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Applied and Environmental Microbiology, January 2004, p. 588-596, Vol. 70, No. 1
0099-2240/04/$08.00+0 DOI: 10.1128/AEM.70.1.588-596.2004
Copyright © 2004, American Society for Microbiology. All Rights Reserved.
Advanced Wastewater Management Centre, The University of Queensland, St. Lucia 4072, Queensland, Australia,1 Department of Environmental Science, Policy, and Management, University of California, Berkeley, California 94720-3110,2 Abteilung für Mikrobielle Ökologie, Institut für Ökologie und Naturschutz, Universität Wien, 1090 Vienna, Austria3
Received 28 May 2003/ Accepted 26 September 2003
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Denitrification is an anoxic biological process where nitrate and nitrite are reduced to N2 gas in the presence of an organic carbon source (electron donor) that is typically measured as chemical oxygen demand (COD) in wastewater treatment plants (28). The stringent standards imposed on wastewater treatment plant effluents pose a particular challenge to biological denitrification, especially for treatment plants with a low COD/N ratio in the influent, due to a shortage of suitable electron donors for the nitrate reduction (14, 17, 36). The addition of external carbon sources to the anoxic zone of treatment plants to facilitate denitrification has been one effective solution to this problem (14, 15, 17, 36).
The main external carbon sources used for denitrification include methanol, ethanol, and acetate, of which methanol is generally the most cost-effective (5, 15, 29, 31). However, a complete evaluation of denitrification systems and a comparison of the effects of different carbon sources and operational strategies on their overall performance are largely missing, and this impedes the optimal use of external carbon sources (38).
A major drawback of using methanol intermittently at full-scale wastewater treatment plants is the initial long lag period (at least several days to weeks) before an increase in denitrification rates (14, 29). This observation has been made for pre- and postdenitrification processes (14, 15, 32). During the lag period, the wastewater treatment plant suffers from poor denitrification capacity and overall moderate process performance. Although this is considered a major problem in the wastewater industry, little progress has been made so far to identify the likely microbiological reason(s) behind the observed lag period by pure-culture-independent methods.
Studies of pure-culture-dependent methods have demonstrated that, following an initial lag period, highly specialized denitrifying microbial populations develop in wastewater treatment systems in the presence of exogenously added methanol (22). However, since most microorganisms in nature typically cannot be cultured axenically (3), much doubt is placed on these findings, particularly since they have not been verified in situ. Therefore, culture-independent rRNA-based molecular methods, including stable-isotope probing (SIP) (33), were used to identify the dominant methanol-utilizing microorganisms in a laboratory scale activated sludge process fed with methanol and operated with only nitrate as the terminal electron acceptor. The methanol-utilizing denitrifiers were enriched from a full-scale activated sludge biomass.
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Mixing was achieved by an impeller stirring at 200 rpm. The pH in the reactor was maintained at 7.5 ± 0.3 with a CO2-N2 gas mixture. To achieve the desired pH and anoxic conditions, the flow rate of each gas was regulated manually. Periodically the DO level in the mixed liquor was measured, but no DO was detected.
Medium.
The basal medium comprised 90 mg of MgSO4 · 7H2O, 160 mg of MgCl2 · 6H2O, 42 mg of CaCl2 · 2H2O, 837 mg of NaNO3, 122 mg of Bacto Peptone (Difco Laboratories, Detroit, Mich.), 20 mg of Bacto Yeast Extract (Difco Laboratories), 50 mg of NH4Cl, 11 mg of KH2PO4, and 26 mg of Na2HPO4 · 12H2O liter-1 and 0.3 ml of a nutrient solution prepared as previously reported (6). The medium was made up with reverse-osmosis-deionized water and sterilized by autoclaving. Methanol was used as the carbon source and was separately fed to the SBR to give an initial in-reactor concentration of 263 mg of methanol liter-1. The methanol/NO3--N ratio in the medium was maintained at 1.9:1 based on the minimal denitrification stoichiometry (37).
Reactor analysis.
Cycle studies were carried out every 2 weeks during the operation of the reactor. Samples were collected every 2 min during the first 30 min and then every 15 min during the 4.7-h anoxic-reaction period of a cycle. The nitrogen removal performance of the SBR was assessed by comparing the supernatant nitrate and nitrite concentrations at the end of a cycle with those concentrations in the influent.
Chemical analysis.
Nitrate, nitrite, ammonia, and phosphate were analyzed on filtered (Whatman nitrocellulose membrane, 0.2-µm-pore-size) samples by a flow injection analysis instrument (Lachat, Zellweger Analytical, Milwaukee, Wis.). The mixed-liquor suspended solids and mixed-liquor volatile suspended solids (MLVSS) were determined according to previously published methods (4).
Microbiological analysis. (i) SIP.
After 6 months of consistent denitrification operation, the enriched denitrifying microbial community in the SBR was investigated by SIP (33) and by full-cycle rRNA analysis (3). A 50-ml mini-SBR was operated to mimic exactly the 1.8-liter parent SBR. However, in the mini-SBR, [13C]methanol (99% 13C) was substituted for the conventional [12C]methanol and the operation was extended over 24 h or four cycles, during which the mixed liquor in the mini-SBR was sampled four times in one cycle to determine denitrification performance.
(ii) DNA extraction and separation of biomarked DNA.
The DNA from the biomass in the mini-SBR (fed with [13C]methanol) and from the 1.8-liter parent SBR (fed with conventional [12C]methanol) was extracted with the Bio 101 FastDNA spin kit (QBiogene). For every milliliter of DNA solution, 1 g of CsCl dissolved in Tris-EDTA buffer (pH 7.6) was added, and 0.8 ml of ethidium bromide (10 mg ml-1 in H2O) was added per 10 ml of DNA-CsCl mixture, such that the final density of the entire mixture was 1.55 g ml-1 (34). The mixture was transferred to 5.1-ml Beckman quick-seal centrifuge tubes, and the DNA fractions were resolved by equilibrium centrifugation (200,000 x g, 24 h, 20°C). A single DNA band ([12C]DNA band) was observed from the biomass of the parent SBR, which had been exposed to conventional [12C]methanol. The DNA from the mini-SBR biomass produced two bands. One was at the same position as the single [12C]DNA band from the parent SBR, and an additional band approximately 1 cm lower was hypothesized to be as a result of 13C-biomarked DNA ([13C]DNA band). Both bands observed from the mini-SBR were collected with syringes and 20-gauge needles (34). Separate [12C]DNA and [13C]DNA fractions from the mini-SBR biomass were desalted of CsCl and purified from ethidium bromide with Microcon YM-10 centrifugal filter units (Millipore Corporation). The accumulated DNA on the filter device was rinsed two or three times with sterile reverse-osmosis-deionized water and collected to a clean tube.
(iii) PCR amplification, cloning, DNA sequencing, and data analysis.
The nearly complete 16S rRNA genes (nucleotides 28 to 1491, Escherichia coli numbering) of the [12C]DNA and [13C]DNA fractions from the mini-SBR biomass were amplified and cloned ([12C]DNA and [13C]DNA clone libraries) by methods previously described (8). In brief, primers 27f and 1492r (19) were used to amplify by PCR the nearly complete 16S rRNA genes, and the amplicons were immediately ligated with a TA cloning kit (Invitrogen, San Diego, Calif.). The ligated products were transformed with ultracompetent E. coli XL2-Blue MRF' cells (Stratagene, Sydney, Australia) and screened for positive inserts (clones that contain 16S rRNA gene inserts) with Luria-Bertani agar plates containing ampicillin, 5-bromo-4-chloro-3-indolyl-ß-D-galactopyranoside (X-Gal), and isopropyl-ß-D-thiogalactopyranoside (IPTG) (8). Inserts from individual clones were amplified and grouped into operational taxonomic units (OTUs) according to restriction fragment length polymorphism (RFLP) analysis (8). A substantial number of clones from each OTU were partially sequenced with the primer 530f (19) to determine the phylogenetic coverage of each group, and subsequently a representative number of clones were fully sequenced (8). Compilation of DNA sequences and their analysis by BLAST (1) and phylogenetic methods (evolutionary distance analysis and tests of robustness) to construct phylogenetic trees were conducted as previously detailed (9, 12).
(iv) Probe design and synthesis.
ARB software (http://www.arb-home.de/) and a database comprising publicly available sequences and our in-house clone sequences were used to design probes (Table 1), as detailed by Hugenholtz et al. (18), to be specific for the microbial communities represented in the [12C]DNA and [13C]DNA clone libraries. The probe design procedure specifically targeted groups of clone sequences from each clone library, which allowed discrimination of other reference sequences. The probe sequences were then confirmed for specificity by using BLAST and were submitted to the probe database ProbeBase (www.probebase.net [25]). In this database, difference alignments, on-line specificity analysis, and other relevant information for published rRNA-targeted probes can be obtained. Finally, the designed oligonucleotides were synthesized and labeled at the 5' end with the indocarbocyanine dye CY3 (Thermohybaid Interactiva, Ulm, Germany).
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TABLE 1. FISH oligonucleotides used in this study
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(vi) FISH and MAR.
A sludge sample obtained from the end of a reactor cycle was diluted with reactor effluent to achieve MLVSS concentrations of 1 to 2 g liter-1. To demonstrate active carbon substrate uptake, a control experiment was performed with pasteurized (80°C for 15 min) biomass. For the experiment, a minimum of three sets of 9-ml glass vials were used. Set 1 was inoculated with 4 ml of pasteurized sludge, while sets 2 and 3 were inoculated with nonpasteurized sludge. A volume of 500 µl of sterile reactor feed which included the electron acceptor (nitrate) but not the electron donor (carbon source) was added to vials of sets 1 and 2 to mimic the exact conditions that prevailed in the reactor. To set 3, with nonpasteurized sludge, 500 µl of sterile reactor feed not containing both the electron acceptor (nitrate) and electron donor (carbon source) was added to demonstrate whether the target cells could carry out any anaerobic uptake of the carbon source. The vials were then sealed with butyl rubber stoppers and flushed with oxygen-free nitrogen for 5 to 10 min. To remove any further traces of oxygen from within these vials, they were placed on a rotary shaker at 200 rpm for 30 min. Finally 500 µl of carbon (nonradioactive methanol and 20 µCi of [14C]methanol [Amersham, Little Chalfont, England]) was introduced into each vial to provide electron donor concentrations equivalent to that of the reactor. Strict anaerobic techniques were used on these anoxic samples at all times, and the samples were incubated at room temperature (20°C) on a rotary shaker (200 rpm). The duration of incubation of multiple nonpasteurized samples (in individual 9-ml vials) ranged from 1 to 4 h. A time series was necessary to determine the minimum duration of incubation since overincubation could result in false interpretation due to a possible uptake of radioactive by-products by nontarget organisms. The control vials were incubated for the entire 4-h period. The subsequent steps of the FISH-microautoradiography (MAR) protocol were then carried out as detailed in Lee et al. (21).
(vii) Microbial quantification by biovolume measurement.
The shifts in microbial communities in the parent SBR sludge were monitored and quantified with published probes along with those designed for this study and from previous studies of denitrifying activated sludges (Table 1). The methods used for microbial quantification have already been described by Zeng et al. (39).
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FIG. 1. Profiles of NO3--N ( ), NO2--N (), PO4-3-P ( ), and NH3-N ( ) in an anoxic reactor cycle during the enrichment of the denitrifying sludge.
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Clone libraries and probe development.
The sludge was subjected to SIP and full-cycle rRNA analysis once the reactor reached steady-state operation.
(i) [13C]DNA clone library.
A total of 55 clones of the [13C]DNA clone library from the mini-SBR DNA was screened by RFLP analysis, and these were assigned to 19 different OTUs, although differences in banding patterns were often subtle (data not shown). Three OTUs contained in total 33 clones (26, 4, and 3 clones), while the remaining 16 OTUs contained 1 or 2 clones each. Representatives of most OTUs (32 clones) were partially sequenced to reveal that 25 clones from 10 OTUs had sequences closely related to 16S rRNA gene sequences from organisms in the class Betaproteobacteria. The single largest OTU was called group A and comprised 26 clones or 47% of the library. Phylogenetic analysis of these partial sequences revealed that all group A clone sequences clustered closely together. By evolutionary distance analysis, the nearly complete sequences of seven group A clones clustered with the obligate methylotrophs Methylobacillus and Methylophilus in the order Methylophilales of the Betaproteobacteria (Fig. 2). Due to the high abundance of this group in the clone library and their phylogenetic affiliation with obligate methylotrophs (which have the capacity to grow on methanol or methylamine but not on methane), they became a focus for oligonucleotide probe design. Only nearly complete 16S rRNA gene sequences (positions 28 through 1491; E. coli numbering) of group A clones were used for probe design. Two probes were designed, namely, DEN67 and MET1216 (Fig. 2 and Table 1). DEN67 was highly specific for group A clone sequences, whereas MET1216 targeted all members of the Methylophilales (Fig. 2). The DEN67 probe highlighted a single type of morphologically distinct cell (short rods) in the parent SBR sludge up to the determined optimal formamide concentration (35%). At 35% formamide in FISH, B. cepacia, with 1 nucleotide mismatch in the probe target site, was not detected. The MET1216 probe did not hybridize to the DEN67-targeted cells or any other cell types in the SBR sludge at any formamide concentration and was not further evaluated for FISH. The MET1216 probe is included in Table 1, since it may be a useful probe for specifically targeting the Methylophilales by other methods, such as membrane hybridization. Simultaneous FISH with DEN67 and BET42a (broadly specific for Betaproteobacteria) confirmed that DEN67-targeted cells are members of the Betaproteobacteria (see Fig. 5A).
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FIG. 2. Phylogenetic tree of the group A clones derived from the [13C]DNA clone library and from publicly accessible databases. Evolutionary distance and parsimony analyses were carried out in PAUP*, version 4.0b10, by employing 2,000 bootstrap resamplings. Filled circles at nodes, >75% bootstrap support from both analyses; open circles, 50 to 75% support from both analyses; half-filled circles, analyses where one algorithm gave >75% bootstrap support and the other gave 50 to 75%. Solid lines, specificities of the DEN67 and MET1216 probes designed in this work; dashed lines, probe that does not have 100% identity with some sequences. Neisseria denitrificans (M35020) was used as the outgroup in the analysis but is not shown in the tree. The scale indicates 0.05 nucleotide change per nucleotide position.
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FIG. 5. In situ analyses of denitrifying bacteria in reactor sludge. (A) Confocal laser scanning micrograph of reactor sludge triple hybridized with EUBMix (25 ng of fluorescein-labeled probe, a mixture of EUB338, EUB338-II, and EUB338-III), BET42a (25 ng, Cy5 labeled), and DEN67 (25 ng, Cy3 labeled) probes. The white cell aggregates (arrows), comprising densely packed 1- to 2-µm-diameter cells, are the DEN67-targeted organisms since they are tripled labeled with EUBMix (green), BET42a (blue), and DEN67 (red) probes. The cyan-colored cells are other Betaproteobacteria since they are only dual labeled with EUBMix (green) and BET42a (blue) probes. (B) Confocal laser scanning micrograph of reactor sludge triple hybridized with EUBMix (25 ng, fluorescein labeled), BET42a (25 ng, Cy5 labeled), and HYP1241 (25 ng, Cy3 labeled) probes. The yellow cell aggregates (arrow), composed of 1- to 2-µm-diameter cells, comprise Hyphomicrobium cells since they are dual labeled with EUBMix (green) and HYP1241 (red) probes. The cyan-colored cells are Betaproteobacteria since they are dual labeled with EUBMix (green) and BET42a (blue) probes. (C) Confocal laser scanning micrograph of [14C]methanol-fed reactor sludge dual hybridized with EUBMix (25 ng of fluorescein) and DEN67 (25 ng, Cy3 labeled) probes. The yellow cell aggregates (arrow) are the DEN67-targeted organisms since they are dual labeled with EUBMix (green) and DEN67 (red) probes. The image was compiled by obtaining a stack of images by confocal laser scanning microscopy and combining them by orthographic projection into a single image. The image stack was acquired to ensure that all organisms that contributed to the MAR signal (D) would be visible in the final image. (D) A micrograph of the radiographic film at the same position as that of panel C. Magnification, x500.
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Use of designed and other group-specific probes.
Laboratory scale SBR sludge samples were fixed every 2 weeks and evaluated with the DEN67 and SAP553 probes together with other published FISH probes specific for microbial groups relevant to denitrification (Table 1). Figure 3 shows the shifts that occurred in the SBR microbial community with changes in the measured denitrification rate. The DEN67-targeted population (part of the Betaproteobacteria) initially comprised just 1 to 2% of all bacteria but rose to 38% at SBR steady-state operation. During this time, the BET42a-targeted Betaproteobacteria decreased from 62 to 29 to 39% of all bacteria. The DEN67-targeted-population changes were quite different from these, highlighting the limited utility of broad-specificity probes for studying specific populations of bacteria. The SAP553-targeted population remained at a low level of around 3 to 4% (results not shown in Fig. 3) despite being well represented among the OTUs in the [12C]DNA clone library. The population of the HYP1241-targeted Hyphomicrobium sp. (in the class Alphaproteobacteria and previously associated with denitrification with methanol) remained at approximately 30% of all bacteria, showing only a marginal increase of 2% from its initial population (Fig. 3). The PAR1457-targeted Paracoccus sp. (in the class Alphaproteobacteria, also previously associated with denitrification with methanol) was only occasionally observed in the sludge (data not shown). Figures 3 and 4 demonstrate a significant positive correlation {Pearson's correlation [r(4)] = 0.953; P < 0.01} between the abundance of the DEN67-targeted organisms and the increase in denitrification rates measured in the SBR. Figure 4 shows that there is no significant correlation between Hyphomicrobium sp. abundance and denitrification rates [r(4) = -0.389; P = 0.5]. The DEN67-targeted organisms are observed as clusters of cells in Fig. 5A, while Fig. 5B demonstrates the in situ abundance of Hyphomicrobium.
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FIG. 3. Bacterial community analysis of the reactor sludge as determined by FISH biovolume measurement. The values obtained with Betaproteobacteria
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FIG. 4. Relationship between denitrification rate and DEN67-targeted cells () and HYP1241-targeted (Hyphomicrobium) cells ( ) as a percentage of the EUBMix (a mixture of EUB338, EUB338-II, and EUB338-III probes)-positive cells. **, significant correlation at the P = 0.01 level.
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Three previous studies exploring the identities of methanol-utilizing denitrifiers relied partially on pure-culture-based approaches (20, 23, 28), with a significant drawback being that many microorganisms cannot yet be isolated in pure culture (3). Neef et al. (28) also designed FISH probes for Paracoccus and Hyphomicrobium and applied them to study a methanol-fed, postdenitrification biofilm system. A correlation between the relative abundance of these genera and denitrification performance was used to suggest their active participation in denitrification (28). Lemmer et al. (23) found that the most highly abundant isolate from a methanol-fed, postdenitrification sand filter biofilm was Hydrogenophaga (from Betaproteobacteria and known to be unable to grow on C1 compounds such as methanol), followed by Paracoccus and Hyphomicrobium (Alphaproteobacteria), both recognized denitrifiers. Layton et al. (20) carried out a full-cycle rRNA analysis of pooled sludge samples from a full-scale industrial wastewater treatment plant, where the ability to carry out denitrification with C1 carbon sources such as methanol was an important feature. According to FISH with probe HYP1241, Hyphomicrobium was found to be abundant within and outside the activated sludge flocs. Although these reports demonstrated the presence of substantial microbial diversity in the analyzed systems, they failed to directly demonstrate that the identified microorganisms were indeed respiring anaerobically with nitrate within the systems, since none of the applied methods was suited to study the phenotype of the microorganisms in their ecological niche.
According to FISH with HYP1241, Hyphomicrobium comprised 22 to 40% of the total bacterial population in the laboratory scale SBR (Fig. 3), but its slight shifts in abundance showed no correlation with the rates of denitrification observed (Fig. 4). The Hyphomicrobium present might have adapted to the methanol feedstock, but, if so, this potential adaptation was extremely slow since, even after 30 days of operation, the denitrification rate was still very low (Fig. 3). Although FISH-MAR was not carried out with HYP1241, nearly all bacteria that took up [14C]methanol were targeted by DEN67. The absence of any Hyphomicrobium sequences in the [13C]DNA clone library also does not support the concept that Hyphomicrobium adapted to methanol and was the responsible denitrifier. It is unlikely that Paracoccus played any role in denitrification in the methanol-fed SBR, since PAR1457-targeted cells were only occasionally observed in the sludge. This finding is further supported by the absence of clones related to Paracoccus in the [13C]DNA clone library. These two previously well-reported methanol-utilizing denitrifiers were thus shown not to be responsible for denitrification in our methanol-fed SBR. SAP553 was designed from the [12C]DNA clone library sequences, but the abundance of these Cytophagales was not correlated with denitrification, nor did they appear as a significant group in the [13C]DNA clone library.
The group A clones by evolutionary distance analysis grouped with the obligate methylotrophs Methylobacillus and Methylophilus (Fig. 2), which are able to grow on methanol or methylamine but not on methane. Other methylotrophs, such as Methylomonas, Methylococcus, Methylobacter, Methylosinus, and Methylocystis, are able to grow on both methane and methanol and hence are also methanotrophs (10, 26). The denitrification activity of methylotrophs has not previously been explored, but at least the group A clone cluster from bacteria closely related to Methylobacillus and Methylophilus has been demonstrated in this study to be denitrifiers. This extends the known phenotype of methylotrophs.
Previous researchers (14, 29) hypothesized that the initial lag period in denitrification activity observed in methanol-amended activated sludge systems might be explained by the development of specific methanol-utilizing populations. This study confirms that DEN67-targeted organisms comprise one bacterial group that was present only at very low levels in the original full-scale denitrifying sludge. They were then enriched to become the dominant group in the biomass, which demonstrated a much higher denitrification rate using methanol than the original reactor inoculum. This establishes that a microbial population shift is the most likely cause for the slow development of denitrification capacity when a particular carbon source, for example, methanol, is used. This finding is highly relevant to the practical operation of denitrification in wastewater treatment processes, as the selection of carbon source added needs to be done with due recognition of the associated operational effects caused by bacterial population changes. The use of external carbon addition is becoming more widespread to meet increasingly demanding effluent concentration limits for total nitrogen in many parts of the world. Since methanol is usually the cheapest carbon source, it is commonly used in such situations, although with various degrees of success. Recognizing the influence of the bacterial community composition on the denitrification performance is therefore highly valuable for the study and optimization of denitrification processes using external carbon sources. Further studies determining the impact of other carbon sources on the microbial population are also important in this context and are under way in our research group.
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