17 research outputs found
The Confounding Effect of Nitrite on N<sub>2</sub>O Production by an Enriched Ammonia-Oxidizing Culture
The effect of nitrite
(NO<sub>2</sub><sup>ā</sup>) on the
nitrous oxide (N<sub>2</sub>O) production rate of an enriched ammonia-oxidizing
bacteria (AOB) culture was characterized over a concentration range
of 0ā1000 mg N/L. The AOB culture was enriched in a nitritation
system fed with synthetic anaerobic digester liquor. The N<sub>2</sub>O production rate was highest at NO<sub>2</sub><sup>ā</sup> concentrations of less than 50 mg N/L. At dissolved oxygen (DO)
concentration of 0.55 mg O<sub>2</sub>/L, further increases in NO<sub>2</sub><sup>ā</sup> concentration from 50 to 500 mg N/L resulted
in a gradual decrease in N<sub>2</sub>O production rate, which maintained
at its lowest level of 0.20 mg N<sub>2</sub>OāN/h/g VSS in
the NO<sub>2</sub><sup>ā</sup> concentration range of 500ā1000
mg N/L. The observed NO<sub>2</sub><sup>ā</sup>-induced decrease
in N<sub>2</sub>O production was even more apparent at increased DO
concentration. At DO concentrations of 1.30 and 2.30 mg O<sub>2</sub>/L, the lowest N<sub>2</sub>O production rate (0.25 mg N<sub>2</sub>OāN/h/g VSS) was attained at a lower NO<sub>2</sub><sup>ā</sup> concentration of 200ā250 mg N/L. These observations suggest
that N<sub>2</sub>O production by the culture is diminished by both
high NO<sub>2</sub><sup>ā</sup> and high DO concentrations.
Collectively, the findings show that exceedingly high NO<sub>2</sub><sup>ā</sup> concentrations in nitritation systems could lead
to decreased N<sub>2</sub>O production. Further studies are required
to determine the extent to which the same response to NO<sub>2</sub><sup>ā</sup> is observed across different AOB cultures
Effect of H<sub>2</sub>S on N<sub>2</sub>O Reduction and Accumulation during Denitrification by Methanol Utilizing Denitrifiers
Sulfide
is produced in sewer networks, and previous studies suggest
that sulfide in sewage could alter the activity of heterotrophic denitrification
and lead to N<sub>2</sub>O accumulation during biological wastewater
treatment. However, the details of this phenomenon are poorly understood.
In this study, the potential inhibitory effects of sulfide on nitrate,
nitrite, and N<sub>2</sub>O reduction were assessed with a methanol-utilizing
denitrifying culture both prior to and after its exposure and adaptation
to sulfide. Hydrogen sulfide was found to be strongly inhibitory to
N<sub>2</sub>O reduction, with 50% inhibition observed at H<sub>2</sub>S concentrations of 0.04 mg H<sub>2</sub>SāS/L and 0.1 mg
H<sub>2</sub>SāS/L for the unadapted and adapted cultures,
respectively. In comparison, both nitrate and nitrite reduction was
more tolerant to H<sub>2</sub>S. A 50% inhibition of nitrite reduction
was observed at approximately 2.0 mg H<sub>2</sub>SāS/L for
both unadapted and adapted cultures, while no inhibition of nitrate
reduction occurred at the highest H<sub>2</sub>S concentrations applied
(2.0 mg H<sub>2</sub>SāS/L) to either culture. N<sub>2</sub>O accumulation was observed during nitrate and nitrite reduction
by the adapted culture when H<sub>2</sub>S concentrations were above
0.5 and 0.2 mg H<sub>2</sub>SāS/L, respectively. Additionally,
we reveal that hydrogen sulfide (H<sub>2</sub>S), rather than sulfide,
was likely the true inhibitor of N<sub>2</sub>O reduction, and the
inhibitory effect was reversible. These findings suggest that sulfide
management in sewers could potentially have a significant impact on
N<sub>2</sub>O emission from wastewater treatment plants
Reducing N<sub>2</sub>O Emission from a Domestic-Strength Nitrifying Culture by Free Nitrous Acid-Based Sludge Treatment
An increase of nitrite
in the domestic-strength range is generally
recognized to stimulate nitrous oxide (N<sub>2</sub>O) production
by ammonia-oxidizing bacteria (AOB). It was found in this study, however,
that N<sub>2</sub>O emission from a mainstream nitritation system
(cyclic nitrite = 25ā45 mg of N/L) that was established by
free nitrous acid (FNA)-based sludge treatment was not higher but
much lower than that from the initial nitrifying system with full
conversion of NH<sub>4</sub><sup>+</sup>-N to NO<sub>3</sub><sup>ā</sup>-N. Under dissolved oxygen (DO) levels of 2.5ā3.0 mg/L, N<sub>2</sub>O emission from the nitritation stage was 76% lower than that
from the initial stage. Even when the DO level was reduced to 0.3ā0.8
mg/L, N<sub>2</sub>O emission from the nitritation stage was still
40% lower. An investigation of the mechanism showed that FNA treatment
caused a shift of the stimulation threshold of nitrite on N<sub>2</sub>O emission. At the nitritation stage, the maximal N<sub>2</sub>O
emission factor occurred at ā¼16 mg of N/(L of nitrite). However,
it increased with increasing nitrite in the range of 0ā56
mg of N/L at the initial stage. FNA treatment decreased the biomass-specific
N<sub>2</sub>O production rate, suggesting that the enzymes relevant
to nitrifier denitrification were inhibited. Microbial analysis revealed
that FNA treatment decreased the microbial community diversity but
increased the abundances of AOB and denitrifiers
Molecular Dynamics Unlocks Atomic Level Self-Assembly of the Exopolysaccharide Matrix of Water-Treatment Granular Biofilms
Biofilm formation, in which bacteria are embedded within
an extracellular
matrix, is the default form of microbial life in most natural and
engineered habitats. In this work, atomistic molecular dynamics simulations
were employed to examine the self-assembly of the polysaccharide Granulan
to provide insight into the molecular interactions that lead to biofilm
formation. Granulan is a major gel forming matrix component of granular
microbial biofilms found in used-water treatment systems. Molecular
dynamics simulations showed that Granulan forms an antiparallel double
helix stabilized by complementary hydrogen bonds between the Ī²-glucosamine
of one strand and the <i>N</i>-acetyl-Ī²-galactosamineā2-acetoamido-2-deoxy-Ī±-galactopyranuronic
pair of the other in both the presence and absence of Ca<sup>2+</sup>. It is shown that Ca<sup>2+</sup> binds primarily to the carboxyl
group of the terminal hexuronic acid of the sugar branch and that
interactions between branches mediated by Ca<sup>2+</sup> suggest
a possible mechanism for strengthening gels by facilitating interhelical
bridging
Mathematical Modeling of Nitrous Oxide (N<sub>2</sub>O) Emissions from Full-Scale Wastewater Treatment Plants
Mathematical
modeling of N<sub>2</sub>O emissions is of great importance
toward understanding the whole environmental impact of wastewater
treatment systems. However, information on modeling of N<sub>2</sub>O emissions from full-scale wastewater treatment plants (WWTP) is
still sparse. In this work, a mathematical model based on currently
known or hypothesized metabolic pathways for N<sub>2</sub>O productions
by heterotrophic denitrifiers and ammonia-oxidizing bacteria (AOB)
is developed and calibrated to describe the N<sub>2</sub>O emissions
from full-scale WWTPs. The model described well the dynamic ammonium,
nitrite, nitrate, dissolved oxygen (DO) and N<sub>2</sub>O data collected
from both an open oxidation ditch (OD) system with surface aerators
and a sequencing batch reactor (SBR) system with bubbling aeration.
The obtained kinetic parameters for N<sub>2</sub>O production are
found to be reasonable as the 95% confidence regions of the estimates
are all small with mean values approximately at the center. The model
is further validated with independent data sets collected from the
same two WWTPs. This is the first time that mathematical modeling
of N<sub>2</sub>O emissions is conducted successfully for full-scale
WWTPs. While clearly showing that the NH<sub>2</sub>OH related pathways
could well explain N<sub>2</sub>O production and emission in the two
full-scale plants studied, the modeling results do not prove the dominance
of the NH<sub>2</sub>OH pathways in these plants, nor rule out the
possibility of AOB denitrification being a potentially dominating
pathway in other WWTPs that are designed or operated differently
Modeling of Nitrous Oxide Production by Autotrophic Ammonia-Oxidizing Bacteria with Multiple Production Pathways
Autotrophic
ammonia oxidizing bacteria (AOB) have been recognized
as a major contributor to N<sub>2</sub>O production in wastewater
treatment systems. However, so far N<sub>2</sub>O models have been
proposed based on a single N<sub>2</sub>O production pathway by AOB,
and there is still a lack of effective approach for the integration
of these models. In this work, an integrated mathematical model that
considers multiple production pathways is developed to describe N<sub>2</sub>O production by AOB. The pathways considered include the nitrifier
denitrification pathway (N<sub>2</sub>O as the final product of AOB
denitrification with NO<sub>2</sub><sup>ā</sup> as the terminal
electron acceptor) and the hydroxylamine (NH<sub>2</sub>OH) pathway
(N<sub>2</sub>O as a byproduct of incomplete oxidation of NH<sub>2</sub>OH to NO<sub>2</sub><sup>ā</sup>). In this model, the oxidation
and reduction processes are modeled separately, with intracellular
electron carriers introduced to link the two types of processes. The
model is calibrated and validated using experimental data obtained
with two independent nitrifying cultures. The model satisfactorily
describes the N<sub>2</sub>O data from both systems. The model also
predicts shifts of the dominating pathway at various dissolved oxygen
(DO) and nitrite levels, consistent with previous hypotheses. This
unified model is expected to enhance our ability to predict N<sub>2</sub>O production by AOB in wastewater treatment systems under
varying operational conditions
Free Nitrous Acid (FNA)-Based Pretreatment Enhances Methane Production from Waste Activated Sludge
Anaerobic
digestion of waste activated sludge (WAS) is currently
enjoying renewed interest due to the potential for methane production.
However, methane production is often limited by the slow hydrolysis
rate and/or poor methane potential of WAS. This study presents a novel
pretreatment strategy based on free nitrous acid (FNA or HNO<sub>2</sub>) to enhance methane production from WAS. Pretreatment of WAS for
24 h at FNA concentrations up to 2.13 mg N/L substantially enhanced
WAS solubilization, with the highest solubilization (0.16 mg chemical
oxygen demand (COD)/mg volatile solids (VS), at 2.13 mg HNO<sub>2</sub>āN/L) being six times that without FNA pretreatment (0.025
mg COD/mg VS, at 0 mg HNO<sub>2</sub>āN/L). Biochemical methane
potential tests demonstrated methane production increased with increased
FNA concentration used in the pretreatment step. Model-based analysis
indicated FNA pretreatment improved both hydrolysis rate and methane
potential, with the highest improvement being approximately 50% (from
0.16 to 0.25 d<sup>ā1</sup>) and 27% (from 201 to 255 L CH<sub>4</sub>/kg VS added), respectively, achieved at 1.78ā2.13
mg HNO<sub>2</sub>āN/L. Further analysis indicated that increased
hydrolysis rate and methane potential were related to an increase
in rapidly biodegradable substrates, which increased with increased
FNA dose, while the slowly biodegradable substrates remained relatively
static
Modeling of Simultaneous Anaerobic Methane and Ammonium Oxidation in a Membrane Biofilm Reactor
Nitrogen
removal by using the synergy of denitrifying anaerobic
methane oxidation (DAMO) and anaerobic ammonium oxidation (Anammox)
microorganisms in a membrane biofilm reactor (MBfR) has previously
been demonstrated experimentally. In this work, a mathematical model
is developed to describe the simultaneous anaerobic methane and ammonium
oxidation by DAMO and Anammox microorganisms in an MBfR for the first
time. In this model, DAMO archaea convert nitrate, both externally
fed and/or produced by Anammox, to nitrite, with methane as the electron
donor. Anammox and DAMO bacteria jointly remove the nitrite fed/produced,
with ammonium and methane as the electron donor, respectively. The
model is successfully calibrated and validated using the long-term
(over 400 days) dynamic experimental data from the MBfR, as well as
two independent batch tests at different operational stages of the
MBfR. The model satisfactorily describes the methane oxidation and
nitrogen conversion data from the system. Modeling results show the
concentration gradients of methane and nitrogen would cause stratification
of the biofilm, where Anammox bacteria mainly grow in the biofilm
layer close to the bulk liquid and DAMO organisms attach close to
the membrane surface. The low surface methane loadings result in a
low fraction of DAMO microorganisms, but the high surface methane
loadings would lead to overgrowth of DAMO bacteria, which would compete
with Anammox for nitrite and decrease the fraction of Anammox bacteria.
The results suggest an optimal methane supply under the given condition
should be applied not only to benefit the nitrogen removal but also
to avoid potential methane emissions
Determining Multiple Responses of Pseudomonas aeruginosa PAO1 to an Antimicrobial Agent, Free Nitrous Acid
Free nitrous acid (FNA) has recently
been demonstrated as an antimicrobial
agent on a range of micro-organisms, especially in wastewater-treatment
systems. However, the antimicrobial mechanism of FNA is largely unknown.
Here, we report that the antimicrobial effects of FNA are multitargeted.
The response of a model denitrifier, Pseudomnas aeruginosa PAO1 (PAO1), common in wastewater treatment, was investigated in
the absence and presence of inhibitory level of FNA (0.1 mg N/L) under
anaerobic denitrifying conditions. This was achieved through coupling
gene expression analysis, by RNA sequencing, and with a suite of physiological
analyses. Various transcripts exhibited significant changes in abundance
in the presence of FNA. Respiration was likely inhibited because denitrification
activity was severely depleted, and decreased transcript levels of
most denitrification genes occurred. As a consequence, the tricarboxylic
acid (TCA) cycle was inhibited due to the lowered cellular redox state
in the FNA-exposed cultures. Meanwhile, during FNA exposure, PAO1
rerouted its carbon metabolic pathway from the TCA cycle to pyruvate
fermentation with acetate as the end product as a possible survival
mechanism. Additionally, protein synthesis was significantly decreased,
and ribosome preservation was evident. These findings improve our
understanding of PAO1 in response to FNA and contribute toward the
potential application for use of FNA as an antimicrobial agent