3 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>โ</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 0โ1000 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>โ</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>โ</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>OโN/h/g VSS in
the NO<sub>2</sub><sup>โ</sup> concentration range of 500โ1000
mg N/L. The observed NO<sub>2</sub><sup>โ</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>OโN/h/g VSS) was attained at a lower NO<sub>2</sub><sup>โ</sup> concentration of 200โ250 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>โ</sup> and high DO concentrations.
Collectively, the findings show that exceedingly high NO<sub>2</sub><sup>โ</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>โ</sup> is observed across different AOB cultures
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>โ</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>โ</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