effects.

  • MnOx@ACF can effectively remove TCH under various environmental factors.

  • MnOx@ACF maintains efficient COD and TCH removal over 30 cycles.

  • Mn(III)-microbial complexes play a role in the degradation process.

  • The presence of microorganisms accelerates the cycling of Mn(III) and Mn(II).

  • The presence of MnOx@ACF stimulates the growth of functional microflora in SBR.

Municipal wastewater treatment plants (WWTPs) are installed to remove pollutants from water, thus protecting the environment and human health. Biological treatment is the core component of WWTPs. With the continuous developments in nanotechnology, several engineered nanomaterials (ENMs) have been released into various environments, with their use being gradually increased in the WWTPs. More than 400,000 tons of ENMs are annually released into natural water bodies and WWTPs (Inshakova et al. 2020; Jin et al. 2024). The introduction of ENMs into WWTPs induces oxidative stress by generating reactive oxygen species, releasing toxic metal ions, and disrupting the cell membrane structure through physical interactions, thereby affecting the treatment efficiency and operational performance of the biological treatment (Wang & Chen 2016). ZnO nanoparticles have been shown to reduce the abundance of microorganisms, disrupt microbial diversity, and decrease the efficiency of biological treatment systems (Zhang et al. 2017; Cheng et al. 2019). Ag nanoparticles can inhibit the activity of nitrifying and denitrifying bacteria, which affects the nitrification and denitrification processes, respectively, in sequencing batch reactors (Chen et al. 2014). Hou et al. (2015) showed that the presence of copper oxide nanoparticles might affect the flocculation ability of activated sludge and its composition of extracellular polymeric substances. In addition, the introduction of carbon nanotubes in WWTPs can have a series of toxic effects on biological treatment processes, such as inhibiting nitrification, reducing organic matter removal, and disrupting sludge flocculation structure and granularity.

Manganese oxides have received widespread attention in environmental remediation because of their environmental friendliness, high natural abundance, low cost, and high activity. Mn(II) is essential for microbial metabolism, which facilitates sludge settlement and alters microbial activity in wastewater treatment. Jiang et al. (2020) found that the presence of Mn(II) prolonged the formation time of aerobic granular sludge and enhanced the secretion of extracellular polymers during the treatment of aniline wastewater. Li et al. (2018) successfully removed 93.95% of the ammonium from the water following the addition of Mn(II) to a sequencing batch reactor (SBR) with high nitrogen removal. He et al. (2019) found that Mn(II) can be oxidized by Mn-oxidizing bacteria or fungi to biogenic manganese oxides (bio-MnOx), and its combination with aerobic granules can be used to continuously oxidize and remove toxic pollutants from SBR.

In recent years, activated carbon fibers (ACFs) have been widely used as ideal support materials for nonhomogeneous catalysts because of their uniform microporous structure, large number of surface-active groups, excellent chemical stability, and inert structure. As ACFs can be processed into different textile structures (e.g., fibers, fabrics, and felts) (Huang et al. 2014; Sun et al. 2014; Wang et al. 2014; Zhou et al. 2015), they are easy to separate and recover from the reaction medium and thus have high practical applications in complex reaction system structures. Therefore, the use of ACFs as a carrier material loaded with manganese oxides can provide high activity and easy separation and recovery. Our group successfully prepared ACF-loaded manganese oxide nanomaterials (MnOx@ACF) and explored its catalytic ability in a previous study (Xiao et al. 2023). However, studies evaluating the environmental behavior and biotoxicity of MnOx@ACFs have been lacking, and exploring the stability, safety, and ecological benefits of MnOx@ACFs has become a priority.

In this study, tetracycline (TCH) was used as the target pollutant, and an SBR was used to simulate a biological treatment system for antibiotic wastewater to investigate the interference mechanism of MnOx@ACF composite catalysts in the biological treatment of antibiotic wastewater and the environmental response of activated sludge microbial flora. The DNA structures of all microorganisms in the samples were extracted from the simulated SBR reactor, and a macrogenomic library was constructed to study and analyze the genetic diversity and ecological information of microorganisms obtained from this environment using genomic research strategies to investigate the effects of the microbial community structure in the SBR reactor in the long-term presence of MnOx@ACF.

Preparation of activated sludge

The activated sludge used in the experiments was obtained from a WWTP in Jiangxia District, Wuhan City, China, and was domesticated under TCH conditions at a concentration of 1 mg/L for 2 weeks before use. The composition and preparation methods of the synthesized wastewater are provided in Text S1 and Table S1, respectively.

Establishment of SBR reactor

The SBR reactors consisted of glass cylinders with an outer meridian of 136 mm, an overall height of 199 mm, and an effective volume of 2.0 L. An aeration device was mounted at the bottom of the reactor, which was connected to an air pump through a silicone tube to increase the dissolved oxygen level in the wastewater in the SBR. Domesticated sludge was inoculated into five SBR reactors (pH = 6.8–7.5) at a concentration of 4,000 ± 20 mg/L mixed liquor suspended solids. One SBR was set up as a no-MnOx@ACF control and named S0. The remaining SBR reactors were spiked with 0.05, 0.1, 0.2, and 0.4 g/L of MnOx@ACF and named S1, S2, S3, and S4, respectively. The five SBR reactors were operated continuously at 30 ± 2 °C for 30 cycles. Each operating cycle lasted for 12 h, including 10 min of filling, 11.5 h of aeration, 10 min of settling, and 10 min of draining. The hydraulic retention time was set to 20 h, and the exchange volume ratio was set to 60%. The airflow rate for aeration was set to 1.5 L/min.

Analytical methods

The chemical oxygen demand (COD) and TCH concentrations in the influent and effluent were monitored during operation. The relevant analytical methods are presented in Text S2.

Preparation of MnOx@ACF

In this study, MnOx@ACF was prepared using a synthetic method previously reported by our group (Xiao et al. 2023). The preparation procedure is described in Text S3.

Characterizations of ACF and mnOx@ACF

The X-ray diffraction (XRD) patterns of ACFs and MnOx@ACF are shown in Figure 1(a), where the large peaks between 15° and 30° are associated with ACF diffraction peaks. The distinct manganese oxide diffraction peaks in MnOx@ACF are related to Mn3O4 (JCPDS No. 80-0382) and MnO2 (JCPDS No. 44-0141), respectively (Zhang et al. 2024). The diffraction peaks of the ACF virtually disappeared after doping with Mn oxides, indicating a successful composite of the materials.
Figure 1

(a) XRD patterns, SEM images, and EDS of (b) ACF and (c) MnOx@ACF, adsorption of TCH by (d) different materials, (e) FTIR spectra of MnOx@ACF, different equilibrium adsorption quantity (q: mg/g) by (f) dosages of MnOx@ACF, (g) pH. [TCH] = 20 mg/L, [catalyst] = 0.1 g/L, [pH] = 5.0.

Figure 1

(a) XRD patterns, SEM images, and EDS of (b) ACF and (c) MnOx@ACF, adsorption of TCH by (d) different materials, (e) FTIR spectra of MnOx@ACF, different equilibrium adsorption quantity (q: mg/g) by (f) dosages of MnOx@ACF, (g) pH. [TCH] = 20 mg/L, [catalyst] = 0.1 g/L, [pH] = 5.0.

Close modal

The scanning electron microscopy images and energy dispersive spectroscopy analysis of the ACF and MnOx@ACF are shown in Figure 1(b) and 1(c). The clean and unloaded ACF surfaces showed clear barred grooves, whereas in the MnOx@ACF-loaded with manganese oxides, the nanoparticles filled the ACF grooves. The change in the Mn content of the seeds also proved that the material was successfully prepared.

Adsorption performance in the mnOx@ACF/TCH system

Figure 1(d) shows the adsorption of TCH by different systems. ACF alone could hardly adsorb TCH, while Mn3O4 and MnO2 only adsorbed 15.5 and 18.0 mg/g of TCH, which was lower than 111.5 mg/g of MnOx@ACF. This indicates that the composites had better TCH adsorption capacity than the single materials, which may be attributed to the electrostatic interactions between the composites and TCH. Figure 1(e) demonstrates the variation spectra of Fourier transform infrared spectrometer (FTIR) before and after the reaction of MnOx@ACF. The small peak at 1,380 cm−1 is usually attributed to the stretching vibration of carboxylates, which may be formed by the carboxyl groups on ACF with Mn ions during pyrolysis (Volkov et al. 2021). The stretching vibration of the peaks at 400 cm−1−800 cm−1 is attributed to the Mn–O bond and the Mn–O–Mn bond, and it can be found that the peaks before and after removal of TCH from MnOx@ACF hardly changed, which indicates the good mechanical stability and physicochemical properties of MnOx@ACF. When the amount of MnOx@ACF was adjusted (Figure 1(f)), the adsorption capacity decreased with an increase in the amount. The maximum adsorption capacity (176 mg/g) and the lowest removal rate of TCH (Figure S1) were observed when 0.05 g/L was used (39.1%). When the dosage was increased to 0.4 g/L, the TCH removal rate was 93.5%, but the adsorption capacity decreased since the increase in the dosage increased TCH adsorption sites by the material but also increased the adsorption resistance, eventually leading to a significant decrease in the adsorption capacity (Zhou et al. 2023).

Adjusting the solution pH can change the form of the TCH molecules (Figure S2). During the gradual increase in pH, TCH was mainly transformed into cationic (TC+) and amphoteric (TC0) forms (Deng et al. 2024), and the adsorption capacity gradually decreased from 125 to 39 mg/g with a further increase in the solution pH (Figure 1(g)). Figure 2(a) demonstrates the zeta potential of MnOx@ACF, which decreases with increasing pH. The PZC of MnOx@ACF was calculated to be 3.91, indicating that there is mainly positive charge aggregation on the surface of MnOx@ACF under acidic conditions. The three pka of TCH were 3.3, 7.7, and 9.7, respectively, and the strong electrostatic repulsion resulted in a decrease in the adsorption of TCH with the further increase of pH, which resulted in the aggregation of negative charges on the surface of MnOx@ACF (Zheng et al. 2024). It has been shown that coexisting anions in an aqueous solution may affect the adsorption capacity of the material for TCH through hydrolytic ionization; therefore, the adsorption capacity of MnOx@ACF for TCH in the presence of different anions was also explored. As shown in Figure S3, Cl, , and had little effect on the adsorption of TCH, whereas both and inhibited the adsorption of TCH by MnOx@ACF. The slight inhibition of may be attributed to the increase in the OH concentration in the solution and the increase in the pH of the solution due to the solution ionization equilibrium induced by hydrolysis (Li et al. 2024b). However, the greater inhibition of was mainly attributed to its high affinity for the solid surface, which led to a decrease in the activity of MnOx@ACF by attaching to its surface (Li et al. 2024a).
Figure 2

(a) Zeta potential classes of MnOx@ACF, and (b) five sets of SBR reactors.

Figure 2

(a) Zeta potential classes of MnOx@ACF, and (b) five sets of SBR reactors.

Close modal

Removal of COD and TCH by MnOx@ACF in SBR reactors

As is widely known, COD can often be used as a measure of the pollutant content in water. Therefore, the COD removal rates in various SBRs were examined to further explore the effects of MnOx@ACF on TCH degradation (Figure 2(b)). As shown in Figure 3(a) and 3(b), the COD removal rate showed a trend similar to that of TCH over 30 cycles. During the first five cycles of operation, the COD removal rate of the five SBRs increased rapidly, possibly because the domesticated activated aerobic sludge in the SBRs had already produced partially resistant bacteria that were able to directly biodegrade TCH upon commissioning, resulting in a sustained decrease in its COD content in a short time. However, a stagnation in COD removal was observed in 5–8 cycles, followed by a sharp increase until stabilization in the 12th cycle. In addition, control S0 had the lowest COD removal rate compared to the other SBR reactors before stabilization. These results indicate that the degradation of organic matter in water by the activated aerobic sludge in the SBR decreased after 4–5 cycles of operation, which may be due to the gradual accumulation of intermediates produced by TCH during the biodegradation process. During this period, the removal of TCH in reactors S1–S4 could be attributed to the adsorption of MnOx@ACF, which is consistent with the fact that the removal of TCH in control S0 was inhibited before stabilization. In contrast, TCH removal was still achieved in the SBR reactor containing MnOx@ACF. After four cycles, the sludge in the SBR reactor adapted to the new water quality conditions, the microbial community changed, the removal of COD stabilized, and the final effluent COD ranged from 30.0 to 40.0 mg/L (Ahmadizadeh et al. 2020). From Table S2, it can be seen that the mixed liquor suspended solids in all S1–S4 samples slightly increased compared to that in the S0 samples, which indicates that the addition of MnOx@ACF enhanced the coagulation performance and microbial activity of the activated sludge (Zhang et al. 2015).
Figure 3

Concentration and removal efficiency of (a) COD and (b) TCH in 30 operation cycles, SEM images of MnOx@ACF (c) before and (d) after 30 cycles, (e) Mn 2p XPS spectra of MnOx@ACF before and after use.

Figure 3

Concentration and removal efficiency of (a) COD and (b) TCH in 30 operation cycles, SEM images of MnOx@ACF (c) before and (d) after 30 cycles, (e) Mn 2p XPS spectra of MnOx@ACF before and after use.

Close modal

Mechanism of COD and TCH degradation in SBR by microbial-mnOx@ACF

Scanning electron microscopy was used to observe the morphological changes in the MnOx@ACF in the SBR biological treatment system. As shown in Figure 3(c) and 3(d), the MnOx@ACF originally dispersed on the surface of the ACF agglomerated after the SBR experiments. The obvious concave strip grooves on the surface of the MnOx@ACF after the SBR experiments were almost invisible, and the original, relatively dispersed MnOx@ACF particles almost exponentially agglomerated on the surface of the ACF after the SBR experiments. Elemental mapping analysis using energy dispersive spectroscopy of the localized regions showed that the mass percentages of Mn atoms were 1.02 and 5.24%, respectively. After the SBR experiments, the MnOx@ACF generated more peaks in the X-ray diffraction patterns (Figure S4), produced by the residual mineral components in the sludge of the nanomaterials (Pan et al. 2022).

To explore the valence changes in MnOx@ACF-Mn species in the SBR reactor, Figure 3(e) shows the Mn 2p spectra for 0, 10, and 30 cycles. Mn(IV), Mn(III), and Mn(II) correspond to 643.0–644.6 eV, 641.8–642.0 eV, and 641.2 eV, respectively. During the first 10 cycles, the Mn(III) content decreased from 65.95 to 28.90%, while the Mn (IV) content and Mn (II) content increased from 24.92 and 10.03% to 50.97 and 20.13%, respectively, which suggests that the microorganisms gradually adapted to the incorporation of the MnOx@ACF, at this stage, and the microorganisms continuously consumed Mn(III). As the system tended to stabilize, Mn(II) was almost completely converted into Mn(III) in the 10th–30th cycles. Thus, the stable removal of COD and TCH may be attributed to the mutual transformation of the Mn(III)-microbial complex and the Mn(II)-microbial complex, which was ultimately enriched in the prismatic grooves of the ACF. Indeed, previous studies have demonstrated that nanomaterials may influence the microbial biochemical reaction process, and Mn is involved in the transfer of extracellular electrons from bacteria to Mn minerals (Deng et al. 2022; Liu et al. 2023), thus facilitating the cycling of Mn(II) and Mn(III).

The cyclic voltammetry (CV) curves of MnOx@ACF and bio-MnOx@ACF after biological treatment are illustrated in Figure 4(a). It can be found that MnOx@ACF has a larger integral area of the closed curve, which represents that MnOx@ACF has a better electron storage capacity. MnOx@ACF and bio-MnOx@ACF show a spike-like structure on the y-axis, in which materials before and after the biological treatment have good redox capacity. In contrast, the spike-like structure of bio-MnOx@ACF is slightly smaller than that of MnOx@ACF, which suggests that microorganisms altered the physicochemical properties of MnOx@ACF during the removal of TCH and COD, participated in the reaction, and played an important role. The electrochemical impedance spectroscopy (EIS) curve in Figure 4(b) can be used to explain the difficulty of electron transfer; the slope of bio-MnOx@ACF is larger than that of MnOx@ACF, which indicates that the exchange of electrons between bio-MnOx@ACF and solution is easier than that of MnOx@ACF, which also means that the addition of microorganisms can enhance the efficiency of electron transfer in the solution and thus the removal of pollutants more efficiently (Ren et al. 2020).
Figure 4

(a) CV curves and (b) EIS of MnOx@ACF and bio-MnOx@ACF.

Figure 4

(a) CV curves and (b) EIS of MnOx@ACF and bio-MnOx@ACF.

Close modal

Performance of mnOx@ACF and bio-mnOx@ACF in real water bodies

The performance of MnOx@ACF and bio-MnOx@ACF materials was practically evaluated for real water treatment. Figure 5(a), 5(d), and 5(g) show the 3D EEM fluorescence spectra of pristine tap water, Jin Lake, and Tangxun Lake samples. The fluorescence spectra can identify a large number of biologically intractable organic pollutants in the wastewater, while the fluorescence spectra can determine the dissolved organic matter (DOM) in the water, which is divided into five regions by fluorescence region integration. Region I represents tyrosine proteins, region II represents tryptophan proteins, region III represents fuller acids, region IV represents soluble microbial metabolites, and region V represents humic acids (Chen et al. 2003). It can be found that the DOM components in tap water, Jin Lake, and Tangxun Lake samples are not particularly different, while the contents are more different. After the treatment of MnOx@ACF, the high-intensity fluorescence of region V was significantly weakened, which indicated that MnOx@ACF could remove humic acid and other substances in the samples. Samples treated with bio-MnOx@ACF showed an increase in the fluorescence intensity of regions III and IV while the intensity of region V was significantly weakened, which may be due to the microorganisms participating in the pollutants' removal, performing metabolic processes, and releasing metabolites.
Figure 5

(a) EEMs of tap water, treated by (b) MnOx@ACF and (c) bio-MnOx@ACF; (d) EEMs of Jin Lake, treated by (e) MnOx@ACF and (f) bio-MnOx@ACF; (g) EEMs of Tangxun Lake, treated by (h) MnOx@ACF, and (i) bio-MnOx@ACF.

Figure 5

(a) EEMs of tap water, treated by (b) MnOx@ACF and (c) bio-MnOx@ACF; (d) EEMs of Jin Lake, treated by (e) MnOx@ACF and (f) bio-MnOx@ACF; (g) EEMs of Tangxun Lake, treated by (h) MnOx@ACF, and (i) bio-MnOx@ACF.

Close modal

Effects of MnOx@ACF on microbial community in SBR

To investigate the effect of the long-term presence of MnOx@ACF on the microbial community structure in SBR reactors, mixed sludge samples were collected from five SBR (S0, S1, S2, S3, and S4) after 30 cycles of operation and subjected to microbial macrogenomic analysis on the Illumina NovaSeq sequencing platform.

Table S3 shows the richness and diversity of microbial communities in sludge samples from each SBR. The Good's coverage of the samples from S0 to S4 was all at 95.0–99.9%, indicating that the sequencing results reflected the real state of microbial community composition well (Karim & Shriwastav 2023). The Chao 1 index reflects the species richness of microbial communities, and its value was significantly higher in the samples from S1 to S4 than in the control S0, implying that the addition of MnOx@ACF stimulated microbial activity in the SBR reactor and enhanced the richness of its community (Zhang et al. 2021). The Simpson and Shannon indices were used to characterize the diversity of the microbial community species, which did not change significantly in the S1–S3 samples compared with that in the S0 sample, but both showed a decreasing trend in the S4 sample. The results indicated that the diversity of microorganisms in the S1–S4 samples was not affected despite the increase in microbial abundance. Some of the dominant species were gradually enriched by long-term exposure to a high dose of MnOx@ACF (0.4 g/L), whereas others were gradually eliminated with the long-term operation of the SBR, and the diversity of the microbial community species was reduced (Zhang et al. 2019; Zhou et al. 2022). In addition, sparse and abundant rank curves can be used to further analyze the homogeneity and diversity of the microbial community based on the operational taxonomic units (OTU) distribution. As shown in Figure 6(a) and 6(b), it can be seen that the curves flattened with an increase in sequencing depth, and the sparse curve of the S0 sample was relatively lower than that of the other samples. This indicated that the sequencing depth was saturated, and the microbial diversity in the S0 sample was lower than that in the other samples. The rank-abundance curves confirmed this result.
Figure 6

(a) Sparse curves, (b) abundance rank curves, (c) changes of community compositions at phylum level by the effect of MnOx@ACF at different dosages.

Figure 6

(a) Sparse curves, (b) abundance rank curves, (c) changes of community compositions at phylum level by the effect of MnOx@ACF at different dosages.

Close modal

The microbial community composition in the SBR reactors was analyzed at the phylum level for different MnOx@ACF concentrations (Figure 6(c)). Proteobacteria (including most nitrifying and denitrifying bacteria) play a key role in biological denitrification (Zhu et al. 2022) and had the highest relative abundance among the five SBRs. This indicates that Proteobacteria dominated in each reactor and that the addition of MnOx@ACF may have favored their enrichment in the environment. However, Actinobacteria, also an important denitrifying microorganism in SBR, showed opposite changes to Proteobacteria. Actinobacteria in the S1–S4 reactors all showed a significant decrease in relative abundance compared to the S0 reactor (17.57%), with relative abundances of 9.27, 6.86, 21.35, and 7.98%, respectively. These results indicate that different types of microbial populations undergo different degrees of population abundance changes when exposed to MnOx@ACFs for long periods. Bacteroidota are commonly found in wastewater treatment systems. Most of the Bacteroidota exist in anaerobic or low-oxygen environments, decompose proteins and amino acids, and effectively remove organic pollutants and nutrients. Their relative abundances were 3.97, 6.01, 4.63, 3.44, and 4.96% in S0–S4 reactors, respectively. In addition, the relative abundance of Chloroflexota, which is mainly a parthenogenetic anaerobic microorganism, did not change significantly in the S1–S4 reactors (1.8, 1.55, 1.64, 2.1, and 1.7%, respectively), suggesting that the presence of MnOx@ACFs provided a better growth environment for it.

To further investigate the effect of MnOx@ACF content on microorganisms at the genus level, a heat map of the top 50 genera in terms of relative abundance was plotted, as shown in Figure 7(a). When MnOx@ACF was added to the SBR system, the microorganisms at the genus level changed significantly; the relative abundance of microorganisms at the genus level was also affected differently by different contents of MnOx@ACF, and their dominant flora were also quite different. In the S0 reactor, Pseudomonas, Sphingorhabdus, Nitrospira, and Shinella were the dominant genera. Among them, the aerobic genera Pseudomonas and Sphingorhabdus play a role in removing organic matter and nitrogen during wastewater treatment (Zheng et al. 2020). In contrast, Shinella is a parthenogenetic anaerobic genus isolated from radionuclide- and nitrate-contaminated groundwater (Grouzdev et al. 2019) that can degrade complex macromolecules, such as lipids, carbohydrates, proteins, and fermentable substrates, into smaller organic matter (Ali et al. 2020). Nitrospira is a bacterial group that influences nitrogen removal efficiency. Among the dominant flora in the S1 reactor, Flavobacterium carries plasmids for aromatic compound degradation genes and enzymes that hydrolyze aromatic compounds, which have potential biotechnological applications in the bioremediation of recalcitrant pollutants (Khan et al. 2015). The S2 reactor had more dominant genera than the other reactors. Thauera, with a relative abundance of 1.67%, are typical denitrifying bacterium widely present in various types of biological wastewater treatment processes. It plays an important role in the removal of C, N, and P from wastewater and has a high pollutant degradation capacity, including aromatic compounds that are usually difficult to degrade (Sawayama et al. 2002). In sample S3, Micropruina, Nakamurella, Propionicimonas, Arachnia, and Ornithinibacter were the dominant species. Among them, Micropruina, Nakamurella, and Propionicimonas are a class of glycogen-accumulating organisms that can convert absorbed exogenous carbon sources into glycogen and store it intracellularly in the aerobic phase (Roy et al. 2021). There were relatively few dominant bacterial groups in S4. One such genus, Ideonella, is capable of anaerobic reactions using chlorate as an electron acceptor (Song et al. 2000). These results suggest that microbial change in activated sludge is a dynamic process that includes the enrichment and disappearance of microorganisms and that the change in microbial populations may be caused by the presence of MnOx@ACF and its content. In addition, the presence of one microbial population may promote the growth of other specific types of microorganisms, and this interaction between different bacterial populations may play an important role in the degradation of organic matter and the stability of the reactor (Wang et al. 2019).
Figure 7

(a) Heatmap analysis of the top 50 abundant genera in SBR with the addition of MnOx@ACF, and (b) relative abundance of different functional bacterial species in sludge samples.

Figure 7

(a) Heatmap analysis of the top 50 abundant genera in SBR with the addition of MnOx@ACF, and (b) relative abundance of different functional bacterial species in sludge samples.

Close modal

First-order metabolic pathway annotations based on the Kyoto Encyclopedia of Genes and Genomes (KEGG) database revealed a functional profile of communities in the S0–S4 reactors, mainly including metabolism, genetic information processing, human diseases, environmental information processing, cellular processes, and organic systems. As shown in Figure 7(b), metabolism was the main function in all samples, which occupies about 70.0% of the functional composition in all S0–S4 samples, followed by genetic information processing and cellular processes. However, the functional composition relationship and the degree of contribution of each type of function in the different samples did not change significantly. The results indicated that the addition of MnOx@ACF did not significantly affect the major functional composition of the microbial communities in the SBR.

Prediction of microbial potential function

In addition, this was used as the abundance unit to map the functional abundance in the S0–S4 samples based on the KEGG database of second-class metabolic pathways, and the results are displayed in Figure S5. The left vertical coordinate shows the classification of the second-rank functional metabolic pathways based on the KEGG database, and the corresponding first-rank functional pathways are shown on the right. Annotation analysis was performed by function in each sample to elucidate the changes in vital metabolic processes caused by the presence of MnOx@ACF. As shown in the figure, the relative abundance of the overall microflora with metabolic levels of functionality increased to varying degrees as the amount of MnOx@ACF dosed in the SBR reactor increased. Among them, amino acid metabolism, carbohydrate metabolism, xenobiotic biodegradation and metabolism, and the metabolism of terpenoids and polyketides all showed significant increases in relative abundance. It has been suggested that the biotoxicity of TCs-like substances may stimulate the microbial community to activate protective mechanisms for degrading TCs, thus enhancing the overall metabolism (Ohore et al. 2021). Broad-spectrum polyketides are associated with the metabolic functions of terpenoids and polyketides (Abegaz & Kinfe 2019). Among all the primary functional pathways with increased relative abundance, nucleotide metabolism, replication and repair, glycan biosynthesis and metabolism, folding, sorting, and degradation, and cell growth and death subchannels showed the lowest increase in functional gene abundance, reflecting the biotoxicity of TCH by affecting cell replication and growth in epiphytic biofilm microbial communities (Xu et al. 2018; Ohore et al. 2021). In addition, although the overall functional abundance in the SBR was increased by the presence of TCH, different dosages of MnOx@ACF further influenced the increase in functional abundance. The results showed that either too high or too low MnOx@ACF affected the microbial functional profiles differently, and the S3 sample (0.2 g/L MnOx@ACF) influenced the strongest disturbance and stimulation of microbial functional abundance compared with the other samples, which may be related to the interactions among MnOx@ACF, TCH, and microbial populations.

In this study, we explored the degradation of TCH by MnOx@ACFs in different environments based on previous studies by constructing a small-scale SBR to simulate the biological treatment system in a WWTP for the biodegradation of TCH, which was operated continuously for 30 cycles. The effluent TCH and COD concentrations reached a steady state after 10 cycles. The microorganisms and MnOx on the ACF gradually generated Mn(III)-microbial complexes in the first 10 cycles and were consumed and converted to Mn(II)-microbial complexes in 10–30 cycles. The continuous conversion of microorganisms, together with Mn(II) and Mn(III), was the main factor responsible for the high TCH and COD removal (Figure 8). Different dosages of MnOx@ACFs may affect the development of different microbial populations. The presence of MnOx@ACF further stimulated the growth of the functional microbial flora during TCH degradation, with 0.2 g/L MnOx@ACF at the strongest disruptive effect. Long-term exposure to MnOx@ACF in the SBR reactor altered the microbial population composition and functional abundance but did not significantly affect the stabilization of the SBR reactor and the biodegradation efficiency of TCH, showing a better ecological response. This lays a foundation and provides new insights into the applications of MnOx@ACF in the biological treatment system.
Figure 8

Possible removal mechanisms of TCH.

Figure 8

Possible removal mechanisms of TCH.

Close modal

This work was financially supported by the National Natural Science Foundation of China (Grant No. 51908432), the Natural Science Foundation of Hubei Province (2023AFB277), and the State Key Laboratory of Pollution Control and Resource Reuse Foundation (No. PCRRF22016). The authors would like to thank Technical Officer Zhengtao Gui of Shiyanjia Lab (www.shiyanjia.com) for the scanning electron microscopy and energy dispersive spectrometry elemental mapping analyses.

All relevant data are included in the paper or its Supplementary Information.

The authors declare there is no conflict.

Abegaz
B. M.
&
Kinfe
H. H.
(
2019
)
Secondary metabolites, their structural diversity, bioactivity, and ecological functions: An overview
,
Phys. Sci. Rev.
,
4
(
6
),
20180100
.
Ahmadizadeh
R.
,
Shokrollahzadeh
S.
,
Latifi
S. M.
,
Samimi
A.
&
Pendashteh
A.
(
2020
)
Application of halophilic microorganisms in osmotic membrane bioreactor (OMBR) for reduction of volume and organic load of produced water
,
J. Water Process. Eng.
,
37
,
101422
.
Ali
J.
,
Wang
L.
,
Waseem
H.
,
Song
B.
,
Djellabi
R.
&
Pan
G.
(
2020
)
Turning harmful algal biomass to electricity by microbial fuel cell: A sustainable approach for waste management
,
Environ. Pollut.
,
266
,
115373
.
Chen
W.
,
Westerhoff
P.
,
Leenheer
J. A.
&
Booksh
K.
(
2003
)
Fluorescence excitation–emission matrix regional integration to quantify spectra for dissolved organic matter
,
Environ. Sci. Technol.
,
37
(
24
),
5701
5710
.
Chen
J.
,
Tang
Y.-Q.
,
Li
Y.
,
Nie
Y.
,
Hou
L.
,
Li
X.-Q.
&
Wu
X.-L.
(
2014
)
Impacts of different nanoparticles on functional bacterial community in activated sludge
,
Chemosphere
,
104
,
141
148
.
Cheng
Y.-F.
,
Zhang
Z.-Z.
,
Li
G.-F.
,
Zhu
B.-Q.
,
Zhang
Q.
,
Liu
Y.-Y.
,
Zhu
W.-Q.
,
Fan
N.-S.
&
Jin
R.-C.
(
2019
)
Effects of ZnO nanoparticles on high-rate denitrifying granular sludge and the role of phosphate in toxicity attenuation
,
Environ. Pollut.
,
251
,
166
174
.
Deng
Y.
,
Xiao
L.
,
Zhou
H.
,
Cui
B.
,
Zhang
L.
,
Chen
D.
,
Gu
C.
,
Zhan
Z.
,
Wang
R.
,
Mei
S.
,
Pei
X.
,
Li
Q.
,
Ye
Y.
&
Pan
F.
(
2024
)
Phytic acid pre-modulated and Fe/N co-doped biochar derived from ramie fiber to active persulfate for efficient degradation of tetracycline via radical and non-radical pathways
,
Sep. Purif. Technol.
,
342
,
126976
.
Grouzdev
D. S.
,
Babich
T. L.
,
Sokolova
D. S.
,
Tourova
T. P.
,
Poltaraus
A. B.
&
Nazina
T. N.
(
2019
)
Draft genome sequence data and analysis of Shinella sp. strain JR1-6 isolated from nitrate- and radionuclide-contaminated groundwater in Russia
,
Data Brief
,
25
,
104319
.
Inshakova
E.
,
Inshakova
A.
&
Goncharov
A.
(
2020
)
Engineered nanomaterials for energy sector: Market trends, modern applications and future prospects
,
IOP Conf. Ser.: Mater. Sci. Eng.
,
971
(
3
),
032031
.
Liu
W.
,
Xu
S.
,
Ma
H.
,
Li
Y.
,
Mąkinia
J.
&
Zhai
J.
(
2023
)
Anaerobic consortia mediate Mn(IV)-dependent anaerobic oxidation of methane
,
Chem. Eng. J.
,
468
,
143478
.
Ohore
O. E.
,
Zhang
S.
,
Guo
S.
,
Manirakiza
B.
,
Addo
F. G.
&
Zhang
W.
(
2021
)
The fate of tetracycline in vegetated mesocosmic wetlands and its impact on the water quality and epiphytic microbes
,
J. Hazard. Mater.
,
417
,
126148
.
Ren
W.
,
Nie
G.
,
Zhou
P.
,
Zhang
H.
,
Duan
X.
&
Wang
S.
(
2020
)
The intrinsic nature of persulfate activation and N-doping in carbocatalysis
,
Environ. Sci. Technol.
,
54
(
10
),
6438
6447
.
Roy
S.
,
Guanglei
Q.
,
Zuniga-Montanez
R.
,
Williams
R. B.
&
Wuertz
S.
(
2021
)
Recent advances in understanding the ecophysiology of enhanced biological phosphorus removal
,
Curr. Opin. Biotechnol.
,
67
,
166
174
.
Sawayama
S.
,
Tsukahara
K.
&
Yagishita
T.
(
2002
)
Removal of 3-chlorobenzoate using granules in the upflow anaerobic sludge blanket method
,
J. Biosci. Bioeng.
,
93
(
5
),
502
504
.
Sun
L.
,
Yao
Y.
,
Wang
L.
,
Mao
Y.
,
Huang
Z.
,
Yao
D.
,
Lu
W.
&
Chen
W.
(
2014
)
Efficient removal of dyes using activated carbon fibers coupled with 8-hydroxyquinoline ferric as a reusable Fenton-like catalyst
,
Chem. Eng. J.
,
240
,
413
419
.
Wang
X.
,
Shen
J.
,
Kang
J.
,
Zhao
X.
&
Chen
Z.
(
2019
)
Mechanism of oxytetracycline removal by aerobic granular sludge in SBR
,
Water Res.
,
161
,
308
318
.
Xiao
L.
,
Deng
Y.
,
Zhou
H.
,
Lu
F.
,
Ke
C.
,
Ye
Y.
,
Pei
X.
,
Xia
D.
&
Pan
F.
(
2023
)
Activated carbon fiber mediates efficient activation of peroxymonosulfate systems: Modulation of manganese oxides and cycling of manganese species
,
Chin. Chem. Lett.
,
34
(
12
),
108407
.
Xu
R.
,
Yang
Z.-H.
,
Wang
Q.-P.
,
Bai
Y.
,
Liu
J.-B.
,
Zheng
Y.
,
Zhang
Y.-R.
,
Xiong
W.-P.
,
Ahmad
K.
&
Fan
C.-Z.
(
2018
)
Rapid startup of thermophilic anaerobic digester to remove tetracycline and sulfonamides resistance genes from sewage sludge
,
Sci. Total Environ.
,
612
,
788
798
.
Zhang
C.
,
Zhang
H.
&
Yang
F.
(
2015
)
Diameter control and stability maintenance of aerobic granular sludge in an A/O/A SBR
,
Sep. Purif. Technol.
,
149
,
362
369
.
Zheng
Y.
,
Yang
D.
,
Dzakpasu
M.
,
Yang
Q.
,
Liu
Y.
,
Zhang
H.
,
Zhang
L.
,
Wang
X. C.
&
Zhao
Y.
(
2020
)
Effects of plants competition on critical bacteria selection and pollutants dynamics in a long-term polyculture constructed wetland
,
Bioresour. Technol.
,
316
,
123927
.
Zhou
C.-S.
,
Wu
J.-W.
,
Ma
W.-L.
,
Liu
B.-F.
,
Xing
D.-F.
,
Yang
S.-S.
&
Cao
G.-L.
(
2022
)
Responses of nitrogen removal under microplastics versus nanoplastics stress in SBR: Toxicity, microbial community and functional genes
,
J. Hazard. Mater.
,
432
,
128715
.
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