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Insight into aggregation capacity of anammox consortia during reactor start-up Yunpeng Zhao, Ying Feng, Jianqi Li, Yongzhao Guo, Liming Chen, and Sitong Liu Environ. Sci. Technol., Just Accepted Manuscript • DOI: 10.1021/acs.est.7b06553 • Publication Date (Web): 05 Mar 2018 Downloaded from http://pubs.acs.org on March 8, 2018
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Insight into aggregation capacity of anammox consortia
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during reactor start-up
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Yunpeng Zhao 1, 2, Ying Feng 1, 2, Jianqi Li 2, 3, Yongzhao Guo 2, 3, Liming Chen 1, 2,
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Sitong Liu 1, 2 *
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1
Department of Environmental Engineering, Peking University, Beijing 100871, China
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2
Key Laboratory of Water and Sediment Sciences, Ministry of Education of China, Beijing
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100871, China
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3
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518055, China
School of Environment and Energy, Peking University Shenzhen Graduate School, Shenzhen
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*Corresponding author: Sitong Liu
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Address: College of Environmental Science and Engineering, Peking University, Yiheyuan Road,
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No.5, Haidian District, Beijing 100871, China.
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E-mail:
[email protected] 14
Tel/Fax: 0086-10-62754290.
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Abstract
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Anammox aggregates have been extensively observed in high-efficiency
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nitrogen-removal reactors, yet the variation and inherent cause of its aggregation
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capacity related to reactor operation are still unknown. Here, we used microbial
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detection, metabolomics, extended DLVO theory and multivariate statistical analysis
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to address this issue. The aggregation capacity of anammox consortia varied
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periodically during reactor operation, which was determined by the hydrophobic force
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and the ratio of extracellular protein (PN) to extracellular polysaccharides (PS).
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Fundamentally, it related to the variation of polysaccharides degradation bacteria
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abundance and the discrepancy of consortia metabolism. Specifically, the
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distinguishable up-regulation of the amino acids Phe, Leu, Ala, Thr, Gly, Glu, and Val
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potentially contributed to the high biosynthesis of extracellular PN. Together with the
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reduced extracellular PS production that was regulated via the
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UDP-N-acetyl-D-glucosamine and UDP-N-acetyl-D-galactosamine pathways, the
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elevated extracellular PN/PS resulted in the obviously increased extracellular
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hydrophobicity and aggregation capacity. Additionally, the overtly enriched
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phosphatidylethanolamine biosynthesis pathway was also vital to increasing
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extracellular hydrophobicity to accelerate aggregation. Understanding aggregation
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capacity variation is useful for advancing anammox aggregation for its application in
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wastewater treatment.
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Introduction
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The anaerobic ammonium-oxidizing (anammox) process, which converts ammonium
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and nitrite to dinitrogen gas,1 has been applied as a promising technology to treat
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ammonium wastewater with its inherent advantages of high nitrogen removal, no
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requirement for oxygen, an additional carbon source and low sludge yield.2 The slow
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growth rate of functional bacteria with two weeks of doubling time3 makes the high
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sludge retention a primary requirement for anammox reactor operation. Researchers
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have applied lots of different strategies to improve sludge retention, such as adding
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functional carriers, using membrane filters in MBR4 and rapid granulation by
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signaling molecules, among others. Actually, no matter the consortia granulation or
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biofilm formation, the intrinsic aggregation capacity of anammox consortia is very
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important, which varies in different conditions. To investigate this issue, it is
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important not only to advance biofilm or aggregation formation but also to clarify the
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potential metabolism conversion in the bacteria along with the different phases of
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reactor operation.
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The extracellular polymeric substance (EPS) matrix plays a core role in
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determining the bacterial aggregation capacity. There were three different concepts
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existing in the EPS compositions determining the microbial aggregation: (i) The “PS”
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mechanism: the gel-forming alginate-like PS could form a cross-network that favors
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sludge aggregation or is a trigger for sludge granulation;5–7 (ii) The “PN” mechanism:
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the electronegativity and hydrophobicity of PN could promote and stabilize the
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aggregate structure;8,9 and (iii) The “PN/PS” mechanism: increasing the PN/PS ratio 3
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could induce an increase in sludge hydrophobicity and bioflocculation ability.10,11
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Previous reports have demonstrated that the EPS of anammox sludge has a strong
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tendency to form biofilm or adhere to inert surfaces,12,13 as it has a larger amount of
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hydrophobic proteins and more loose secondary structure compared to activated
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sludge, nitrifying sludge and denitrifying sludge.8,14 The EPS is closely related to the
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microbial survival ability and aggregation morphology. There are some factors that
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influence EPS production, such as growth phase, substrate type, and external
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conditions.15 In fact, the EPS levels and chemical composition vitally depend on the
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bacteria metabolism. Therefore, the metabolism profile of the bacteria significantly
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determines its aggregation capacity.
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EPS consists of different types of biopolymers, such as PN, PS, and phospholipids.
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They are all organic macromolecules that are biosynthesized by polymerization of the
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specific building blocks.5 For example, 20 amino acids, such as Ala, Arg, Asn, and
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others, are reported for bacterial protein synthesis.16 Bacterial polysaccharides are
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found to be converted from monosaccharides that could be biosynthesized from the
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Embden–Meyerhoff–Parnas gluconeogenesis (EMP) pathway or amino sugars as
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precursors.17 The major composition of extracellular phospholipids includes
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phosphatidylethanolamine (PtE) and phosphatidylcholine (PtC).16,17 Recently,
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researchers found many generation genes and pathways for bacterial EPS. For
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example, the biosynthesis of tetratricopeptide repeat (TPR) protein is coded by the
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asnB gene for activated sludge bacteria.18 Polysaccharide biosynthesis is encoded by
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the cps3E-F region in some types of lactic acid bacteria.19 Phosphoethanolamine (PE) 4
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and phosphocholine (PC) can be formed by a bifunctional
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cardiolipin/phosphoethanolamine synthase and glycerolphosphocholine (GPC)
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pathway, respectively.20 Although the hydrophobicity of anammox consortia EPS for
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its aggregation has been described previously, how bacterial metabolism regulates
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EPS production and further influences the bacterial aggregation capacity remain to be
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clarified.
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Therefore, this study focused on understanding the variation in bacterial
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aggregation capacity during anammox reactor operation and interpreting the inherent
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cause using recently developed metabolome biotechnology. Bacterial aggregation
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capacity, EPS components, and community composition combined with the extended
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DLVO theory for the bacteria samples harvested across 210 days of reactor operation
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were used to go insight into consortia aggregation capacity variation during anammox
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reactor start-up.
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Materials and methods
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Reactor start-up and operation. A membrane bioreactor (MBR) with a 5.0-L
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working volume was operated for 210 d. The polyvinylidene fluoride (PVDF)
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membrane was placed in the center of the reactor. Then, anammox consortia that had
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been stored at 4 °C for 60 days was inoculated with the initial VSS concentration of
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about 0.06 g /L.21 The influent ammonium and nitrite concentration was gradually
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increased from 20 mg–N/L that was favorable for inoculum adaption to 300 mg–N/L.
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The details of the medium composition are presented in Supporting Information (SI)
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Text S1.
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The reactor was operated in continuous mode at a constant flow rate (2.3 mL/min,
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HRT=36 h) and was maintained in an anaerobic condition during the reactor operation.
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According to the microbial community structure, the start-up period could be divided
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into two stages: phase I (days 1–90) and phase II (days 91–210). The reactor pH was
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kept in the range of 7.5 to 8.0, and the temperature was maintained at 37 ± 1 °C.
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The influent and effluent concentrations of ammonium, nitrite and nitrate were
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determined every two days using an APHA standard engineering method. 22
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Suspended granular samples were obtained from the reactor every 30 days in two
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phases (on day 30 60, 90, 120, 150, 180 and 210) and samples on day 165 and 195
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were also harvested to get more information about the variation of aggregation
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capacity in the late stage of the reactor operation. Inoculum and these samples were
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labeled in order as S1–S10, respectively. These samples were used to determine
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biomass concentration, aggregation capacity, diameter, EPS composition and structure,
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contact angle, zeta potential and bacterial community structure. Meanwhile, the
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representative samples were also applied to detect metabolites: (i) the samples
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obtained every 60 days [on day 60 (S3), 120 (S5) and 180 (S8), respectively]; (ii) the
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samples obtained on the final day of the reactor operation [on day 210 (S10)].
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Aggregation capacity and diameter size assay. Aggregation capacity was
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determined using attachment-crystal violet staining.23 The consortia samples with
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synthetic medium were added to a 12-well plate and then incubated on a shaker. After
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that, the microbial suspension that could not be immobilized onto the plate wall was
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removed. Anammox consortia that were immobilized onto the plate wall were stained
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with crystal violet before elution by ethanol. Finally, the aggregation capacity was
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expressed in terms of the absorbance of ethanol solution. Higher absorbance indicated
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higher aggregation capacity.23 Additionally, the turbidity assays were used to support
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the results. Detailed methods are presented in SI Texts S2 and S3. The diameter of
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samples was determined using the Nano ZS instrument (Malvern. Inc., USA), based
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on the assumption that the aggregates were spherical.24 Five parallel samples were
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determined for each test.
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EPS Extraction and Determination. EPS was extracted using the cation exchange
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resin (CER) method proposed by Hou et al.8 The extracellular polysaccharides and
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proteins were determined using the Anthrone method25 and the BCA assay26
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respectively, and was normalized by the biomass concentration. The biomass
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concentrations were determined in terms of volatile suspended solids (VSS)
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concentration22 using the vigorously mixed consortia by magnetic stirring and N2
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gas.27 The PN or PS percentage was defined as the ratio of PN or PS to the sum of PN
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and PS concentrations. The extraction EPS solution was also lyophilized for the FTIR
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and XPS analyses.8 Pearson correlation analysis and Kruskal–Wallis tests were carried
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out using SPSS v20.0.
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Extended DLVO theory. To determine the interaction energy between sludge cells
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influencing anammox aggregation, the extended DLVO analysis was performed.28-30
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The total interaction energy (WT) is the summation of the Van der Waal energies (WA), 7
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electric double layer (WR), and acid–base interaction (WAB), or WT = WA + WR +
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WAB. Calculation of the functional forces of WR, WA, and WAB was performed
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according to the surface thermodynamic calculation approach based on the contact
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angle and zeta potential of samples.29,30 The contact angle and zeta potential were
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measured as described previously.29,30 Detailed methodology and calculations can be
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found in SI Texts S4 and S5, respectively.
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Microbial community analysis. Microbial DNA from consortia samples was
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extracted using the FastDNA @ SPIN Kit for Soil (MP Biomedicals, USA), as per the
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manufacturer’s instructions. Next, the V4 regions of bacterial 16S rRNA gene were
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amplified with the primer pair 5158F/806R.31 Finally, the extracted and purified PCR
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products were sequenced using the Illumina MiSeq platform at Majorbio Co., Ltd.
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(Shanghai, China). Thereafter, raw sequences (NCBI SRA: SRP126708) were quality
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filtered using the following criteria: sequence length shorter than 200 bp, average
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sequence quality score less than 25, or sequences containing any primer mismatches,
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barcode mismatches, ambiguous bases, or homopolymer runs exceeding two bases
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were excluded from further sequence analysis.31 Furthermore, the biomarkers among
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different phases were identified using the filtered data with linear discriminant
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analysis (LDA) effect size (LEfSe) as describe.32 The Fluorescence in situ
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hybridization (FISH) was used to validate the abundance of anammox species. Details
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were presented in SI Text S6.
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Metabolomic Profiling and Quantitation Analysis. The sample was harvested
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after centrifugation at 4°C at 6000×g for 3 min and washing with 1× PBS buffer three 8
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times. The sample was resuspended in 1.5 mL of cold ultrapure water (stored at 4 °C),
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and the mixture was sonicated with a probe tip sonicator on ice (3–s intervals between
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3-s pulses; 30 min, 30% of maximum intensity; Scientz, JY–92–IIN, 650W).33 Then,
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6 mL of pre-chilled methanol/water (4:1, v/v) was subsequently added to the
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samples.34 The samples were incubated at -80 °C for 2 h to precipitate the cellular
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proteins. After centrifugation (20 min at 10,000× g at 4°C), the supernatants were
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collected and dried under a gentle steam of nitrogen gas at room temperature.
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Afterwards, the samples were stored in a -80 °C freezer and prepared for metabolites
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that including intracellular and extracellular compounds determination using
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high-performance liquid chromatography with tandem mass spectrometry
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(HPLC–MS/MS). Furthermore, untargeted metabolomic analysis is used for global
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metabolome analysis, while targeted analysis is more accurate for quantitation.35
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Detailed metabolomics analysis methods are presented in SI Text S7. All tests were
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repeated three times. Additionally, the detailed methods to determine the hydrolysates
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of extracellular proteins and polysaccharides were presented in SI Text S8.
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The metabolites that were identified in all four samples were used for statistical,
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principal components analysis (PCA), and pathway analyses. Two–tail paired t-tests
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were conducted in Excel. All the heatmaps and the PCA analysis in this study were
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completed in R using the ggbiplot packages respectively. Prior to analysis, the
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metabolic data were pretreated using the autoscaling method.36 Pathway analysis was
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finished using Metaboanalyst (www.metaboanalyst.ca).
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Results 9
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Bacterial aggregation capacity and diameter size variations response to
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operational phases. During reactor start-up, there were discrepant nitrogen
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conversion ratios and nitrogen removal rates (NRRs) between two phases (Figure 1
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and SI Figure S1). During phase I, both the nitrite to ammonium consumption ratio
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(△NO2-–N/△NH4+–N) and the nitrate to ammonium conversion ratio
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(△NO3-–N/△NH4+–N) varied considerably. And the reactor performance gradually
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increased corresponding to the highest NRR of 124.52 g–N/(m3 d) in the end. In phase
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II, the average △NO2-–N/△NH4+–N and △NO3-–N/△NH4+–N was 1.07±0.03 and
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0.22±0.04, respectively. The total NRR increased sharply from 131.46 to 356.73
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g–N/(m3 d) with the increased influent nitrogen concentrations from 120 mg/L to 300
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mg/L.
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To determine whether the aggregation behavior of anammox consortia varied with
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the reactor operation, a comparison of aggregation capacity was conducted.
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Interestingly, the aggregation capacity exhibited the periodic law of first increase, and
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subsequently decreased during the reactor start-up. For example, it decreased to the
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minimum in the beginning of phase II (S5) and then increased. It decreased again for
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S8 and increased until the end of phase II (S10). The diameters of anammox
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aggregates that were the intuitive reflection of aggregate capacity were shown in SI
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Figure S2. Importantly, its variation tendency was all agreed with the variations of
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aggregation capacity (r = 0.947, P = 0.000). Turbidity assay was also conducted to
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support these results (SI Figure S3) (details were presented in SI Text S9).
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Variation in EPS chemical structure and composition. To uncover the variation 10
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in the EPS composition of anammox consortia, the concentrations of PN and PS were
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determined. Changes in the concentration of PN, PS, and the ratio of PN/PS showed
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different trends as follows [Figure 2(b)]: (i) PN concentration was relatively lower for
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inoculum and the samples in the end of phase I (S4) and in the initial period of phase
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II (S5 and S6). The average concentration of PN in phase II was significantly higher
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than that in phase I (Kruskal–Wallis test, P < 0.03). (ii) Intriguingly, PS concentration
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exhibited the periodic variation law of first increase, and subsequently decreased
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during the reactor start-up. (iii) Integrating the change rules of these two indices, the
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ratio of PN/PS changed periodically in two phases. It was relatively lower for the
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inoculum (S1), at the end of phase I (S4), the initial period of phase II (S5) and S8.
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Furthermore, the correlation between the aggregation ability and the concentration
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of PN was significantly positive (r = 0.547, P < 0.003) [Figure 2(c)]. Importantly,
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though there was no significant relationship with the concentration of PS [Figure 2(d)],
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a relatively stronger and significantly more positive correlation was observed between
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the aggregation capacity and ratio of PN/PS (r = 0.670, P = 0.000) than that observed
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between the aggregation capacity and PN concentration [Figure 2(e)]. Consequently,
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the PN/PS ratio, and not the individual concentration of PN or PS, showed a stronger
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positive correlation with the aggregation capacity.
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To unravel the functional groups of the anammox consortia surface, the EPS was
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further analyzed by FTIR spectroscopy and XPS analysis. The FTIR results showed
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that the variation in the chemical structure of EPS was in line with the composition
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change (SI Figure S4). In addition, the absorption bands of lipids reached a maximum 11
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in the end of phase I (S4) and afterwards became invisible in phase II (S5-S10). Most
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importantly, the XPS analysis showed that the ratio of hydrophobic functional groups
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also changed periodically along with the variation of aggregation capacity during the
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reactor operation (SI Figure S5). Details are presented in SI Text S10.
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Various bacterial interaction energies. To determine the key interaction energy
238
influencing the anammox aggregation, the contact angles and zeta potential combined
239
with an extended DLVO theory analysis were performed. The results of the contact
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angles against the three types of liquids (water, ethanediol and propanetriol) and the
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zeta potential in 0.1 M NaCl solution are shown in SI Tables S1 and S2, respectively.
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Combining these experimental results, the interaction energies can be calculated using
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the formula presented in SI Text S5. Figure 3 shows the curves for total energy (WT)
244
as a function of separation distance among bacteria of different samples. Interestingly,
245
the energy barriers that would prevent the bacteria from aggregating also varied
246
periodically. This finding was in line with the aggregation capacity results [Figure
247
2(a)].
248
In fact, the contributions of WA, WR and WAB in extend DLVO were significantly
249
dependent and discrepant. Here, though the WA and WR curves were nearly similar for
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different consortia samples (SI Figure S6), the WAB curves that depended on the
251
hydrophobic interaction followed the periodical rule during the reactor start-up.
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Importantly, there were obvious energy barriers while the WAB values of consortia
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samples were higher, such as S1, S4 and S5. Thus, the WAB that on behalf on the
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hydrophobic force played a decisive role in determining the aggregation process, 12
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which agreed with the EPS content results. Therefore, it is important to elaborate on
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the biosynthesis and degradation of anammox EPS that led to the variation in bacterial
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hydrophobicity and aggregation ability.
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Bacterial community shift. To identify the microbiological community shift
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during the reactor operation, 16S rRNA gene sequencing and FISH combined with
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PCA analysis were conducted. Though the abundance of 47 community members
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(species with more than 1% relative abundance) changed markedly between phase I
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and phase II [Figures 4(a) and 4(b)] (details were presented in SI Text S11 and
263
Figures S7 and S8), the PCA analysis showed the colonization-specific clustering of
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phase I and phase II, respectively. Therefore, the bacterial community structures were
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relatively stable in phase I and phase II, respectively.
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Importantly, the variation in the Phycisphaerae classes and the Anaerolineaceae
267
families followed a periodic law [Figure 4(a)], which was the same as the variation in
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PS [Figure 2(b)]. To explore whether there was a correlation between these species
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and the PS in anammox consortia, a Pearson correlation analysis was carried out.
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Surprisingly, the relationship between the ratio of PS and the sum of the relative
271
abundance of these two species was significantly negative (P < 0.03) [Figure 4(c)].
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Metabolite profile related to anammox consortia EPS shift. To provide insight
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into the possible metabolic pathways of EPS, the metabolites of one sample in phase I
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(S3) and three samples in phase II (S5, S8 and S10) were examined. In all, the 383
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metabolites that were detected in all four samples belonged to the following Kyoto
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Encyclopedia of Genes and Genomes metabolic pathways: amino acids,
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carbohydrates, lipids, peptides, nucleotides, cofactors and vitamins.
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Figure 5(a) depicts the intensities of the detected metabolites in each sample. As
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whole, dramatic changes of amino acids, sugar and glycerophospholipid were
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observed in the metabolic activities of anammox consortia. PCA of the metabolic
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profiles brought insight into the colonization-specific clustering of the four samples
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[Figure 5(b)]. The detail differentiation among colonization states has been shown in
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Figures 5(c)-(e). From these figures, we could distinguish specific biosynthetic
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pathways for the predominant EPS components.
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Figure 5(c) shows the biosynthetic pathway of amino acids. These amino acid
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intensities of four samples were all significantly distinct, especially for phenylalanine
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(Phe), leucine (Leu), alanine (Ala), threonine (Thr), glycine (Gly), glutamate (Glu),
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valine (Val), and others. However, not every amino acid can be the predominant
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component of extracellular proteins. The relationships of 20 amino acids and PN were
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established using Pearson correlation analysis. The results showed that only seven
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amino acids exhibited strongly positive correlations (P < 0.003), including Phe, Leu,
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Ala, Thr, Gly, Glu and Val (SI Figure S9). Importantly, these seven amino acids were
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indeed involved in the hydrolysates of extracellular PN (SI Figure S10). Therefore,
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these seven amino acids might be the main synthetic monomers of extracellular
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proteins.
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Unlike the complex biosynthesis pathway of PN, the sugar metabolism of
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anammox consortia is relatively straightforward. PS was biosynthesized mainly via
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the uridine diphosphate-N-acetylglucosamine (UDP-GlcNAc) and uridine
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diphosphate-N-acetylgalactosamine (UDP-GalNAc) biosynthetic pathways, since
300
these metabolites and their biosynthetic precursors (Fru-6P and Glu-6P) were all
301
detected in the hydrolysates of extracellular polysaccharides (SI Figure S10).
302
Additionally, it also can be supposed by the varied regulation of sugar metabolites
303
intensities and PS concentrations in different samples (Details were presented in Text
304
S12). Furthermore, the catabolism of UDP-hexosamine was more active for S10 than
305
that for S8 and the lower concentration of PS might be degraded for S10 (details were
306
presented in Text S12).
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Except for PN and PS, phospholipids are the other important components of
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microorganism EPS and have an important role in determining the hydrophobicity.5
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Although there were many types of lipids detected, only phosphatidylcholine (PtC)
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and phosphatidylethanolamine (PtE) biosynthesis pathways were relatively intact. The
311
intensities of phosphocholine (PC) and phosphoethanolamine (PE), which are the
312
precursors of PtC and PtE, respectively, varied unceasingly with the reactor start-up.
313
Integrating the results of FTIR analysis, the PtE that was formed by the reaction of PE
314
decarboxylation was supposed to be the dominant content of extracellular
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phospholipids instead of PtC (details were presented in SI Text S13).
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Discussion
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Increased extracellular PN/PS improves anammox sludge aggregation capacity.
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To our best knowledge, this is the first to present the aggregation capacity of
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anammox consortia through the microbial and metabolome analysis during reactor
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start-up, as aggregation capacity is important for anammox sludge retention and
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accelerating anammox reactor start-up. The anammox process can be proved through
322
the bacterial community structure and nitrogen conversion ratios. Although both of
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△NO2-–N/△NH4+–N and△NO3-–N/△NH4+–N did not completely conform with the
324
theoretical value of anammox process, they both agreed well with the anammox
325
process during bioreactor start–up.37 This was because an almost pure free-cells
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suspension of highly active anammox was used to calculate the stoichiometry of
327
anammox process as described previously, but several other species of bacteria were
328
present in the anammox consortia community in the bioreactor.38 EPS, a complex
329
organic macromolecule mixture of polymers, is accountable for organism cohesion.5,15
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Since PN and PS were predominantly present in EPS and the summation of these two
331
components concentration was regarded as the EPS concentration, the PN and PS
332
concentrations of EPS could focally affect the surface characteristics of anammox
333
consortia.14
334
Here, we first presented that the ratio of extracellular PN/PS showed a stronger
335
positive correlation with aggregation capacity of anammox consortia, which indicated
336
that it played more potentially important role in affecting the aggregation capacity.
337
Though it has been reported that PN, PS and PN/PS ratio all could determine the
338
microorganism aggregation,5-11 here, the aggregation capacity had a more strongly
339
and significantly positive relationship with the PN/PS ratio. Furthermore, the 16
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aggregation capacity increased while the extracellular hydrophobic compositions and
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interaction increased. Therefore, we supposed that the anammox aggregation was
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determined by the hydrophobic components and force, which agreed with the results
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of previous studies.8,39 As the aggregate caused by hydrophobic force that is a
344
hydrogen band in the micro-scale28 had more tight structure that could prevent oxygen
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pervasion into the interior of aggregates1 than that caused by the alginate PS that
346
contains the diamond-shaped holes.6 The abundance of PN, as well as PS, affected the
347
hydrophobicity. Hence, the higher PN/PS ratio resulted from the metabolism of EPS
348
(detailed discussion in 4.2, 4.3 and 4.4), and not the individual PN or PS
349
concentration, contributed more to the anammox aggregates.
350
Active PN metabolism increases the bacterial aggregation capacity.
351
Considering that the bacterial community structure was relatively stable in different
352
phases and the aggregation capacity and EPS components varied constantly, the shift
353
in microbial community was not the only cause for the variations observed in the
354
aggregation capacity and EPS composition. Variations in the EPS composition also
355
corresponded with the metabolites. Additionally, all metabolites from the entire
356
biomass were extracted. Some identified metabolites from the inner of the aggregates
357
that contain the inert biomass may not contribute towards surface aggregation.
358
However, it has been reported that in microorganisms, the cell-free channel structures
359
were a strategy to transport metabolites from inner aggregation to the surface.40
360
Therefore, all identified metabolites from different layers of aggregates were assumed
361
to have the same contribution for surface aggregation. 17
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In this study, the concentration of PN changed greatly, and those of S1 (inoculum),
363
S4 (end of Phase I), S5and S6 (initial of phase II) consortia were relatively lower than
364
those of other samples. The low protein concentration of S1 may have been caused by
365
enzyme hydrolysis when stored at 4 °C.41 The lower content of the other samples may
366
be attributed to the operational stage. Previous studies have shown that the EPS
367
composition of the same sludge is dynamic in different operational phases.42
368
Interestingly, the PN concentration of anammox consortia was relative lower for S4,
369
S5 and S6. Since there was a marked increase in the biomass concentration from S4 to
370
S6, this period was considered as the propagation phase (SI Figure S11). There are
371
different theories about the variation in bacterial extracellular PN in this phase. It has
372
been found that the PN concentration increased for hydrogenotrophic methanogens,43
373
while it was decreased for Rhodopseudomonas acidophila.44 In this study, the
374
reduction in the PN composition of anammox consortia was caused by the amino
375
acids for PN biosynthesis being used for cell growth and reproduction. Here, we
376
proposed that the main amino acids to synthesize protein included Phe, Leu, Ala, Thr,
377
Gly, Glu, and Val based on the Pearson correlation analysis. In addition, the
378
abundance of Gly, Glu, and Thr, which were selected on the basis of the correlation
379
analysis, was relatively lower in the hydrolysates of extracellular proteins. This may
380
be because amino acids were used as carbon and energy sources by heterotrophic
381
bacteria.1 Firstly, the intensities of these seven amino acids were significantly lower
382
for S5 compared to the other three samples (S3, S8 and S10) and led to a decrease in
383
PN production at this stage. Secondly, the possible participant in other roles of these 18
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amino acids in metabolism including the biosynthesis of nucleotide sugar45-47 and
385
phospholipids48,49 could also cause a further decrease in excretion in propagation
386
phase (detailed discussion in 4.3, 4.4 and SI Text S14). Therefore, Phe, Leu, Ala, Thr,
387
Gly, Glu and Val were supposed to be the dominant residues of extracellular PN, and
388
their low concentrations for the synthesis of extracellular PN contributed to the low
389
aggregation capacity.
390
Furthermore, the average PN concentration of phase I was significantly lower than
391
that of phase II, especially than that of the end of phase II. These results might be
392
caused by the energy metabolism of anammox consortia to adapt to the environment
393
changes. Analysis of the purine metabolic pathway revealed that the intensities of
394
metabolites required for ATP synthesis, such as guanosine and AMP, were all higher
395
in S3 (phase I) than those in S8 and S10 (phase II) (SI Table S5), which indicated that
396
the energy metabolism during phase I was more active than that during phase II.
397
Importantly, it has been shown that the microorganism have a distinct upregulation of
398
energy metabolism to adapt to the new environment, and maintain steady-state
399
metabolism during the stationary phase.50 Hence, compared to phase II, the anammox
400
consortia need more energy in phase I. Additionally, it has been reported that EPS
401
synthesis costs energy, and decreased EPS secretion potentially conserves energy for
402
bacterial growth.51 Consequently, the energy that is produced might be preferentially
403
used for microbial growth, rather than for PN production in phase I, which may result
404
in lower PN concentration in phase I.
405
Polysaccharides degradation and inactive UDP-hexosamine biosynthesis 19
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406
metabolism increases the bacterial aggregation capacity. Though the carbohydrate
407
structure in EPS was relatively stable, their content changed greatly and influenced
408
the characteristics of EPS.52 The results of this study agree with this finding.
409
Interestingly, the variation in PS concentration followed a periodic law, and we
410
proposed that one of the crucial reasons was the shift of PS degradation bacteria. It
411
has been shown that the Phycisphaerae classes can grow on cellobiose and
412
monosaccharides.53 Additionally, the Anaerolineaceae families have the ability to
413
degrade polysaccharides.54,55 Here, the variation in the sum of the abundance of these
414
two species also followed a periodic law and lagged behind the variation in PS. Most
415
importantly, there was a significantly negative relationship between the sum
416
abundance of these two species and the PS ratio. Just as the sugar metabolism for S10
417
was more active compared to S8, the sum of the relative abundance of these two
418
species was also higher for S10 than that for S8, which caused the PS concentration of
419
S10 to be lower than that of S8 and aggregation capacity of S10 to be higher than that
420
of S8. Therefore, these kinds of species could potentially increase the aggregation
421
capacity of anammox consortia through degrading PS. It’s also the possible reason
422
that the polysaccharides concentration and aggregation capacity changed periodically.
423
Furthermore, the biosynthesis of PS can be divided into two classes based on the
424
synthesis pathway.5,56 The first class comprises the production of
425
monopolysaccharides that are biosynthesized by the polymerization reaction of
426
monosaccharides including glucose and fructose. However, most PS is
427
heteropolysaccharides with irregular repeating units that are synthesized from a 20
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428
variety of intracellular sugar nucleotides including glucose, GlcNAc and GalNAc,
429
among others.5,56 Here, we proposed that the PS of anammox consortia was mainly
430
biosynthesized through the UDP-GlcNAc and UDP-GalNAc synthesis pathways from
431
GlcNAc and GalNAc as precursors, which is the same as the lactic acid bacteria.56 At
432
the same time, the higher PS concentration of S5 was causd by the active metabolism
433
of sugar to biosynthesize cell tissues for anammox growth and reproduction (detailed
434
discussion in SI Text S15).5,57 Additionally, some types of amino acids might also be
435
translated into glucose and hexosamine via the EMP pathway for synthesis of
436
cell-building organisms for supplementation as described previously (detailed
437
discussion in SI Text S15).17,45,46,58 Taken together, the active biosynthesis of
438
UDP-GlcNAc and UDP-GalNAc was the fundamental cause of the high content of PS
439
and also led to the low aggregation capacity.
440
Active phosphatidylethanolamine (PtE) biosynthesis metabolism benefits the
441
bacterial aggregation capacity. It is known that hydrophobic phospholipids also
442
have effects on the bacterial aggregation ability.5 As the dominant compositions of
443
phospholipids, phosphatidylcholine (PtC) and phosphatidylethanolamine (PtE) can be
444
synthesized through three routes: CDP-choline and CDP-ethanolamine (Kennedy)
445
pathways and the CDP-diacylglycerol pathway. Therein, the Kennedy pathways
446
biosynthesized PtC and PtE from phosphocholine (PC) and phosphoethanolamine (PE)
447
as precursors, respectively, while the CDP-diacylglycerol pathway synthesized
448
phosphatidylserine from CDP-diacylglycerol as a precursor.59,60 Considering the
449
variation in phospholipids metabolites and extracellular phospholipids, we proposed 21
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450
that PtE might be the predominant component of extracellular phospholipids for
451
anammox consortia.
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452
Furthermore, the decreased intensities of phospholipids for consortia in phase II
453
were caused by the role and metabolism of PE and PC. Previous studies have shown
454
that PE and PC are the major components of phospholipids in most bacterial
455
membranes.20 It has been found that either PE or PC is the head-group of ladderane
456
lipids that play an important role in translocation of hydrazine in the anammoxosome
457
membrane to complete the anammox process.58,61 Hence, the metabolism of this type
458
of lipid should be active to transport the increasing hydrazine while the NRR
459
increased. Here, compared to PE, the metabolism and catabolism pathway of PC
460
became more active while the influent nitrogen concentration increased. Hence, we
461
supposed that PC instead of PE was the dominant head-group of the anammoxosome
462
membrane for anammox consortia and that the active metabolism of PC contributed to
463
the increased NRR for phase II, which was also one of the reasons for the lower PN
464
concentration.
465
Most importantly, the active metabolism of PtE could increase the aggregation
466
capacity of anammox consortia. Taking the case of S4 and S5, S4 consortia had a
467
lower PN concentration and a similar PN/PS ratio to S5. However, the aggregation
468
capacity of S4 was significantly higher than that of S5. This result was likely because
469
the active PtE metabolism in S4 contributed to the higher concentration of
470
hydrophobic lipids in EPS. Then, it contributed stronger hydrophobic interactions and
471
higher aggregation capacity for S4, which also agreed with results of the extended 22
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DLVO theory. Therefore, the metabolism of phospholipids was also critical to
473
bacterial aggregation capacity.
474
Significance of this study. The determination of the aggregation capacity of
475
anammox consortia during reactor start-up has an important role in achieving rapid
476
biofilm formation, reactor start-up and advancing the anammox technology
477
applications for wastewater treatment. This study, for the first time, showed that the
478
anammox aggregation capacity changed periodically and was strongly correlated to
479
the extracellular PN/PS ratio and hydrophobic functional groups that are related to the
480
periodical variation of microbial community structure and discrepant metabolism. As
481
there was a great difference in bacterial aggregation capacity among the different
482
operational phases, optimal bio-carriers with special surface characteristics such as
483
hydrophobicity and zeta potential could be designed for different phases.
484
Importantly, active metabolism of the seven amino acids and PtE biosynthesis and
485
the inactive metabolism of the two UDP-hexosamine biosynthetic pathways have the
486
potential to improve the aggregation capacity. Therefore, the accommodation capacity
487
of anammox biomass can be improved through stimulating some metabolism
488
pathways. This study is first to elucidate the variation in aggregation capacity and
489
EPS composition of anammox consortia across the operational phases of the reactor
490
based on the metabolism profile, and it provides a methodology reference for similar
491
studies.
492
23
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Acknowledgments
494
The authors are grateful to the Foundations (NSFC No.51478006 and
495
No.JSGG20160429162015597) for financial support.
496
Supporting Information
497
Tables showing contact angle and zeta potential assay results, main bacterial taxa of
498
anammox consortia, metabolites intensities of purine pathway and pyruvate and
499
abbreviations of partial metabolites. Details of two aggregation capacity assays,
500
contact angle and zeta potential analysis, extended DLVO theory, FISH method,
501
untargeted and targeted metabolomic method, hydrolysates of extracellular proteins
502
and polysaccharides measurement methods, FTIR and XPS results, microbial
503
community shifts, sugar and glycerophospholipid vary, and discussions of amino
504
acids and nucleotide sugars. Figures illustrating the nitrogen conversion ratio,
505
aggregation capacity, aggregate diameter, FTIR and XPS analysis, extended DLVO
506
theory, FISH analysis, correlation between the amino acids and extracellular PN,
507
hydrolysates of extracellular PN and PS and biomass concentration.
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accumulation. J. Bacteriol. 2012, 194 (3), 686–701.
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(51) Raszka, A.; Chorvatova, M.; Wanner, J. The role and significance of extracellular polymers
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in activated sludge. Part I: Literature review. Acta Hydroch. Hydrob. 2006, 34 (5), 411–424.
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(52) Rehm, B. H. A. Microbial production of biopolymers and polymer precursors: applications
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and perspectives; Caister Academic Press: New Zealand, 2009.
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(53) Wang, X.; Sharp, C. E.; Jones, G. M.; Grasby, S. E.; Brady, A. L.; Dunfield, F. Stable-isotope
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probing identifies uncultured planctomycetes as primary degraders of a complex
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heteropolysaccharide in soil. Appl. Environ. Microbol. 2015, 81 (14), 4607–4615.
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(54) Ahn, J. H.; Song, J.; Kim, B. Y.; Kim, M. S.; Joa, J. H.; Weon, H. Y. Characterization of the
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bacterial and archaeal communities in rice field soils subjected to long-term fertilization practices.
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(55) Terashima, M.; Yama, A.; Sato, M.; Yumoto, I.; KamagaTa, Y.; Kato, S. Culture-dependent
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and independent identification of polyphosphate-accumulating Dechloromonas spp.
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predominating in a full-scale oxidation ditch wastewater treatment plant. Microbes Environ 2016,
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(56) Boels, I. C.; van Kranenburg, R.; Hugenholtz, J.; Kleerebezem, M.; de Vos, W. M. Sugar
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catabolism and its impact on the biosynthesis and engeneering of exopolysaccahrides production
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in lactic acid bacteria. Int. Diary J. 2001, 11, 723–732.
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Messner, P.; Schäffer, C.; van Niftrik, L. The S-layer protein of the anammox bacterium Kuenenia
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Daims, H.; Bartol-Mavel, D.; Wincker, P. Barbe, V.; Fonknechten, N.; Vallenet, D.; Segurens, B.;
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Schenowitz-Truong, C.; Medigue, C.; Collingro, A.; Snel, B.; Dutilh, B. E.; Op den Camp, H. J.
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M.; van der Drift, C.; Cirpus, I.; van de Pas-Schoonen, K. T.; Harhangi, H. R.; van Niftrik, L.;
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Schmid, M.; Keltjens, J.; van de Vossenberg, J.; Kartal, B.; Meier, H.; Frishman, D.; Huynen, M.
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A.; Mewes, H. W.; Weissenbach, J.; Jetten, M. S. M.; Wagner, M.; Le Paslier, D. Deciphering the
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evolution and metabolism of an anammox bacterium from a community genome. Nature 2006,
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(59) Gibellini, F.; Smith, T. K. The Kennedy pathway-de novo synthesis of
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phosphatidylethanolamine and phosphatidylcholine. IUBMB Life 2010, 62 (6), 414–428.
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(60) P Pessi, G.; Kociubinski, G.; Mamoun, C. B. A pathway for phosphatidylcholine biosynthesis
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in Plasmodium falciparum involving phosphoethanolamine methylation. Proc. Natl. Acad. Sci. U.
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(61) Chaban, V. V.; Nielsen, M. B.; Kopec, W.; Khandelia, H. Insights into the role of cyclic
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Figure captions
689
Figure 1. Nitrogen concentration profile and removal rate during anammox reactor
690
start-up: (a) NH4+-N, NO2--N and NO3--N concentrations in the influent and effluent
691
in phase I (days 1-90) and phase II (days 91-210). (b) NH4+-N and NO2--N removal
692
efficiency, as well as nitrogen removal rate in two phases.
693
Figure 2. (a) The aggregation capacity for ten anammox consortia samples during the
694
reactor start-up. S1-S10 represent that the inoculum samples and the samples obtained
695
on day 30, 60, 90, 120, 150, 165, 180, 195, and 210, respectively. Red, green and blue
696
columns indicate the samples in inoculum, phase I and phase II, respectively. (b) The
697
extracellular proteins (red columns) and polysaccharides (grey columns) contents and
698
the ratio of protein to polysaccharides (blue columns) of anammox consortia in
699
inoculum, phase I and phase II. Error bars represent standard deviations of triplicate.
700
(c), (d) and (e) show the correlation relationships between the sludge aggregation
701
capacity and the concentration of extracellular PN, PS and PN/PS ratio, respectively.
702
The red open circles depict the value of these three indexes. The dark grey lines
703
indicate fitted linear models with confidence intervals of 0.95 (light grey lines), which
704
were established by the Pearson correlation analysis. P < 0.05 was considered
705
statistically significant in all statistical analysis.
706
Figure 3. Total energy of the interaction (WT) vs. separation distance curves of
707
anammox consortia samples of (a) inoculum (S1), (b) phase I (S2-S4), (c) phase II
708
(S5-S10) calculated by extended DLVO theory. The electric double layer (WR), the 34
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709
van der Waals energies (WA) and the acidbase interaction (WAB) vs. separation
710
distance curves were presented in SI Figure S4.
711
Figure 4. (a)Heatmap showing relative abundance of 47 kinds of predominant
712
bacterial community types (phyla with more than 1% relative abundance) detected in
713
samples from inoculum and two phases. The detailed taxonomy was presented in SI
714
Table S3. (b) Principal component analysis (PCA) plot of bacterial taxa of anammox
715
consortia among different phases. Red, green and blue colonization-specific clustering
716
indicates the samples of inoculum, phase I and phase II, respectively. (c) The
717
correlation relationship between the sum relative abundance of the Phycisphaerae
718
classes and the Anaerolineaceae families and the ratio of extracellular
719
polysaccharides in the sum of extracellular proteins and polysaccharides. Correlation
720
relationship was assessed by the Pearson analysis. The dark grey lines indicate fitted
721
linear models with confidence intervals of 0.95 (light grey lines). P < 0.05 was
722
considered statistically significant.
723
Figure 5. (a) The heatmap showing relative abundance of metabolites in four samples
724
(S3, S5, S8 and S10) determined by the untargeted and targeted metabolomic analysis.
725
S3, S5, S8 and S10 represented the samples obtained on day 60, 120, 180 and 210,
726
respectively. Each column represents one biological replicate and every sample was
727
conducted in triplicate. (b) PCA analysis plot of anammox consortia metabolites in
728
four samples. (c) (d) and (e) represent metabolic pathway of amino acids,
729
polysaccharides and glycerophospholipid. Red, green, blue and purple circle represent
730
the metabolite intensity of the samples obtained on day 60 (S3), 150 (S5), 180 (S8) 35
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731
and 210 (S10), respectively. The different circle’s diameter represents the different
732
metabolite intensity. And the metabolite intensity of S3 was used as a control with the
733
fixed diameter. The circle’s diameters of other three samples were same as that of S3
734
when the metabolites intensities changed no significance, and were bigger or smaller
735
than that of S3 when the metabolites intensities were significantly increased or
736
decreased, respectively (P < 0.05). The solid lines represent the intracellular
737
metabolic pathways, and the dotted lines represent the supposed extracellular
738
metabolic pathways.
739
36
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740 741
Figure 1. Nitrogen concentration profile and removal rate during anammox reactor
742
start-up: (a) NH4+-N, NO2--N and NO3--N concentrations in the influent and effluent
743
in phase I (days 1-90) and phase II (days 91-210). (b) NH4+-N and NO2--N removal
744
efficiency, as well as nitrogen removal rate in two phases.
37
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Page 38 of 43
745 746
Figure 2. (a) The aggregation capacity for ten anammox consortia samples during the
747
reactor start-up. S1-S10 represent that the inoculum samples and the samples obtained
748
on day 30, 60, 90, 120, 150, 165, 180, 195, and 210, respectively. Red, green and blue
749
columns indicate the samples in inoculum, phase I and phase II, respectively. (b) The
750
extracellular proteins (red columns) and polysaccharides (grey columns) contents and
751
the ratio of protein to polysaccharides (blue columns) of anammox consortia in
752
inoculum, phase I and phase II. Error bars represent standard deviations of triplicate.
753
(c), (d) and (e) show the correlation relationships between the sludge aggregation
754
capacity and the concentration of extracellular PN, PS and PN/PS ratio, respectively.
755
The red open circles depict the value of these three indexes. The dark grey lines
756
indicate fitted linear models with confidence intervals of 0.95 (light grey lines), which
757
were established by the Pearson correlation analysis. P < 0.05 was considered
758
statistically significant in all statistical analysis.
759 38
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760
761
Figure 3. Total energy of the interaction (WT) vs. separation distance curves of
762
anammox consortia samples of (a) inoculum (S1), (b) phase I (S2-S4), (c) phase II
763
(S5-S10) calculated by extended DLVO theory. The electric double layer (WR), the
764
van der Waals energies (WA) and the acidbase interaction (WAB) vs. separation
765
distance curves were presented in SI Figure S4.
766
39
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767 768
Figure 4. (a)Heatmap showing relative abundance of 47 kinds of predominant
769
bacterial community types (phyla with more than 1% relative abundance) detected in
770
samples from inoculum and two phases. The detailed taxonomy was presented in SI
771
Table S3. (b) Principal component analysis (PCA) plot of bacterial taxa of anammox
772
consortia among different phases. Red, green and blue colonization-specific clustering
773
indicates the samples of inoculum, phase I and phase II, respectively. (c) The
774
correlation relationship between the sum relative abundance of the Phycisphaerae
775
classes and the Anaerolineaceae families and the ratio of extracellular
776
polysaccharides in the sum of extracellular proteins and polysaccharides. Correlation
777
relationship was assessed by the Pearson analysis. The dark grey lines indicate fitted
778
linear models with confidence intervals of 0.95 (light grey lines). P < 0.05 was
779
considered statistically significant.
780 40
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781 782
Figure 5. (a) The heatmap showing relative abundance of metabolites in four samples
783
(S3, S5, S8 and S10) determined by the untargeted and targeted metabolomic analysis.
784
S3, S5, S8 and S10 represented the samples obtained on day 60, 120, 180 and 210,
785
respectively. Each column represents one biological replicate and every sample was
786
conducted in triplicate. (b) PCA analysis plot of anammox consortia metabolites in
787
four samples. (c) (d) and (e) represent metabolic pathway of amino acids,
788
polysaccharides and glycerophospholipid. Red, green, blue and purple circle represent
789
the metabolite intensity of the samples obtained on day 60 (S3), 150 (S5), 180 (S8) 41
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790
and 210 (S10), respectively. The different circle’s diameter represents the different
791
metabolite intensity. And the metabolite intensity of S3 was used as a control with the
792
fixed diameter. The circle’s diameters of other three samples were same as that of S3
793
when the metabolites intensities changed no significance, and were bigger or smaller
794
than that of S3 when the metabolites intensities were significantly increased or
795
decreased, respectively (P < 0.05). The solid lines represent the intracellular
796
metabolic pathways, and the dotted lines represent the supposed extracellular
797
metabolic pathways.
798
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799
TOC/Abstract graphic
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