4 research outputs found
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>S–S/L and 0.1 mg
H<sub>2</sub>S–S/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>S–S/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>S–S/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>S–S/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
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
Stereoselective Radical Cyclization Cascades Triggered by Addition of Diverse Radicals to Alkynes To Construct 6(5)–6–5 Fused Rings
Cascade radical cyclization of alkynyl
ketones with various carbon-
and heteroatom-centered radical precursors via a sequential radical
addition/1,5-H radical shift/5-<i>exo-trig</i>/radical cyclization
process was realized for the first time. This method provides a strategically
novel and step-economical protocol for diversity-oriented synthesis
of a wide range of carbocyclic and heterocyclic 6(5)–6–5
fused ring systems with three contiguous stereocenters, including
a quaternary carbon in high yields with excellent chemo- and diastereoselectivity
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>–N/L) being six times that without FNA pretreatment (0.025
mg COD/mg VS, at 0 mg HNO<sub>2</sub>–N/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>–1</sup>) and 27% (from 201 to 255 L CH<sub>4</sub>/kg VS added), respectively, achieved at 1.78–2.13
mg HNO<sub>2</sub>–N/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