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Environmental Processes
Identification of bisphenol-A assimilating microorganisms in mixed microbial communities using C-DNA stable isotope probing 13
Sandeep Sathyamoorthy, Catherine Hoar, and Kartik Chandran Environ. Sci. Technol., Just Accepted Manuscript • DOI: 10.1021/acs.est.8b01976 • Publication Date (Web): 24 Jul 2018 Downloaded from http://pubs.acs.org on July 26, 2018
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Environmental Science & Technology
Identification of bisphenol-A assimilating microorganisms in mixed microbial communities using 13C-DNA stable isotope probing Sandeep Sathyamoorthy‡, Catherine Hoar‡, Kartik Chandran*
Columbia University, Department of Earth and Environmental Engineering, 500 West 120th Street, Room 1045 Mudd Hall, New York, NY 10027. *corresponding author:
[email protected]. ‡These authors contributed equally.
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ABSTRACT
2
A wide range of trace organic contaminants (TOrCs), including the endocrine disrupting
3
compound bisphenol-A (BPA), are subject to microbial transformations during biological
4
wastewater treatment.
5
capable of assimilating emerging contaminants.
6
(DNA-SIP) was used to investigate biodegradation and assimilation of BPA by mixed microbial
7
communities collected from two full-scale wastewater treatment plant bioreactors in New York
8
City and subsequently enriched under two BPA exposure conditions. The four enrichment modes
9
(two reactors with two initial BPA concentrations) resulted in four distinct communities with
10
different BPA degradation rates. Based on DNA-SIP, bacteria related to Sphingobium spp. were
11
dominant in the assimilation of BPA or its metabolites. Variovorax spp. and Pusillimonas spp.
12
also assimilated BPA or its metabolites. Our results highlight that microbial communities
13
originating from wastewater treatment facilities harbor the potential for addressing not only
14
human-derived carbon, but also BPA, a complex anthropogenic TOrC. While previous studies
15
focus on microbial biodegradation of BPA, this study uniquely determines the ‘active’ fraction of
16
microorganisms engaged in assimilation of BPA-derived carbon. Ultimately, information on
17
both biodegradation and assimilation can facilitate better design and operation of engineered
18
treatment processes to achieve BPA removal.
However, relatively little is known about the identity of organisms Here,
13
C-DNA stable isotope probing
19
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INTRODUCTION
21
The ecological impacts of trace organic contaminants (TOrCs) elicit growing concern,
22
particularly in light of research suggesting that chronic exposure to TOrCs may be deleterious to
23
the reproduction and development of aquatic species.1-3 Wastewater treatment plants (WWTPs)
24
are essential barriers for the influx of TOrCs into the environment. Although WWTPs are not
25
currently designed for attenuating TOrCs, reports suggest partial removal and transformation of a
26
wide range of TOrCs within the biological treatment process through both abiotic and biotic
27
reactions.4-6 However, relatively little is known about the identity of microbial species able to
28
assimilate TOrCs.
29
The overall objective of this study was to identify bacteria capable of assimilating the
30
endocrine disrupting compound bisphenol-A (BPA). The release of BPA into the environment is
31
primarily from industrial facilities and WWTPs.7 BPA mimics estrogen and has both agonist and
32
antagonist effects.8 In the environment, chronic exposure to BPA at concentrations as low as
33
10 µg/L can result in transcriptional level changes in the reproductive systems of certain fish
34
species.9 However, other studies have shown no effect of certain BPA exposure treatments on
35
other aquatic species.10 Furthermore, the effects of BPA on different species are varied and not
36
well understood, especially in relation to long-term exposure and implications of BPA mixed
37
with other chemicals.11 Despite its elimination from a wide range of consumer products and
38
industrial formulations, over one million pounds of BPA are released into the environment
39
annually.12 In 2014, BPA was included on the list of chemicals for assessment under the Toxic
40
Substances Control Act by the United States Environmental Protection Agency.12 The removal
41
of BPA in WWTPs is highly variable, ranging from 10% to >99%, with reported WWTP influent
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concentrations of BPA ranging from nondetectable to ~40 µg/L and effluent concentrations
43
ranging from nondetectable to ~20 µg/L.13
44
We evaluated BPA biodegradation and assimilation by two enriched microbial communities
45
originating from an urban WWTP in New York City through substrate consumption and DNA
46
stable isotope probing (DNA-SIP) assays, respectively. DNA-SIP relies on the incorporation of a
47
stable isotope (e.g.,
48
compound in batch substrate depletion assays.14, 15 Isopycnic ultracentrifugation is used to isolate
49
the labeled DNA, and bacteria that carry the
50
Generation Sequencing.16 A variety of SIP techniques have been used to study the
51
biodegradation of a wide range of contaminants, including TOrCs.17-19 In this study, we expand
52
the application of SIP to elucidate the assimilation of BPA or its metabolites by enriched
53
microbial communities originating from a full-scale urban WWTP. Future efforts to achieve or
54
enhance BPA removal could take advantage of the presence of these protagonists in WWTPs
55
through engineering strategies aimed at reconciling specific microbial community structure with
56
biodegradation or treatment function.
13
C or
15
N) into the DNA of bacteria capable of assimilating the labeled
13
C label are subsequently identified using Next
57 58
MATERIALS AND METHODS
59
BPA Degradation Experiments
60
Batch experiments were employed to evaluate the biodegradation and assimilation of BPA by
61
microbial communities initially originating from two separate biological treatment reactors at a
62
full-scale WWTP in New York City. One of these reactors is used for primary effluent treatment
63
(PET reactor) and the other is used to treat reject water from anaerobic digestion after
64
centrifugation (separate centrate treatment – SCT reactor). Samples were collected from aerobic
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zones of both reactors; a simplified process flow diagram of the reactors is shown in Figure S-1
66
(Supplementary Information). The PET and SCT reactors were selected in order to assess the
67
influence of two distinct wastewater treatment processes (Supplementary Information Table S-1)
68
on the microbial community structure and the resulting BPA biodegradation and assimilation
69
potential of these communities.
70
Enrichment of the microbial communities on BPA prior to conducting batch DNA-SIP
71
experiments allowed for the elucidation of microbes with a higher potential for BPA assimilation
72
than the parent activated sludge population along with an assessment of the effect of different
73
BPA exposure conditions on biodegradation. Preliminary experiments indicated that BPA was
74
slowly biodegraded by microbial communities from the PET and SCT reactors after a long lag
75
period (~50-80 h, Supplementary Information Section S-2), conditions that are not ideal or
76
recommended for DNA-SIP experiments.20,
77
conditions were applied to lab scale fed-batch reactors (SI, Section S-3). The first condition was
78
a high concentration (HC) exposure at a dose of 100 mg-BPA/L, which corresponded to the BPA
79
concentration used in the subsequent DNA-SIP experiments. The second condition was a low
80
concentration (LC) dose exposure at 500 µg/L. BPA was added to the fed-batch reactors using a
81
stock solution of BPA in methanol (600 mg-BPA/g and 7,000 µg-BPA/g for HC and LC
82
exposure treatments, respectively) upon >99% removal of BPA. We hypothesized that the
83
selected BPA concentration in the HC and LC-treatments would give rise to distinct diversity
84
and identity of BPA-assimilating microorganisms. Samples from high concentration exposure
85
treatments (PET-HC and SCT-HC) and low concentration exposure treatments (PET-LC and
86
SCT-LC) were collected for SIP experiments after 35 and 40 days, respectively. The resulting
21
During enrichment, two separate exposure
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total BPA loading through the HC and LC exposure treatments was 1,000 mg and 6 mg BPA,
88
respectively.
89 90
13
C-DNA Stable Isotope Probing
91
Biomass samples from each of the four treatments were centrifuged (3,500 xg, 15 min, 4°C
92
using a Beckman Coulter Avanti J-6 XPI centrifuge and JA 25.15 rotor) and the biomass pellets
93
were twice washed and re-suspended in a BPA-free medium for DNA-SIP experiments (see SI,
94
Section S-4 for starting biomass concentrations and Table S-2 for medium details). For each
95
treatment, batch experiments included duplicate
96
experiments. Inclusion of the 12C-BPA control samples allowed us to differentiate the fraction of
97
biomass capable of BPA assimilation from the fraction of the microbial consortium capable of
98
BPA biodegradation. The 12C-BPA SIP controls and
99
in open 20 mL glass scintillation vials (Kimble-Chase, Vineland, NJ) with a liquid volume of 5
100
mL. The vials were sampled at the time of >99.99% removal of BPA to maximize
101
biodegradation and assimilation of
102
metabolites, similar to the approach applied in previous studies, e.g. Baytshtok, et al.22 An
103
additional parallel time-course evaluation (TC) using
104
appropriate time at which to terminate the SIP experiments. The TC experiments were conducted
105
in 40 mL glass scintillation vials (VWR, Radnor, PA) with a liquid volume of 20 mL. A
106
no-biomass control (NB) was also included. All experiments were conducted in duplicate in an
107
orbital shaker (New Brunswick Scientific, Enfield, CT) operating at 260 RPM at 21 ± 1 oC. The
108
target initial BPA concentration in the DNA-SIP experiments, controls and the TC reactors was
109
100 mg/L. Control and TC reactors were spiked with unlabeled BPA (99+%, Sigma-Aldrich,
13
12
C-BPA controls and duplicate
13
13
C-BPA
C-BPA SIP experiments were conducted
C-BPA while minimizing cross-feeding of
12
13
C-BPA
C-BPA was included to determine the
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Saint Louis, MO), and experimental reactors were spiked with labeled Bisphenol-A-(diphenyl-
111
13
112
concentration relative to the typical BPA concentrations detected in wastewater influents was
113
utilized in the DNA-SIP experiments because the biomass yields for BPA for wastewater
114
microbial communities are unknown. Applying a high concentration of the labeled compound
115
ensures the availability of labeled
116
study of emerging contaminant degradation by enriched cultures.23
C12) (99 atom %
13
C, 98%, Sigma-Aldrich, ISOTEC INC, Miamisburg, OH). A high BPA
13
C-DNA, an approach that has been used previously in the
117 118
Analytical Methods
119
BPA was quantified using high performance liquid chromatography with UV detection and
120
mass spectrometry (MS). Separation was achieved using a 3µm analytical Acclaim PA2 column
121
(2.1 x 150 mm; Thermo Scientific) at 30 oC with an isocratic mobile phase consisting of
122
methanol (70 vol %) and water at 0.20 mL/min. The injection volume was 50 µL. Quantification
123
of BPA was based on UV detection at 230 nm (DAD-3000, Thermo Scientific), with a method
124
detection limit of 1.8 µg-BPA/L. Calibration standards were prepared using serial dilutions in
125
water of a stock solution of BPA dissolved in methanol. Identification of BPA was confirmed
126
using MS (MSQ Plus single quadrupole mass spectrometer, Thermo Scientific) using
127
atmospheric pressure charge ionization (APCI) in negative mode with a cone voltage of -65V,
128
source temperature of 550oC and nitrogen pressure of 50 psi.
129 130
DNA Extraction and Density Gradient Ultracentrifugation
131
DNA from biomass samples was extracted with the DNeasy Blood & Tissue Mini Kit protocol
132
using the Qiacube robotic workstation (Qiagen, Valencia, CA) following the manufacturer’s
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protocol. The DNA concentration in the extracts was measured using a NanoDrop lite UV
134
spectrophotometer (Thermo Scientific, Waltham, MA) and the extracted DNA was stored at -
135
20oC. Equal masses of DNA from the duplicate
136
achieve a mass of 5,000 ng DNA for utilization in ultracentrifugation of labeled DNA fractions.
137
This mass of DNA was sufficient for detection and quantification of separated DNA based on
138
preliminary optimization of ultracentrifugation (data not shown) and consideration of the
139
unknown adbundance of and resulting biomass yields for those organisms capable of
140
assimilating BPA or its metabolites. Equal masses of DNA from the 12C-BPA SIP controls were
141
similarly combined.
13
C-BPA SIP experiments were combined to
142
The gradient solution for ultracentrifugation was prepared in a 15 mL centrifuge tube
143
(Corning, Tewksbury, MA) following the method previously described, with minor
144
adjustments.22,
145
1,200 µl, to which 4,800 µl CsCl solution (64 wt%) was added. The density of the gradient
146
solution was determined using a refractometer (Reichert Model Brix/RI-Chek, Reichert
147
Industries, Depew, NY). The density was adjusted using either gradient buffer or CsCl solution
148
to 1.72 g/ml. The gradient solution was loaded into 5 mL polyalomer ultracentrifuge tubes
149
(Beckman Coulter, Jersey City, NJ) and the tubes were balanced to within 10 mg as
150
recommended. Ultracentrifugation (40,000 RPM or ~177,000 xgav, 20 oC, 69 h) was performed
151
at using a vTi 65.2 rotor in a L8-M ultracentrifuge (Beckman Coulter, Jersey City, NJ). Ten
152
gradient fractions (500 µL each) were removed from the ultracentrifuge tube using a syringe
153
pump and bromophenol blue solution.22, 24 The density of each fraction was determined using a
154
refractometer. DNA was recovered from each fraction using ethanol precipitation and
155
resuspended in 100 µL DNA-free water.
24
Gradient buffer24 was added to the combined DNA to a total volume of
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Quantitative real-time polymerase chain reaction (qPCR) was used to measure the abundance
157
of the total bacterial 16S rRNA gene in each fraction using EUB primers25 (forward primer
158
1055f (5′-ATGGCTGTCGTCAGCT-3′) and reverse primer 1392r (5′-ACGGGCGGTGTGTAC-3′),
159
Integrated DNA Technologies, Coralville, IA). qPCR analyses were conducted on an iQ5
160
real-time PCR thermal cycler (BioRad, Hercules, CA) using SYBR® green chemistry in a 25 uL
161
reaction mixture with the specific components of the reaction mixture as follows: mastermix 12.5
162
µL (iQ SYBR® Green Supermix), forward primer 1.0 µL, reverse primer 1.0 µL, 5 µL target
163
DNA and nuclease-free water 5.5 µL. Primer stock solutions used in the reactions were made at
164
a concentration of 5 µM. The reactions were performed in triplicate for each sample with a set of
165
triplicate standards and no-template controls included in each plate. The standards used in each
166
assay were generated through serial decimal dilutions of a stock standard of plasmid DNA with
167
the targeted 16S rRNA gene inserts. Absence of primer dimers was confirmed for each reaction
168
based on inspection of the melt-curves. Information for the qPCR standard curve and qPCR
169
results is included in SI Section S-5.
170 171
DNA Sequencing and Analysis of Sequencing Data
172
Ion Torrent sequencing was employed to identify BPA assimilating bacteria in each of the
173
microbial communities. Equal volumes of DNA from each of the independently obtained
174
duplicate heavy-DNA gradient fractions (density > 1.737 g/mL) from a given ultracentrifugation
175
tube were pooled to produce a single heavy-DNA sample. The light-DNA gradient fractions
176
(density ≤ 1.737 g/mL) from the ultracentrifugation tube were similarly pooled for each tube.
177
Therefore, four pooled DNA samples were sequenced from each of the four SIP experiments
178
(12C-SIP controls and
13
C-SIP experiments from PET and SCT reactors). These sixteen heavy
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and light pooled DNA samples, in addition to the DNA from the four microbial consortia at the
180
start of the SIP experiments and the PET and SCT reactors at the start of the exposure treatments,
181
were sequenced via amplicon sequencing of the 16S rRNA gene using the Ion Torrent Personal
182
Genome Machine (PGM) platform (Thermo Fisher Scientific).
183
Amplification for preparation of the sequencing libraries was carried out using the fusion
184
method
(Thermo
Fisher
Scientific)
with
the
forward
primer
1055f
185
(5′-ATGGCTGTCGTCAGCT-3′) and reverse primer 1392r (5′-ACGGGCGGTGTGTAC-3′) that
186
were linked to unique 6-nucleotide multiplex barcodes (Ion Xpress barcode adapters, Thermo
187
Fisher Scientific). The amplification consisted of 30 cycles of 94 °C for 30 s, 55 °C for 30 s, and
188
68 °C for 90 s. Amplification reactions were performed in a 25 µL reaction mixture with the
189
following components: mastermix 12.5 µL (iQ Sybrmix, BioRad, Hercules, CA), forward fusion
190
primer 1.0 µL, reverse fusion primer 1.0 µL, nuclease-free water 5.5 µL and template DNA
191
5.0 µL. The amplified DNA was purified using the Qiaquick PCR Purification protocol using the
192
Qiacube robotic workstation (Qiagen, Valencia, CA).
193
Sequencing libraries were quantified using the KAPA library quantification kit (KAPA
194
biosystems, Wilmington, MA) following the manufacturer’s protocol with minor modifications.
195
DNA libraries were diluted (1:2000) in nuclease-free water. The reactions were performed in a
196
20 µL reaction mixture with the following components: mastermix 10 µL (KAPA SYBR®
197
FAST qPCR Master Mix), forward/reverse primer mix 2 µL (10x Ion Torrent primer mix),
198
nuclease-free water 6 µL and diluted library DNA 2 µL. Sequencing libraries were each prepared
199
at a concentration of 100 pM and combined. A diluted library at a concentration of 8 pM was
200
subsequently enriched using the Ion PGM™ Template OT2 400 Kit (Thermo Fisher Scientific).
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The enriched samples were loaded onto a 316 Chip v2 and sequenced using the 400-bp
202
sequencing kit (Thermo Fisher Scientific).
203
Raw sequence reads from the Torrent Suite server were converted to fastq format and
204
processed using tools available in Mothur26 within the Galaxy platform.27, 28 Raw sequence reads
205
were trimmed using Mothur to remove those sequences with (i) a sequence length shorter than
206
280 or longer than 380 nt and (ii) an average quality score of 99.99% in all four SIP experiment batch incubation
218
reactors (PET-HC, SCT-HC, PET-LC and SCT-LC), over a course of 20 h, 36 h, 48 h and 58 h,
219
respectively (Figure 1). For each reactor, initial BPA-degradation was characterized by a lag
220
phase, followed by an approximately linear decrease in BPA concentration. Biomass-normalized
221
biodegradation coefficients for this period of linear degradation were estimated to be ~6 µg-
222
BPA/(mg-pCODh) for PET-HC, ~3 µg-BPA/(mg-pCODh) for SCT-HC, ~8 µg-BPA/(mg-
223
pCODh) for PET-LC, and ~4 µg-BPA/(mg-pCODh) for SCT-LC, (SI, Section S-7, Table S-5).
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Therefore, for the same exposure treatment, BPA biodegradation by the PET microbial
225
community occurred more rapidly than biodegradation by the SCT community, likely linked to
226
differences in structure and function of the two communities. Such differences may have
227
originated from different WWTP process conditions (e.g. diversity and availability of carbon
228
substrates) of the source biomass, which persisted through enrichment, though an assessment of
229
these factors was beyond the scope of this work. Nonetheless, BPA exposure indeed resulted in
230
distinct enriched community structures, as indicated by 16S rRNA gene-based phylogenetic
231
analysis (see details in the following section: Exposure Conditions Influence Microbial
232
Community Structure).
233
During all four experiments, a biodegradation metabolite was produced (as detected using
234
HPLC-UV-MS) and subsequently consumed. The UV spectrum of the metabolite exhibited a
235
single broad peak at 277 - 278 nm. Analysis of the mass spectrum identified dominant ions with
236
m/z ratios of 226 and 241 in negative-ion mode, and 149 and 243 in positive-ion mode,
237
respectively (SI, Section S-8). Positive identification of this and any other metabolites in future
238
studies would be useful in further understanding relevant biodegradation pathways, though such
239
analysis was beyond the scope of this work.
240 241
Analysis of SIP Gradient Fractions
242
The EUB gene-copy density profile for gradient fractions from the
12
C-BPA experiments
243
indicated a single peak with the center of mass in the range of 1.71 – 1.73 g/mL (Figure 2 (left
244
panel) and SI, Figure S-7 (Section S-9)). For the
245
density (~1.74 – 1.77 g/mL) was present in the EUB gene-copy density profiles from all four
246
13
13
C-SIP experiments, a second peak of higher
C-SIP experiments (SI, Figure S-7). The proportion of heavy-DNA (i.e., density >1.737 g/mL)
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247
gene copies present in the
248
high concentration BPA exposure) were 0.15 and 0.35, respectively (Table 1 and SI, Figure S-7,
249
calculated as the ratio of gene copies in the heavy fraction to the total gene copies in the sample).
250
In contrast, the proportion of heavy-DNA in the PET-LC and SCT-LC experiments were 0.51
251
and 0.63, respectively (Table 1). The higher proportion of heavy-DNA from the two SIP
252
incubations using the biomass previously exposed to a lower BPA concentration (i.e., PET-LC
253
and SCT-LC) reflected more effective assimilation of 13C-BPA or 13C-BPA metabolites over the
254
longer duration of BPA biodegradation observed for the ‘LC’ incubations (see Figure 1).
255
C-BPA samples from the PET-HC and SCT-HC experiments (i.e.,
Bacteria affiliated with the phylum Proteobacteria were preponderant in the heavy-DNA pool 13
256
from each of the four
257
reads, and α-Proteobacteria comprised between 65% and 98% of the bacterial reads from the
258
heavy-DNA pool (Figure 2, right panel and SI, Figure S-8 – S-11). The relative abundance of
259
α-Proteobacteria in the heavy-DNA pool samples from all four of the
260
significantly higher (z-test with α = 0.05) than that measured in the enriched samples collected
261
for SIP experiments (e.g., sample SCT-HC in Figure 2) or the initial samples collected from the
262
WWTP (e.g., sample SCT in Figure 2). This suggests that α-Proteobacteria may be preferentially
263
involved in the biodegradation and assimilation of BPA and its metabolites. Indeed, the
264
microbial communities derived from the heavy-pools of the 13C-BPA experiments are dominated
265
by relatively few bacterial genera as evidenced by their low Shannon-Wiener diversity indices
266
(SI, Table S-6: H’ = 0.09 – 1.87).
C-BPA SIP experiments accounting for greater than 95% of bacterial
13
C experiments was
267 268
Identification of Bisphenol-A Assimilating Bacteria
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Based on 16S rRNA gene-based phylogenetic analysis, the 13C-DNA pools from the PET-HC,
270
PET-LC, SCT-HC and SCT-LC samples were highly enriched (79%, 98%, 57% and 96%,
271
respectively) in bacteria related to Sphingobium spp. (genus-level analysis, Figure 3). Other
272
genera, notably Variovorax spp. and Novosphingobium spp., were also identified in the
273
heavy-DNA pool of the
274
(Figure 3). Based on a comparison of the inferred microbial community structure in the
275
heavy-DNA pool from each 13C-BPA SIP experiment with the heavy-DNA pool of the 12C-BPA
276
control, we identified genera which assimilated the
277
metabolites. It should be noted that the heavy-DNA pool associated with the
278
represents those microorganisms with DNA of inherently high buoyant density due to a high
279
G+C content and not due to assimilation of
280
assimilators were those present with a representation ratio greater than one. We define the
281
representation ratio to mathematically describe the ratio of the relative abundance of a genus in
282
the heavy-DNA pool from the
283
genus in the heavy-DNA pool from the 12C-BPA control. Our analysis revealed that the heavy-
284
DNA pool from the SCT-HC SIP experiment had the largest number of genera with a
285
representation ratio of greater than one (17) while the heavy-DNA pools from the PET-HC,
286
PET-LC and SCT-LC experiments each had three or fewer genera with a representation ratio
287
greater than one. The most prominent potential BPA assimilating genus was Sphingobium, which
288
had high relative abundance (>50% from all experiments) and an average representation ratio of
289
2.3 ± 0.8 across all experiments. The SCT-HC SIP experiment resulted in the most diverse set of
290
potential BPA assimilating organisms, which, in addition to Sphingobium spp., included
291
Sphingomonas spp., Pusillimonas spp., Novosphingobium spp., and GKS98 spp. among others
13
C-BPA SIP experiments using the PET-HC and SCT-HC biomass
13
13
13
C-label from
13
C-BPA or 12
13
C-labeled
C-BPA control
C-labeled BPA. Identified potential BPA
C-labeled experiment to the relative abundance of the same
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(Figure 4). Pusillimonas spp. were identified as potential BPA assimilators only through the
293
SCT-HC SIP experiment.
294
Bacteria belonging to the genera Sphingobium and Sphingomonas (see SI, Table S-7 for
295
details) have been previously identified as capable of using BPA or other endocrine disrupting
296
compounds as a sole carbon source for growth.30-35 Identification of Sphingomonas spp. as
297
potential BPA assimilators in this work thus provides direct evidence of their previously reported
298
growth on BPA. Here we also report the hitherto undocumented ability of Variovorax spp. or
299
Pusillimonas spp. to assimilate BPA or its biodegradation products. Relevant enzymes and
300
pathways for the degradation of aromatic compounds, including BPA, have been proposed for
301
several species of Sphingomonads.35, 36 Future research aimed at obtaining isolates of these BPA
302
assimilating species would help provide a deeper understanding of BPA biodegradation kinetics
303
and metabolic pathways. While isolates were not studied in this work, insights gained from
304
DNA-SIP can form the first line of evidence towards an exploration of degradation pathways in
305
mixed cultures by newly identified degraders or assimilators. Representation ratios above one for
306
Variovorax spp. and Pusillimonas spp. (Figure 4) were observed only in either of the two
307
experiments in which a high BPA (100 mg/L) concentration was utilized during the exposure
308
treatment (PET-HC or SCT-HC), suggesting a lower BPA affinity coefficient for these bacteria
309
relative to Sphingobium spp. Variovorax paradoxus are able to degrade complex organic
310
compounds and are often found in highly polluted engineered and natural systems.37-40
311
β-Proteobacteria GKS98 spp. have previously been implicated as typical freshwater bacteria.41
312
The potential complexity of BPA biodegradation by mixed culture systems warrants further
313
investigation into the individual roles and functions of specific genera. If, for example,
314
assimilating bacteria identified here are unable to act directly on BPA, they may instead be
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involved in assimilating metabolites of BPA, suggesting cooperation in the biodegradation and
316
assimilation of BPA by multiple bacteria within mixed microbial communities.
317 318
Exposure Conditions Influence Microbial Community Structure
319
Exposure to BPA in the high-concentration exposure treatment (100 mg/L) resulted in
320
differing enrichment of Sphingobacteria in the PET reactor and β-Proteobacteria in the SCT
321
reactor (SI, Figure S-12), which highlights the effect of the BPA exposure treatment on microbial
322
community structure. The relative abundance of the potential BPA assimilating Sphingobium
323
spp. increased in both PET-HC and SCT-HC exposure treatments (Figure 5). The low
324
concentration exposure treatment (500 µg/L BPA) also resulted in an increase in relative
325
abundance of Sphingobium spp. An increase in the relative abundance of other potential BPA
326
assimilating genera identified in this research (e.g., Pusillimonas spp. and Comamonas spp.) was
327
also observed in the SCT-HC exposure treatment. Interestingly however, the relative abundance
328
of the ‘BPA non-assimilators’ Methylobacillus spp. and Castellaniella spp. increased by more
329
than 5% in the SCT-HC but not the PET-HC exposure treatment (Figure 5). Note that the relative
330
abundance of these two BPA non-assimilating genera was less 0.02% in the samples collected
331
from both the PET and SCT reactors. The growth of Methylobacillus spp., which are reportedly
332
obligate methylotrophs,42 may be explained by the addition of methanol used to dissolve BPA, to
333
the fed-batch reactors. However, it is interesting that the same increase in relative abundance of
334
Methylobacillus spp. or other methylotrophs was not observed in the PET-HC reactor despite the
335
fact that the same total methanol COD was added to both high-concentration exposure
336
treatments. Rather, the microbial community dynamics in the PET-HC reactor favored BPA
337
assimilating organisms. Therefore, enrichments resulted in distinct communities (SI, Figure S-
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338
12), even across identical BPA exposure conditions, which suggests a persisting influence of the
339
starting community conditions.
340 341
Assessing the potential for BPA biodegradation and assimilation in WWTP bioreactors
342
Using the results from our SIP experiments, we classified the microbial communities into three
343
categories – potential BPA assimilators, potential BPA degraders and potential BPA non-
344
degraders. Potential BPA assimilators are those bacteria in the microbial community that took up
345
the 13C BPA-derived carbon, identified based on a representation ratio greater than one. Potential
346
BPA degraders are those bacteria that are able to degrade but not assimilate BPA and/or
347
biodegradation products and were identified based on (1) a representation ratio less than or equal
348
to one and (2) increased abundance and relative abundance from the start to end of each SIP
349
experiment. Potential BPA non-degraders are those bacteria that neither assimilate nor degrade
350
BPA or its biodegradation product(s). Genera with (1) representation ratios less than or equal to
351
one and (2) decreased or unchanged abundances from the start to the end of each SIP experiment
352
were classified as potential BPA non-degraders. This classification distinguishing assimilating
353
and non-assimilating bacteria underscores the utility of DNA-SIP. This distinction could not be
354
made by examining enrichment alone, since bacteria from both the assimilating and non-
355
assimilating groups increased in abundance over the course of BPA exposure.
356
Despite the significant differences in the treatment process conditions in the PET and SCT
357
reactors (see SI, Table S-1), the distributions of microbial genera enriched from these two
358
reactors were not statistically different (Mann Whitney test with α = 0.05). Both PET and SCT
359
initiated microbial enrichments were dominated by α, β, γ-Proteobacteria and Sphingobacteria,
360
with each being represented in approximately the same proportion (SI, Figure S-12). Analysis of
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361
the relative abundance of bacteria within the PET and SCT reactors suggests that while the
362
reactors were composed primarily of potential BPA non-degraders (79% and 78%, respectively),
363
both the PET and SCT reactors had the capacity for BPA degradation and assimilation, with
364
comparable combined fractions of potential BPA degraders (18% and 11%, respectively) and
365
assimilators (3% and 11%, respectively). However, the analysis does indicate that the SCT
366
bioreactor had the potential for a higher fraction of BPA assimilating microorganisms. Similar
367
analysis through molecular methods such as DNA sequencing or qPCR targeting relevant
368
organisms could be used as a preliminary assessment of the potential for TOrC degradation or
369
enrichment in both engineered and natural systems.
370
In conclusion, our application of DNA-SIP elucidated numerous Proteobacteria potentially
371
capable of assimilating BPA or biodegradation metabolites. We identified genera which have
372
been previously reported as capable of growth on BPA (e.g., Sphingobium spp. and
373
Sphingomonas spp.) and elucidated novel assimilators such as Pusillimonas spp. and Variovorax
374
spp. Results from our research can help to guide the design and development of specific
375
biomarkers to evaluate the potential for primary BPA assimilation and secondary assimilation of
376
its metabolites, in engineered and natural environmental systems. Our results confirm that
377
wastewater treatment process operating conditions and BPA exposure history play a role in
378
shaping microbial community structure and function. Additional research is warranted to explore
379
links between microbial community structure, function and the metabolic capability to degrade
380
and assimilate additional emerging contaminants. Such research will beneficially inform the
381
design and operation of engineered environmental systems and enable better characterization of
382
the ability of natural systems to degrade an ever-growing suite of complex anthropogenic
383
chemicals being detected in global water bodies.
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384 385
ACKNOWLEDGMENTS
386
Funding sources
387
This work was supported by the National Science Foundation, (CBET 1438578) and the Water
388
Environment Research Foundation.
389
Supporting Information. SI Sections S-1 through S-9, Tables S-1 through S-7 and Figures S-1
390
through S-12 can be found in the Supplementary Information file.
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TABLES
Table 1. Fraction of EUB gene copies in light (ρ ≤ 1.737 g/mL) and heavy (ρ > 1.737 g/mL) fractions from 12C-BPA controls and 13C-BPA SIP experiments. Enrichment exposure BPA Conc. (µg/L) Sample
100,000
500
PET-HC
SCT-HC
PET-LC
SCT-LC
light
99.3%
97.6%
96.6%
99.2%
heavy
0.7%
2.4%
3.4%
0.8%
light
85%
65%
49%
37%
heavy
15%
35%
51%
63%
Fractions from 12C-BPA control
Fractions from 13C-BPA experiment
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FIGURES
PET-HC SIP sample
PET-LC SIP sample SCT-HC SCT-LC SIP sample SIP sample
B P A C on c en tration (m g/L )
120 100 80 60 P E T -HC P E T -L C S C T -HC S C T -L C HC -no biomas s L C -no biomas s
40 20 0 0
10
20
30
40
50
60
Tim e (h ) Figure 1. BPA concentrations for time course evaluation (TC) reactors from SIP experiments. Results are shown for microbial communities originally derived from the PET and SCT bioreactors following high concentration exposure (PET-HC and SCT-HC) and low concentration exposure (PET-LC and SCT-LC). Results are also shown for the no biomass controls. Sampling time points are indicated.
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1.70
1.0
SCTSCT-HC 1.0
1.0
SCTSCT-HC 12C
1.0
0.8
0.8
0.6
0.6
0.4
0.4
0.2
0.2
0.0 1.0
0.0 1.0
0.8
0.8
0.6
0.6
0.4
0.4
0.2
0.2
0.0
0.0
0.8
0.8
1.72
Relative Abundance
Density (g/mL)
1.71
1.73 1.74 1.75 1.76
0.6
0.4
0.2
0.6
0.4
0.2
1.77 0.0
0.2
0.4
0.6
0.8
SCTSCT-HC 13C
Light Fractions
SCT-HC 13C SCT-HC 12C
Heavy Fractions
SCT
1.69
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Other Flavobacteria Spartobacteria Verrucomicrobiae Acidobacteria Chlamydiae Chlorobia Sphingobacteria Cytophagia Anaerolineae Actinobacteria Phycisphaerae Planctomycetacia Deltaproteobacteria Betaproteobacteria Gammaproteobacteria Alphaproteobacteria
1.0 0.0
0.0
Fraction of EUB copies Figure 2. (Left Panel) Post ultracentrifugation EUB-gene copy-density profile from SCT-HC 12C control and 13C experiment. Dashed line indicates density threshold of 1.737 g/ml delineating heavy and light gradient fractions. (Right Panel) Relative abundances of different bacteria classes in the biomass collected from (i) the SCT reactor (SCT) and (ii) sample collected at the start of the SIP experiment following the high concentration exposure treatment (SCT-HC), shown alongside relative abundance of bacteria classes from the light and heavy fractions from the SCT-HC 12C and SCT-HC 13C.
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Is os phaera
Planctomycetacia
L uteimonas
γ -Proteobacteria
Xanthomonas
P E T-HC P E T-L C S C T-HC S C T-L C
R hodanobacter P s eudoxanthomonas P s eudomonas β -Proteobacteria
Methylobacillus Variovorax Hydrogenophaga C omamonas C as tellaniella P us illimonas GK S 98 S phingomonas
α -Proteobacteria
S phingobium Novos phingobium R hodobacter Actinobacteria
Acidimicrobineae 0.00
0.05
0.10 0.60 0.80 1.00
R elativ e A bu n dan c e Figure 3. Relative abundance of genera which are present in the heavy fraction following ultracentrifugation of DNA from the
13
C-BPA SIP experiments for the PET-HC, PET-LC,
SCT-HC and SCT-LC SIP experiments. Only those genera present at ≥0.05% in any of the heavy fractions are shown.
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5
SIP expt.
Representation Ratio
Order
PET-HC PET-LC SCT-HC SCT-LC
GKS98
4
Acidobacteria Actinobacteria Alphaproteobacteria Betaproteobacteria Deltaproteobacteria Gammaproteobacteria Planctomycetacia Verrucomicrobiae Other
Pusillimonas
3
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Sphingobium
Variovorax Afipia
2
Novosphingobium Sphingomonas
1
0 0.00
0.02
0.04
0.06
0.08 0.50
1.00
Relative abundance in heavy fraction 13 from C-DNA SIP experiment Figure 4. Evaluation of relative enrichment of genera based on the Representation Ratio (see text for details) and relative abundance of genera in the heavy DNA fraction from SIP experiments.
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Assimilators
γ -Proteobacteria
F ulvimonas P s eudomonas Azomonas P eredibacter Alicycliphilus C urvibacter C omamonas B ordetella P us illimonas P igmentiphaga Achromobacter GKS 98 Variovorax S phingomonas Novos phingobium B os ea Afipia S phingobium
δ -Proteobacteria β -Proteobacteria
P E T -HC P E T -L C S C T -HC S C T -L C
α -Proteobacteria
0.00
0.02
0.04
0.06
0.08
0.10
Non-Assimilators Planctomycetacia
Is os phaera R hodanobacter L uteimonas F luvicola Hydrogenophaga Methylovers atilis Methylobacillus C as tellaniella P arvibaculum Acidimicrobineae
γ -Proteobacteria Flavobacteria
α -Proteobacteria
α -Proteobacteria Actinobacteria 0.00
1
0.02
0.04
0.06
0.08
0.10
C han ge in R elativ e A bun dan c e th rou gh E x pos u re
2
Figure 5. (top panel) Enrichment of BPA assimilators identified in this research (i.e., genera
3
with a representation ratio greater than 1) through the high and low concentration exposure 25 ACS Paragon Plus Environment
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4
treatments for those taxa with a relative abundance greater than 0.05%.
(bottom panel)
5
Enrichment of genera not able to assimilate BPA or metabolites but which exhibited an increase
6
in relative abundance of 1% or greater as a result of the exposure treatment.
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ABSTRACT ART
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