Ligand-Enhanced Abiotic Iron Oxidation and the E
ff
ects of Chemical
versus Biological Iron Cycling in Anoxic Environments
Sebastian H. Kopf,
†
Cynthia Henny,
§
and Dianne K. Newman
*
,
†
,
‡
,
∥
†
Division of Geologial and Planetary Sciences and
‡
Division of Biology, California Institute of Technology, Pasadena, California,
United States
§
Research Center for Limnology, LIPI, Cibinong, Indonesia
∥
Howard Hughes Medical Institute, Pasadena, California, United States
*
S
Supporting Information
ABSTRACT:
This study introduces a newly isolated, genet-
ically tractable bacterium (
Pseudogulbenkiania
sp. strain MAI-1)
and explores the extent to which its nitrate-dependent iron-
oxidation activity is directly biologically catalyzed. Speci
fi
cally,
we focused on the role of iron chelating ligands in promoting
chemical oxidation of Fe(II) by nitrite under anoxic conditions.
Strong organic ligands such as nitrilotriacetate and citrate can
substantially enhance chemical oxidation of Fe(II) by nitrite at
circumneutral pH. We show that strain MAI-1 exhibits
unambiguous biological Fe(II) oxidation despite a signi
fi
cant
contribution (
∼
30
−
35%) from ligand-enhanced chemical
oxidation. Our work with the model denitrifying strain
Paracoccus denitri
fi
cans
further shows that ligand-enhanced
chemical oxidation of Fe(II) by microbially produced nitrite can be an important general side e
ff
ect of biological denitri
fi
cation.
Our assessment of reaction rates derived from literature reports of anaerobic Fe(II) oxidation, both chemical and biological,
highlights the potential competition and likely co-occurrence of chemical Fe(II) oxidation (mediated by microbial production of
nitrite) and truly biological Fe(II) oxidation.
■
INTRODUCTION
Fe(II)/Fe(III) is an important redox couple in natural
environments.
1
In anoxic systems, iron oxidation can be
mediated by several biological agents, such as anoxygenic
phototrophs
2,3
and nitrate-dependent chemotrophs.
4,5
While
the enzymatic machinery for Fe(II) oxidation has been
identi
fi
ed and characterized for two anoxygenic photo-
trophs,
3,6,7
comparable catalysts have not yet been identi
fi
ed
for nitrate-dependent chemotrophs. Toward this end, we
isolated a fast growing Fe(II) oxidizing, nitrate-dependent
chemotroph from the iron-rich tropical Lake Matano,
8
with the
intention of developing it into a model genetic system.
However, work with the isolate highlighted a second, often
overlooked aspect of Fe(II) oxidation in anoxic environments:
direct chemical interaction with nitrite (a form of chemo-
denitri
fi
cation
9
). Being able to distinguish the mechanisms and
turnover rates of direct biological versus abiotic components of
anaerobic Fe(II) oxidation is necessary to gain a complete
understanding of the biogeochemical coupling of the N and Fe
redox cycles. Here, we expand our understanding of chemo-
denitri
fi
cation by experimental elucidation of how organic
ligands promote abiotic Fe(II) oxidation by nitrite, and discuss
its relevance to assessing the potential co-occurrence of
chemical and biological Fe(II) oxidation.
The isolation and characterization of an increasing number of
microorganisms capable of nitrate-dependent anaerobic Fe(II)
oxidation in recent years
4,5,10
−
16
has revealed the potential for
chemotrophic recycling of Fe(II) in anoxic systems. However,
deconvolving the chemical and biological aspects of this process
remains challenging in many environmental settings
17,18
and
even laboratory studies.
19,20
The complication arises whenever
denitrifying organisms reduce nitrate in iron-rich anoxic
systems, where the metabolic intermediate nitrite can oxidize
Fe(II).
21
−
26
This was recently highlighted in a review by
Picardal,
27
which underscored that while biologically induced
(through the production of nitrite during biological denitri
fi
-
cation), Fe(II) oxidation can be abiotically catalyzed and
proceed by chemodenitri
fi
cation. Because Fe(II) oxidation may
also be directly catalyzed by (potentially the same) denitrifying
organisms, two competing pathways exist whose precise
mechanisms and relative importance in nature are poorly
understood. While the physiology of nitrate-dependent Fe(II)-
oxidizing bacteria has been the subject of a growing number of
studies,
16,24,28
−
30
the chemical aspect of anaerobic Fe(II)
Received:
March 22, 2012
Revised:
February 6, 2013
Accepted:
February 12, 2013
Published:
February 12, 2013
Article
pubs.acs.org/est
© 2013 American Chemical Society
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2611
oxidation by nitrite has received less attention,
27,31
despite its
relevance to constraining the extent of its microbial counter-
part.
Rapid oxidation of Fe(II) by nitrite in strongly acidic
conditions was described as early as 1936,
32
with high reaction
rates linked to the generation and subsequent degradation of
nitrous acid (p
K
a
= 3.4). At circumneutral pH, nitrite is stable
and anaerobic Fe(II) oxidation requires a catalyst or suitable
Fe(II)-containing mineral to proceed at appreciable rates.
Acceleration of this process has been reported with a number of
speci
fi
c Fe(II) mineral phases and catalysts, such as Cu
2+
,
33
iron
oxides and hydroxides,
31,34
−
37
green rust,
25,38
as well as
siderite
39
and vivianite,
23
and even microbial surfaces,
22
providing possible reaction mechanisms for Fe(II)-oxidizing
chemodenitri
fi
cation. The same is true for nitrate, which is
generally less reactive toward Fe(II) than nitrite at circum-
neutral pH,
40
but can similarly bene
fi
t from metal and mineral
catalysis.
41,42
However, metals and surfaces are not the only
agents for chemical catalysis. While the kinetic e
ff
ects of ligands
(including EDTA, NTA, and citrate) on iron redox processes in
oxic environments have been explored before
43
−
46
and often
lead to acceleration of Fe(II) oxidation, much less is known
about their e
ff
ects in the absence of molecular oxygen. Several
studies have investigated the e
ff
ect of ligands on iron redox
processes in acidic conditions and solvents,
47,48
but with the
notable exception of studies on microbial Fe(II) oxidation in
the presence of EDTA,
13,49
little is known about the impact of
ligands at circumneutral pH.
Here, we investigate the e
ff
ect of several Fe(II)-chelating
ligands on iron-oxidizing chemodenitri
fi
cation to (1) assess true
biological Fe(II) oxidation in the newly isolated
β
-proteobacte-
rium
Pseudogulbenkiania
sp. strain MAI-1 and (2) elucidate the
role ligands could play more generally in abiotic Fe(II)
oxidation in laboratory and environmental settings. We use
Paracoccus denitri
fi
cans
as a model strain to show how Fe(II)
oxidation can appear to be directly biologically catalyzed when,
in fact, much of this activity may only be indirectly biologically
mediated. We describe the kinetics and potential reaction
mechanism of the chemical oxidation of Fe(II) by nitrite
observed in these experiments and discuss their relevance for
the interpretation of laboratory and environmental studies. We
place our
fi
ndings in the context of chemical and biological
oxidation rates reported in the literature to evaluate their
relative importance in anaerobic Fe(II) oxidation.
■
MATERIALS AND METHODS
Media.
All reagent solutions were autoclaved or
fi
lter-
sterilized prior to use. The basal medium for all experiments
was a freshwater medium containing 500 mg/L MgSO
4
·
7H
2
O,
300 mg/L NH
4
Cl, 100 mg/L CaCl
2
·
2H
2
O, and 5.4 mg/L
KH
2
PO
4
·
H
2
O
2
. For microbial cultures, the medium was
amended with a 1000
×
vitamin mix (
fi
nal concentrations in
the medium: 40
μ
g/L 4-aminobenzoic acid, 10
μ
g/L D-biotin,
100
μ
g/L nicotinic acid, 50
μ
g/L Ca pantothenate, 100
μ
g/L
pyridoxamine
·
2HCl, 100
μ
g/L thiamine
·
2Cl) and a 1000
×
trace element solution (
fi
nal concentrations in the medium: 1.1
mg/L FeSO
4
·
7H
2
O, 42
μ
g/L ZnCl
2
,50
μ
g/L MnCl
2
·
4H
2
O,
190
μ
g/L CoCl
2
·
6H
2
O, 2
μ
g/L CuCl
2
·
2H
2
O, 24
μ
g/L
NiCl
2
·
6H
2
O, 18
μ
g/L Na
2
MoO
4
·
2H
2
O, 300
μ
g/L H
3
BO
3
).
50
For aerobic cultures, the medium was bu
ff
ered to pH 7.2 with
20 mM phosphate. For anoxic experiments, the medium was
pH bu
ff
ered with 22 mM NaHCO
3
and adjusted to pH 7 with
1 M HCl under an oxygen free atmosphere containing 15%
CO
2
. Phosphate addition was minimal (but not microbially
growth inhibiting) to avoid
precipitation of vivianite
(Fe
3
(PO
4
)
2
·
8H
2
O) at high Fe(II) concentrations. The
fi
nal
ionic strength was
∼
0.04 M. Anoxic solutions were prepared
using O
2
-free deionized water and stored anoxically for at least
three days prior to use. Reactant solutions containing nitrite
were always prepared fresh from an anoxic stock solution kept
at pH 11 to avoid degradation through self-decomposition. All
glassware and plastics were autoclaved and stored anoxically for
at least three days prior to use.
Bacterial Strains.
Paracoccus denitri
fi
cans
strain ATCC
19367 was obtained from the United States Department of
Agriculture culture collection and was grown routinely in
anoxic freshwater medium under denitrifying conditions with
succinate as the growth substrate.
Pseudogulbenkiania
sp. strain
MAI-1 is a newly isolated
β
-proteobacterium that was routinely
growninanoxicfreshwatermediumunderdenitrifying
conditions with acetate as the growth substrate.
Isolation.
Cultures of anaerobic Fe(II) oxidizing chemo-
trophs were enriched by inoculating freshwater medium
supplemented with 10 mM FeCl
2
,10mMNa
3
NTA, 2 mM
Na acetate, and 5 mM NaNO
3
with samples from a microbial
mat in the litterol zone of iron-rich tropical Lake Matano,
Sulawesi Island, Indonesia.
8
Enrichments were incubated at 30
°
C in the dark. After a few days, some enrichments developed
the characteristic dark green color of Fe(III)-NTA, indicating
Fe(II) oxidation. Cultures exhibiting fast Fe(II) oxidation were
transferred successively to fresh Fe(II)-containing medium.
After four transfers, serial dilutions of enrichments were plated
on YP agar pates (0.3% yeast extract, 0.3% Difco Bacto
Peptone, 1.2% agarose) and incubated aerobically at 30
°
Cin
the dark to identify strains potentially suitable for genetic
manipulation. Colonies were picked and subcultured in the
Fe(II) enrichment medium. Fast Fe(II) oxidizers were plated
again, and the purity was assessed by phase-contrast
microscopy. The 1497-bp 16S rRNA gene sequence of strain
MAI-1 was deposited in the GenBank database under the
accession number HQ714499. The pure strain was deposited
with the American Type Culture Collection under the ATCC
number BAA-2177.
Analytical Techniques.
The concentration of Fe(II) was
determined colorimetrically at 562 nm using the ferrozine [3-
(2-pyridyl)-5,6 bis(4-phenylsulfonic acid)-1,2,4-triazine, mono-
sodium salt] assay
51
without prior acidi
fi
cation of analyte.
Sample acidi
fi
cation in the presence of nitrite led to
underestimation of Fe(II) concentrations
31
and was therefore
avoided (see Supporting Information Figure S4). The assay was
calibrated using ferrous ammonium sulfate hexahydrate of
known concentration. Nitrite was determined colorimetrically
at 520 nm using sulfanilamide and N-1-napthylethylenediamine
dihydrochloride.
52
The chelator EDTA is incompatible with
this assay,
53
but none of the ligands used in this study interfere
with nitrite determination (Supporting Information Figure S5).
The assay was calibrated using a commercial nitrite standard
(Fluka Analytical TraceCERT). Samples for Fe(II) and nitrite
determination in microbial cultures were obtained with a sterile
disposable syringe
fl
ushed for 30 s with 20%CO
2
/80%N
2
. The
evolution of N
2
O in abiotic reactions was assessed qualitatively
by gas-chromatography using a Hewlett-Packard 5890 Series II
Plus Gas Chromatograph equipped with a Thermal Con-
ductivity Detector. Samples were injected onto a HP-MOLSIV
column (30m, 0.32 mm inner diameter (ID), 12
μ
m
fi
lm) and
eluted with helium at a
fl
ow rate of 10 mL/min using a
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temperature gradient from 35 to 240
°
C (4 min at 35
°
C, 35
°
C/min up to 140
°
C, 25
°
C/min up to 240
°
C). Formation of
the nitrosyliron-NTA complex (Fe(II)-NTA-NO) was assessed
qualitatively by monitoring its characteristic absorption peaks
(440 nm and 600 nm)
54,55
spectroscopically. Growth of
microbial cultures was followed by optical density at 600 nm
(OD
600
) in cultures without iron and at 700 nm (OD
700
)in
cultures with iron. This wavelength was used to decrease
distortion by Fe(III)-NTA, which absorbs strongly at 600 nm.
OD
700
underestimates optical density as compared to OD
600
.
Experimental Procedure.
Kinetic Fe(II) oxidation experi-
ments were conducted inside an anaerobic chamber (Coy
Laboratory Products, Inc.) equipped with palladium catalysts
for O
2
removal. The chamber contained
∼
3%H
2
/15% CO
2
/
82% N
2
and experiments were performed at 25
°
C using a
digital heat block. Samples were taken at varying time points
and analyzed immediately for Fe(II) and nitrite concentrations
using a BioTek Synergy 4 Microplate Reader housed inside the
chamber. Oxidation experiments were conducted in sterile basal
freshwater medium containing 2 mM Fe(II) and 2 mM NO
2
−
and were amended alternatively with 2 mM nitrilotriacetate
(NTA), 300 mg/L Pahokee Peat Humic Acid (PPHA,
International Humic Substances Society), 0.1, 0.5, or 2 mM
citrate, 300 mg/L PPHA + 2 mM citrate. PPHA was selected as
the humic acid of choice due to its high solubility and low
capacity for storing redox equivalents that could rereduce
Fe(III) and interfere with the experiment.
56
Control experi-
ments included incubations of Fe(II) with or without NTA in
the absence of nitrite or in the presence of 2 mM nitrate. pH
was measured at the beginning and conclusion of each
experiment.
Pseudogulbenkiania
sp. strain MAI was grown in triplicate at
30
°
C in the dark in freshwater medium amended with 0.5 mM
acetate, 4 mM Fe(II), and 8 mM NTA, and a headspace of
∼
3%H
2
/15% CO
2
/82% N
2
. Cultures were sampled regularly
for nitrite accumulation and Fe(II) oxidation.
Paracoccus denitri
fi
cans
was grown in triplicate at 30
°
C in the
dark in freshwater medium amended with 10 mM succinate and
20 mM nitrate and sampled regularly for nitrite accumulation.
Upon reaching a nitrite concentration of
∼
5 mM, 5 mL of each
culture was withdrawn and processed anaerobically as follows:
each withdrawn sample was divided in four. Two aliquots were
left unchanged while the other two were
fi
lter sterilized using a
0.2
μ
m syringe
fi
lter. All aliquots were spiked with
∼
5mM
Fe(II) and one of each set (one un
fi
ltered
P. denitri
fi
cans
and
one
fi
lter-sterilized aliquot) was further amended with 10 mM
citrate (all from 1 M stock solutions to avoid sample dilution).
No citrate was present in cultures prior to spiking. Aliquots
were incubated at 25
°
C for 4 h and sampled at regular intervals
as described in the kinetic Fe(II) oxidation experiments. The
remaining cultures were reincubated at 30
°
C for continued
monitoring of growth and nitrite accumulation.
Computation.
Nonlinear least-squares model
fi
ts and
parameter estimates for kinetic data were computed using the
statistical model analysis functionality provided by Wolfram
Mathematica
(v. 8.0). Fe(II) speciation in solution was
estimated using the Visual MINTEQ equilibrium speciation
model (v. 3.0) with stability constants provided by King
57
(Fe(II)-carbonate complexes) and the MINTEQ database
58
(all other Fe(II) species) and precomputed humic substance
properties based on the NICA-Donnan model.
59
Chemical
oxidation of Fe(II) with nitrite produced by MAI-1 was
modeled using Euler
’
s method to calculate stepwise solutions of
eq 5. Nitrite concentrations at each time step were calculated
by linear interpolation between closest measurement time
points. Chemical oxidation with concomitant biological NO
consumption was modeled by assuming complete NO removal
and subsequent lack of Fe(II)-NTA-NO complex formation.
■
RESULTS
The enrichment of fast growing anaerobic Fe(II) oxidizing
chemotrophs lead to the successful isolation of
Pseudogulben-
kiania
sp. strain MAI-1, a novel
β
-proteobacterium closely
related to the lithoautotrophic Fe(II) oxidizer
Pseudogulbenkia-
nia
sp. 2002
16,28
(96.9% 16S rRNA gene sequence similarity,
97.3% to the type strain
Pseudogulbenkiania sub
fl
ava
BP-5
60
).
MAI-1 has several key characteristics necessary for routine
genetic manipulation: the strain forms colonies on plates
(aerobically within 24 h), grows rapidly both aerobically and
anaerobically (overnight at 30
°
C), is sensitive to antibiotics,
and cryopreserves well. Most importantly, it displays the
desired phenotype: rapid nitrate dependent Fe(II) oxidation
(10 mM in less than 24 h, Supporting Information Figure S1)
in the presence of a chelator, nitrilotriacetate (NTA), that
prevents the formation of mineral precipitates (which could
obscure cells in automated assays) but does not serve as a
growth substrate for the organism (Supporting Information
Figure S2). When
fi
rst isolated, MAI-1 appeared to be an ideal
candidate for elucidating the genes required for nitrate
dependent Fe(II) oxidation. However, although Fe(II)-NTA
is highly stable in abiotic controls in the presence of nitrate
(Figure 1; Supporting Information Figure S1), adding Fe(II)-
NTA to
fi
lter-sterilized spent MAI-1 growth medium that had
Figure 1.
Ligands a
ff
ect the abiotic oxidation of Fe(II) by NO
2
−
. Error
bars omitted for clarity (relative standard deviation of Fe(II) and
NO
2
−
quantitation from all seven experiments estimated at 3% and
2%, respectively).
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accumulated substantial amounts of nitrite lead to rapid Fe(II)
oxidation with concomitant nitrite reduction (Supporting
Information Figure S3). The strain
’
s ability to use a wide
range of chelators as a carbon substrate (e.g., citrate, humic
acids, DTPA) and its inability to grow and oxidize free Fe
2+
(Supporting Information Figure S1) precluded avoiding NTA.
Additionally, MAI-1 cannot use alternate electron acceptors
(e.g., DMSO, TMAO, fumarate), requiring the use of nitrate
(and consequentially risking the production of nitrite) for
anaerobic culturing.
To quantitatively assess the e
ff
ect of Fe(II) chelation on
chemical oxidation by nitrite at circumneutral pH, we
conducted kinetic experiments with NTA as well as two
environmentally relevant Fe(II)-chelating ligands (citrate, CIT,
and Pahokee Peat Humic Acid, PPHA). Attempts to investigate
the e
ff
ect of Fe(II) chelation with the siderophore desferox-
amine (DFO) and the organic pollutant ethylenediaminete-
traacetate (EDTA) proved unsuccessful because of interference
with the ferrozine assay and the nitrite assay, respectively
(Supporting Information Figure S5). They were not pursued
further. Figure 1 shows the oxidation of Fe(II) and
concomitant reduction of NO
2
−
over the course of
∼
100 h
(4.2 days) for each condition. Nitrite-free controls without any
oxidant or amended with nitrate show little Fe(II) oxidation (a
maximum of 2% without oxidant, 5% with nitrate; see Table 1)
over the course of the experiment. This provided con
fi
dence
that O
2
contamination is not a signi
fi
cant source of error in our
experimental setup and suggested that nitrate is relatively
unreactive toward Fe(II) even in the presence of ligands (see
abiotic control in Supporting Information Figure S1). Nitrite in
the absence of iron shows high stability, con
fi
rming the
expected absence of nitrite self-decomposition that occurs at
acidic pH.
61
In the absence of any chelating moieties, less than
9% of Fe(II) is oxidized by nitrite within the
fi
rst 22 h. Similar
control experiments in previous reports have yielded Fe(II)
oxidation rates at
∼
8% Fe(II) within 10 h,
36
∼
9% within 20 h,
39
and
∼
1% within 24 h.
37
Complexation by both citrate and
NTA, however, leads to rapid depletion of Fe(II) and nitrite,
indicating that these organic ligands can accelerate Fe(II)
oxidation by nitrite (Figure 1).
Equipped with an estimate for the extent of chemical Fe(II)
oxidation by nitrite in the presence of NTA, we grew MAI-1 in
the presence of Fe(II)
−
NTA while closely monitoring the
accumulation of nitrite (Figure 2) to model the maximal abiotic
Fe(II) oxidation resulting from an abiotic reaction with nitrite.
Given the strong e
ff
ect of citrate on the chemical oxidation of
Fe(II) by nitrite, we also tested the hypothesis that abiotic
Fe(II) oxidation could be mediated by the biological
production of nitrite during denitri
fi
cation in general. For this
purpose,
P. denitri
fi
cans
, a model denitrifying microorganism,
was grown anaerobically on succinate and nitrate, such that
substantial quantities of nitrite accumulated during early
exponential growth (Supporting Information Figure S6).
After accumulation of
∼
5 mM nitrite,
fi
lter sterilized culture
medium as well as active cultures of
P. denitri
fi
cans
were
amended with
∼
5 mM Fe(II) with or without 10 mM citrate.
Figure 3 illustrates the resulting oxidation of Fe(II) over the
course of 4 h. Moderate oxidation occurred in the absence of
chelation both with
P. denitri
fi
cans
cultures as well as in spent
medium (up to 21% and 12%, respectively). Higher oxidation
rates for cultures are likely a consequence of continued
denitri
fi
cation by
P. denitri
fi
cans
, increasing the measured pool
of nitrite by up to 13%. However, the most striking feature is
the rapid depletion of Fe(II) and nitrite (up to 76% Fe(II),
38% NO
2
−
) observed with the addition of 10 mM citrate,
regardless of the presence of
P. denitri
fi
cans
(Table 2, Figure 3).
■
DISCUSSION
Reaction Mechanism and Kinetics.
Understanding the
kinetics of Fe(II) oxidation in the presence of ligands provides
the tools for predicting the potential e
ff
ects of ligand-enhanced
Fe(II) oxidation in microbial systems. The total consumption
of Fe(II) and nitrite (Table 1) suggests that Fe(II) oxidation by
nitrite proceeds with 2:1 Fe(II)/NO
2
−
stoichiometry regardless
Table 1. Summary of Kinetic Fe(II) Oxidation Experiments by Nitrite
a
reactant changes within
∼
100 h
Fe(II) oxidation
NO
2
−
reduction
Δ
Fe(II)
Δ
NO
2
−
Δ
Fe(II)/
Δ
NO
2
−
model
k
app
(LCI;UCI
d
)
model
k
app
(LCI;UCI
d
)
[
μ
M] (%
b
)[
μ
M] (%
b
)(
±
1
σ
)
c
R
2
[10
−
3
M
−
1
s
−
1
]
R
2
[10
−
3
M
−
1
s
−
1
]
Controls
2mMNO
2
−
only
−
3 (0%)
2 mM Fe(II) only
−
3 (0%)
+2 mM NTA
−
35 (2%)
+2 mM NO
3
−
−
91 (5%)
+2 mM NTA + 2 mM NO
3
−
−
64 (3%)
Kinetically Unresolved
2 mM Fe(II) + 2 mM NO
2
−
−
963 (48%)
−
478 (24%)
2.0
±
0.3
+0.1 mM citrate
−
933 (50%)
−
480 (24%)
1.9
±
0.2
+300 mg/L PPHA
−
592 (30%)
−
303 (16%)
2.0
±
0.4
Second-Order Kinetics
+0.5 mM citrate
−
1281 (66%)
−
686 (34%)
1.9
±
0.2
0.9995
0.98 (0.92;1.04)
0.9995
1.04 (0.88;1.19)
+2 mM citrate
−
1883 (96%)
−
945 (47%)
2.0
±
0.1
0.9979
4.67 (4.18;5.17)
0.9992
4.31 (3.57;5.06)
+2 mM citrate +300 mg/L PPHA
−
1773 (90%)
−
931 (48%)
1.9
±
0.1
0.9963
3.31 (2.85;3.78)
0.9997
3.59 (3.24;3.93)
+2 mM NTA
−
1119 (55%)
−
1065 (54%)
1.1
±
0.1
0.9987
6.66 (5.19;8.13)
0.9993
6.11 (5.15;7.07)
a
The rate constant
k
app
is reported for reactions that are described well by second-order kinetics. The experiments were conducted at 25
°
C, pH 6.9
to 7.1. The p-values for the model parameter
k
app
are <0.001 for all conditions.
R
2
is the adjusted regression coe
ffi
cient for the least-squares
fi
t.
b
Percentage change of [Fe(II)] and [NO
2
−
] relative to starting concentrations.
c
Derived by error propagation from measurement errors (relative
standard deviation of Fe(II) and NO
2
−
quantitation during experiments estimated at 3% and 2% respectively).
d
Lower (LCI) and upper (UCI) 95%
con
fi
dence interval of parameter derived from model
fi
t.
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of complexation (no ligand, PPHA, citrate), with the notable
exception of NTA, which appears to deplete Fe(II) and NO
2
−
in a 1:1 ratio. The 2:1 stoichiometry is in agreement with
literature reports that the predominant product of nitrite
reduction at pH regimes between 6 and 8 is N
2
O,
22,33,36,37,62
according to the following representative net reaction:
++→++
+−++
k
4Fe
2NO
6H
4Fe
N O 3H
O
1
2
2
3
22
(1)
where Fe
2+
can be unbound Fe
2+
or a ligand-bound Fe(II)-L
species, and Fe
3+
can be ligand-bound Fe(III)-L or contained
within an (oxy)hydroxide mineral (e.g., FeOOH). This net
reaction likely comprises a number of elementary reaction
steps; we consider the following three to contextualize our
observations:
++→++
+−++
k
(slow)
Fe
NO
2H
Fe
NO H
O
2
2
2
3
aq
2
(2)
+→ −
+
+
k
(fast) Fe
NO
(Fe(II) NO)
3
2
aq
2
(3)
−+→++
++
+
k
(fast)
(Fe(II) NO)
H
Fe
1
2
NO
1
2
H
O
4
23
22
(4)
Equations 3
63
and 4
64
proceed rapidly at circumneutral pH,
with eq 2 being the rate limiting step (
k
1
≈
k
2
). Accordingly,
the reaction consumes 2 Fe(II) for every NO
2
−
, except in the
case of NTA. Both citrate and NTA complexes with ferrous
iron can bind nitric oxide such that the following reactions can
occur in competition with eq 3:
−+→ −−
−
−
k
(Fe(II) CIT) NO
(Fe(II) CIT NO)
5aq
(5)
−+→−−
−
−
k
(Fe(II) NTA) NO
(Fe(II) NTA NO)
6
aq
([6])
Figure 2.
Fe(II) oxidation by
Pseudogulbenkiania
sp. strain MAI-1
during anaerobic growth with nitrate. Nitrite accumulation during
growth depicted in top panel, concomitant Fe(II) oxidation in middle
panel, modeled abiotic Fe(II) oxidation in bottom panel (see Materials
and Methods for details on computation). Solid and dashed lines
indicate Fe(II) oxidation without/with biological NO consumption,
respectively. Dotted line indicates Fe(II) oxidation with 6
×
higher rate
constant and NO consumption. Model range for three biological
replicates shaded in gray. Vertical line indicates time point addressed
in text. Experiment conducted in biological triplicates (solid markers)
and with abiotic control (empty circles,
○
). All data are shown.
Figure 3.
Fe(II) oxidation in
P. denitri
fi
cans
cultures and
fi
lter-
sterilized spent medium. Fe(II) concentrations shown as solid lines,
NO
2
−
concentrations as dashed lines. Samples are drawn from
triplicate cultures (Supporting Information Figure S6) after accumu-
lation of
∼
5mMNO
2
−
and spiked with Fe(II)
±
citrate at 0 h. All
data are shown.
Table 2. Summary of Kinetic Fe(II) Oxidation Experiments
by Nitrite in
P. denitri
fi
cans
Cultures and Spent Medium
a
reactant changes
within
∼
4 h
Fe(II) oxidation
NO
2
−
reduction
Δ
F
e(II)
Δ
NO
2
−
model
k
app
(LCI;UCI
c
) model
k
app
(LCI;UCI
c
)
[mM]
(%
b
)
[mM]
(%
b
)
R
2
[10
3
M
−
1
s
−
1
]
R
2
[10
3
M
−
1
s
−
1
]
P. denitri
fi
cans
#
1
−
3.7
(76%)
−
1.9
(36%)
0.9991 12 (11;14) 0.9991 11 (8;15)
#
2
−
3.3
(73%)
−
1.8
(36%)
0.9984 11 (9;13)
0.9996 10 (8;12)
#
3
−
3.2
(69%)
−
1.8
(38%)
0.9977 10 (7;13)
0.9985 11 (6;17)
Filter Sterilized
#
1
−
3.6
(73%)
−
1.8
(33%)
0.9990 11 (9;12)
0.9981 10 (6;15)
#
2
−
3.2
(71%)
−
1.7
(34%)
0.9985 11 (9;13)
0.9995 10 (8;12)
#
3
−
3.2
(65%)
−
1.7
(37%)
0.9983 9 (7;11)
0.9988 12 (7;17)
a
The experiment was conducted at 25
°
C. P-values for the model
parameter
k
2
are <0.01.
R
2
is the adjusted regression coe
ffi
cient for the
least-squares
fi
t.
b
Percentage change of [Fe(II)] and [NO
2
−
] relative
to starting concentrations.
c
Lower (LCI) and upper (UCI) 95%
con
fi
dence interval of parameter derived from model
fi
t.
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However, Fe(II)-NTA forms a considerably stronger complex
with NO (
k
6
≈
2.1
×
10
7
M
−
1
s
−
1
,
K
eq
=10
6.26
)
54,65,66
than
Fe(II)-citrate (
k
5
≈
4.4
×
10
5
M
−
1
s
−
1
,
K
eq
=10
2.83
)
66
or Fe
2+
alone (
k
3
≈
6.2
×
10
5
M
−
1
s
−
1
,
K
eq
=10
2.65
),
63
potentially
preventing eq 4 from proceeding. For example, if 100
μ
M
Fe(II) reacted with 100
μ
MNO
2
−
to form NO in the presence
of 2 mM NTA, more than 99.98% of the produced NO would
form the highly stable Fe(II)-NTA-NO complex. The 1:1
stoichiometry of Fe(II) oxidation by nitrite observed in the
presence of NTA is likely a consequence of this stable Fe(II)
−
NTA
−
NO complex formation. As expected, we con
fi
rmed
evolution of N
2
O during Fe(II) oxidation by nitrite by gas
chromatography in the presence of citrate, but no N
2
O formed
in the presence of NTA (Supporting Information Figure S8);
the formation of the Fe(II)
−
NTA
−
NO complex could be
observed instead (Supporting Information Figure S9).
Based on the rate-limiting, Fe(II) and NO
2
−
dependent
fi
rst
reaction step (eq 2), a plausible scheme for the overall reaction
kinetics is a second-order rate expression with overall rate
constant
k
app
in analogy with oxidation of Fe(II) and Mn(II) by
O
2
57,67
=−
−
tk
dFe(II)/d
2 [Fe(II)][NO ]
app
2
(7)
=−
−−
tk
dNO /d
[Fe(II)][NO
]
2app 2
(8)
where Fe(II) comprises the total pool of ferrous iron (free Fe
2+
as well as all complexed Fe(II)). Given the equimolarity of
initial total Fe(II) and NO
2
−
in our experimental setup, we
integrate eqs 7 and 8 to yield the following decay equations
(see the Supporting Information for details):
=
−+
t
Fe(II)( )
Fe(II)
12e
kt
0
Fe(II)
0app
(9)
=
−+
−
−
−
−
t
NO ( )
NO e
12e
kt
kt
2
2
0
NO
NO
2
0
app
2
0
app
(10)
Least-squares
fi
ts of eqs 9 and 10 to our experimental results
for Fe(II) and NO
2
−
depletion provide two separate estimates
of the overall rate constant
k
app
for each condition (Tables 1
and 2). Reactions without a ligand and with low citrate or
PPHA are better described by a linear least-squares
fi
t
(apparent zero-order kinetics) and are therefore considered
kinetically unresolved (no
k
app
determined). Elementary
reaction steps and kinetic constraints for these conditions
cannot be deduced from our observations, and it remains
unclear why the reactions appear to be zero-order. Oxidation in
these conditions likely proceeds as a consequence of ferric
(oxy)hydroxide precipitation (observed visually) and subse-
quent heterogeneous autocatalysis as reported by Tai and
Dempsey (2009).
37
Apparent zero-order kinetics could re
fl
ect
the complex balance between the generation of catalytic
mineral surfaces and depletion of dissolved Fe(II) and nitrite.
At higher concentrations of citrate and NTA, the reactions
remained homogeneous and are in agreement with a second-
order kinetic interpretation of our data (Tables 1 and 2 and
Supporting Information Figure S7). Rate constants derived
from Fe(II) oxidation and nitrite reduction agree well within
their 95% con
fi
dence intervals, lending further credence to the
model. The pH remained close to 7.0 in all conditions, with an
average change of 0.1 by the end of the experiment (Supporting
Information Table S1), suggesting that the presence of the
ligands, rather than
fl
uctuations in pH are responsible for the
observed di
ff
erences in reaction kinetics. The reaction
progression observed in the presence of PPHA suggests that
chelation of Fe(II) by the humic acid moieties (10% of the
initial Fe(II) pool is organically complexed) has little to no
e
ff
ect on the kinetics of iron oxidation (see Figure 1, PPHA and
CIT + PPHA). Rather than accelerating Fe(II) oxidation,
PPHA appears to have a slight retarding e
ff
ect. In contrast to
experiments without a ligand, PPHA is likely to impede iron
oxide formation and autocatalysis as a result of its high a
ffi
nity
for Fe(III). In combination with citrate, PPHA leads to
diminished formation of the Fe(II)-citrate complex (Support-
ing Information Table S2), which appears to reduce the overall
reaction rate (Table 1).
Additional information for predicting the contribution of
chemical Fe(II) oxidation, especially in well-de
fi
ned laboratory
systems, can be gained from identifying the reactive species. In
analogy to Fe(II) and Mn(II) oxidation by O
2
, the overall rate
constant
k
app
observed in our experiments can likely be
explained in terms of the weighted sum of the oxidation rates of
individual Fe(II) species
57,67
k
app
=
∑
k
i
α
i
where
α
i
is the
fraction of each Fe(II) species in solution and
k
i
the species-
speci
fi
c second-order rate constant for oxidation by nitrite. A
comparison of
k
app
with the extent of Fe(II) complexation for
each experimental condition (Figure 4; Supporting Information
Table S2) suggests that the Fe(II)-L complex is involved in
accelerating Fe(II) oxidation, although the e
ff
ect is ligand-
speci
fi
c (no e
ff
ect for PPHA, variable magnitude for citrate and
NTA). The observed reaction rates at low species fractions of
Fe(II)-L (<20%) suggest the existence of other Fe(II) species
with appreciable nitrite-dependent oxidation rates. We
speculate that the carbonate species Fe(II)
−
CO
3
−
OH
−
and
Fe(II)
−
(CO
3
)
2
2
−
(Supporting Information Table S2) could
provide such reactive species in analogy to their role in Fe(II)
oxidation by molecular oxygen.
57
However, the precise
mechanism and species-speci
fi
c reaction rates
k
i
for the
Figure 4.
Rate constants increase with increasing degree of Fe(II)
complexation. Second-order rate constants for oxidation experiments
in the presence of citrate (black symbols) and NTA (gray symbols) are
plotted against the degree of Fe(II) complexation by citrate/NTA.
Rate constants derived from [Fe(II)] depicted as circles (
○
),
constants derived from [NO
2
−
] as squares (
□
). Error bars indicate
95% con
fi
dence intervals (Tables 1 and 2). Details on speciation can
be found in Supporting Information Table S1. Larger con
fi
dence
intervals for data reported in Table 2 are a consequence of reduced
temporal resolution and greater deviation from the assumption that
initial Fe(II) and NO
2
−
concentrations are equimolar.
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observed oxidation of Fe(II) by nitrite are beyond the scope of
this report and await further study. Due to the uncertainty
surrounding the reactive species involved, we recommend
caution in applying the rate constants derived in Tables 1 and 2
to aqueous environments with widely di
ff
ering Fe(II) complex-
ation, pH, or ionic strength.
Biological Fe(II) Oxidation by
Pseudobulkeniania
sp.
Strain MAI-1.
Using the kinetic rate constants derived for the
oxidation of Fe(II) by nitrite in the presence of NTA with the
nitrite accumulation measured in culture of MAI-1 (Figure 2),
we modeled the purely abiotic Fe(II) oxidation that would
result from the interaction of Fe(II) with the accumulated
nitrite (Figure 2, bottom), assuming the presence of cell
Table 3. Maximal Rates of Fe(II) Oxidation Reported for Various Anaerobic Processes at Circumneutral pH (25
−
30
°
C, Except
Where Otherwise Indicated)
experimental conditions
max. rates
pH
bu
ff
er
Fe(II)
nitrite
nitrate
Δ
Fe(II)
[
μ
M/h]
reference
Chemical (Abiotic)
+30 mg/L lepidocrocite (
γ
-FeOOH)
7.5 autotitration
0.2 mM
0.2 mM
−
7
36, Figure 5
+30 mg/L lepidocrocite (
γ
-FeOOH)
8.5 autotitration
0.2 mM
0.2 mM
−
40
36, Figure 5
Fe(II) as siderite (10 g/L
∼
80 mM)
6
MES/PIPES/
HEPES
10 g/L
4.6 mM
−
265
39, Figure 5
Fe(II) as siderite (10 g/L
∼
80 mM)
6.5 MES/PIPES/
HEPES
10 g/L
4.6 mM
−
169
39, Figure 5
Fe(II) as siderite (10 g/L
∼
80 mM)
7.9 MES/PIPES/
HEPES
10 g/L
4.6 mM
−
140
39, Figure 5
+2.5 mM Fe(II) as HFO, 64
μ
M average solid-bound
Fe(II)
6.8 PIPES
0.38 mM 0.38 mM
−
158
37, Table 1,
#
6
+17.5 mM Fe(III) as HFO, 188
μ
M average solid-
bound Fe(II)
6.8 PIPES
0.34 mM 0.32 mM
−
301
37, Table 1,
#
11
F(II) as green rust
8.25 autotitration
10.81 mM
14.2 mM
−
139
42, Table 1
+2 mM NTA
7
bicarbonate
2 mM
2 mM
−
192
this study,
Table 1
+2 mM CIT
7
bicarbonate
2 mM
2 mM
−
134
this study,
Table 1
+10 mM CIT,
P. denitri
fi
cans
spent medium
7
bicarbonate
5 mM
5 mM
−
1695
this study,
Table 2
+10 mM CIT,
P. denitri
fi
cans
culture
7
bicarbonate
5 mM
5 mM
−
1910
this study,
Table 2
Mixed (Chemical + Biological)
D. frappieri
strain G, Fe(II) complexed by
10 mM NTA
∼
7
bicarbonate
4.8 mM
1.4 mM
2.5 mM
−
294
20, Figure 5
D. frappieri
strain G, Fe(II) as smectite
∼
7
bicarbonate
3 mM
1.4 mM
5 mM
−
175
20, Figure 6
Pseudogulbenkiania
sp. MAI-1, Fe(II)-NTA
7
bicarbonate
4 mM
5 mM
10 mM
−
360
this study,
Figure 2
Chemotrophic
enrichment culture, +1 mM acetate
7
bicarbonate
10 mM
?
3 mM
−
106
4, Figure 1
enrichment culture containing
Sideroxydans
species
6.8 bicarbonate
10 mM
?
4 mM
−
156
29, Figure 1a
Pseudogulbenkiania
strain 2002
6.8 bicarbonate
10 mM
?
2.2 mM
−
74
16, Figure 4
strain HidR2, +1 mM acetate
6.7 bicarbonate
6 mM
<30
μ
M5mM
−
66
14, Figure 2
Ferroglobus placidus
, 85C
7
bicarbonate
2 mM
up to
550
μ
M
0.64 mM
−
173
5, Figure 4
cell suspension of
D. suillum
, grown on acetate +
nitrate
6.8 bicarbonate
10 mM
?
10 mM
−
4700
12, Figure 3a
Paracoccus ferrooxidans
, +25 mM EDTA,
+1 mM ethanol
7
bicarbonate
25 mM
?
5 mM
−
1600
13, Figure 3a
Acidovorax
sp. strain BoFeN1, +2 mM acetate
6.8 bicarbonate
2.5 mM
<1 mM
5 mM
−
48
15, Figure 2
Acidovorax
sp. strain BoFeN1, +5 mM acetate
7
bicarbonate
10 mM
0 mM
10 mM
−
240
30, Figure 1a
Acidovorax
sp. strain 2AN, +1.6 mM acetate
6.85 bicarbonate
8.3 mM
up to 1 mM 5 mM
−
158
24, Figure 2a
Acidovorax
sp. strain 2AN, + 4 mM EDTA,
+1.2 mM ethanol
7
PIPES
4 mM
?
5 mM
−
970
49, Figure 3c
Dechloromonas
sp. UWNR4, + 4 mM EDTA,
+1.2 mM ethanol
7
PIPES
4 mM
?
5 mM
−
950
49, Figure 3d
lake sediment slurry
∼
7
bicarbonate
1.4 mM
0.01 mM
1 mM
−
6
69, Figure 3
Phototrophic
Rhodopseudomonas palustris
strain TIE-1, + 0.2 mM
citrate
7
bicarbonate
4.5 mM
−
21
3, Figure 2
Rhodobacter capsulatus
strain SB1003,
+0.2 mM citrate
7
bicarbonate
0.1 mM
−
34
3, Figure 4
Rhodobacter capsulatus
strain SB1003, +1 mg/L HA
7
bicarbonate
0.1 mM
−
50
70, Figure 4
Rhodobacter capsulatus
strain SB1003, +0.2 mM NTA
7
bicarbonate
0.1 mM
−
112
70, Figure 4
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surfaces
22
to have negligible e
ff
ects on purely chemical
oxidation. Even if we conservatively assume the upper 95%
con
fi
dence interval for the rate constant (8.13 M
−
1
s
−
1
; see
Table 1) and that produced NO is biologically consumed (thus
leaving more Fe(II) free to react by preventing formation of the
highly stable Fe(II)-NTA-NO complex), abiotic oxidation
would maximally account for
∼
30%/35% (solid vs dashed
curve) of the observed Fe(II) oxidation after 28 h (time point
indicated by vertical line in Figure 2). In fact, a 6
×
higher rate
constant (combined with biological consumption of any
produced NO) would be required to attribute observed Fe(II)
oxidation to purely chemical processes (Figure 2, dotted
model). Based on the kinetic quanti
fi
cation of chemical
oxidation of Fe(II), it thus becomes evident that
Pseudogulben-
kiania
sp. MAI-1 can directly oxidize Fe(II), establishing the
organism as a novel neutrophilic nitrate-dependent chemotroph
with unambiguous biological Fe(II)-oxidizing activity. The
potential to easily genetically manipulate this strain makes it a
good candidate for elucidating the machinery involved in
biological Fe(II) oxidation. Whether the biological component
of Fe(II) oxidation in MAI-1 occurs via a dedicated enzyme
system or via nonspeci
fi
creactionswithredoxactive
components of the cell, such as periplasmic thiols or
components of the electron transport chain,
25,26
is a question
that could be addressed in the future.
Chemical vs Biological Fe(II) Oxidation in Laboratory
and Environmental Studies.
Given the aforementioned
di
ffi
culty in discriminating between chemical and biological
contributions to anaerobic Fe(II) oxidation in many systems, it
can be informative to compare Fe(II) oxidation rates observed
in a variety of environmental and laboratory settings. Table 3
provides an overview of the maximal Fe(II) oxidation rates
reported in a number of publications on chemical and biological
Fe(II) oxidation in nitrite/nitrate rich anoxic environments at
circumneutral pH. Several observations are particularly note-
worthy:
(i) The majority of observed maximal rates of chemical and
biological Fe(II) oxidation fall within a similar range of
values (
∼
10
−
100
μ
M/h), highlighting the likely
competition and co-occurrence of chemical and bio-
logical processes involved in the coupled biogeochemical
cycling of iron and nitrogen. Moreover, because nitrite is
produced and often accumulates during the microbial
denitri
fi
cation process, they are intrinsically coupled.
This biologically induced chemical oxidation of iron (via
the microbial production of nitrite) in organic rich
environments such as soils and wetlands is likely to
contribute signi
fi
cantly to the cycling of iron and
immobilization of metal contaminants and organic
pollutants on iron (oxy)hydroxides. High oxidation
rates reported for environmental samples with mixed
contributions from biological and chemical catalysis
20
illustrate the interplay of these processes and call for
caution in interpreting an observed e
ff
ect to stem from
solely one or the other mechanism.
(ii) In the case of mineral accelerated Fe(II) oxidation, the
presence of amorphous hydrous ferric oxide (HFO/
ferrihydrite)
9,31,37
and green rust
42
appears to cause the
most signi
fi
cant acceleration of Fe(II) oxidation (see
Table S3 for additional detail on rate constants derived
for mineral catalysis). This e
ff
ect is likely to be highly
relevant in natural settings where poorly crystalline iron
oxides are ubiquitous. However, it is also important to
consider this e
ff
ect in laboratory studies where iron
oxides precipitate over the course of an experiment and
can provide catalytic surfaces for chemodenitri
fi
cation as
suggested previously.
23
−
25
(iii) In the case of ligand-enhanced Fe(II) oxidation by
nitrite, the absence of a major e
ff
ect of the humic acid
representative PPHA and low environmental abundance
of the anthropogenic ligand NTA (maximal levels of 10
−
100 nM in aqueous systems),
1
suggests that citrate
(detected in soil solutions in appreciable quantities,
∼
100
μ
M range)
68
is likely to be the only ligand investigated in
this study that could be relevant in natural systems. In
laboratory studies of iron oxidizing microorganisms in
the presence of citrate or NTA, the ligands
’
e
ff
ect on
oxidation kinetics is a crucial aspect of Fe(II) depletion
that cannot be disregarded. This is particularly clear from
the experiment reported in Figure 3 that con
fi
rms ligand-
enhanced chemical oxidation of Fe(II) by nitrite can be
an important side e
ff
ect of microbial denitri
fi
cation.
Here, chemical Fe(II) oxidation could be mistaken for
direct biological catalysis by
P. denitri
fi
cans
; while direct
catalysis may indeed be at play, it would simply be
challenging to unambiguously identify without appro-
priate controls. In conclusion, this study serves as a
reminder of the complex interplay between direct and
indirect biological e
ff
ects involving metal transforma-
tions. In the case of denitrifying microorganisms, the
extent to which these di
ff
erent processes catalyze Fe(II)
oxidation likely depends on the precise culturing
conditions and must be evaluated on a case-by-case basis.
■
ASSOCIATED CONTENT
*
S
Supporting Information
Derivation of reaction equations and additional tables and
fi
gures as described in the text. This material is available free of
charge via the Internet at http://pubs.acs.org.
■
AUTHOR INFORMATION
Corresponding Author
*
Phone: 626-395-3543. Fax: 626-395-4135. E-mail: dkn@
caltech.edu.
Notes
The authors declare no competing
fi
nancial interest.
■
ACKNOWLEDGMENTS
We thank Jim Morgan for many insightful conversations and
inspiring S.H.K. to pursue this project, Sean Crowe, CarriAyne
Jones, Arne Sturm, Sulung Nomosatryo, David Fowle, and Don
Can
fi
eld for sample acquisition and
fi
eldwork in Indonesia,
Nathan Dalleska and the Caltech Environmental Analysis
Center for instrumentation that bene
fi
ted this project, Andreas
Kappler, Nicole Klu
̈
glein, and Jay Labinger for helpful
discussions, members of the Newman Lab and the anonymous
reviewers for constructive criticism that improved the manu-
script. This work was supported by grants to D.K.N from the
Dreyfus Foundation and the Howard Hughes Medical Institute
(HHMI). D.K.N. is an HHMI Investigator. S.H.K. is an HHMI
International Student Research Fellow.
Environmental Science & Technology
Article
dx.doi.org/10.1021/es3049459
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2013, 47, 2602
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|
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2013, 47, 2602
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