8 research outputs found
A Low-Temperature Route Triggered by Water Vapor during the Ethanol-SCR of NO<i>x</i> over Ag/Al<sub>2</sub>O<sub>3</sub>
A negative
temperature dependence was found for the selective catalytic
reduction of NO<i>x</i> by ethanol (ethanol-SCR) over Ag/Al<sub>2</sub>O<sub>3</sub> in
the absence of water vapor. Activation energy measurements for this
process confirmed that two reaction routes occurred in different temperature
ranges. In situ DRIFTS experiments revealed that these temperature-dependent
reactions were closely related to the process of the partial oxidation
of ethanol. During the partial oxidation of ethanol at low temperatures
below 400 °C, enolic species and acetates were produced, the
former of which exhibited much higher activity for NO<i>x</i> reduction than the latter. Therefore, the formation of enolic species
and their further transformation to produce N<sub>2</sub> governs
the low-temperature route for ethanol-SCR. At temperatures above 400
°C, only acetate appeared during the partial oxidation of ethanol,
and its further reaction with NO<i>x</i> accounts for the
high-temperature route. More importantly, introduction of water vapor
significantly enhanced the deNO<i>x</i> activity of Ag/Al<sub>2</sub>O<sub>3</sub> for ethanol-SCR, especially in the low-temperature
region. On pure Al<sub>2</sub>O<sub>3</sub>, however, the ethanol-SCR
process was suppressed by the presence of water vapor, indicating
that the promotion effect of water vapor is closely related to silver.
Within the low-temperature region, water addition promoted the partial
oxidation of ethanol to produce enolic species, the occurrence of
which also enhanced the formation of NO<sub>2</sub> during the ethanol-SCR
over Ag/Al<sub>2</sub>O<sub>3</sub>. The produced NO<sub>2</sub> in
turn accelerated the formation of enolic species and also exhibited
a higher reactivity toward enolic species compared with NO. Such synergistic
effects of NO<sub>2</sub> and enolic species induced by water vapor
addition thus triggered a cyclic reaction pathway for NO<i>x</i> reduction with high efficiency
Silver Valence State Determines the Water Tolerance of Ag/Al<sub>2</sub>O<sub>3</sub> for the H<sub>2</sub>–C<sub>3</sub>H<sub>6</sub>–SCR of NO<i><sub>x</sub></i>
The influence of
the silver valence state on Ag/Al<sub>2</sub>O<sub>3</sub> on the
water tolerance of H<sub>2</sub>–C<sub>3</sub>H<sub>6</sub>–SCR of NO<i><sub>x</sub></i> was investigated.
The valence state of silver species on Ag/Al<sub>2</sub>O<sub>3</sub>, which was carefully characterized by XPS, UV–vis, and XANES
measurements, was adjusted by varying the calcination temperature
from 500 to 900 °C. Oxidized silver species were predominant
on Ag/Al<sub>2</sub>O<sub>3</sub> calcined at temperatures below 600
°C (LT-catalysts), while further increasing the calcination (temperatures
above 600 °C, HT-catalysts) promoted the transformation of oxidized
silver species into metallic silver clusters. The samples with higher
amounts of oxidized silver species exhibited better water tolerance
in the H<sub>2</sub>–C<sub>3</sub>H<sub>6</sub>–SCR.
Activation energy measurements confirmed that the mechanism of NO<i><sub>x</sub></i> reduction on these catalysts was the same.
In situ DRIFTS studies demonstrated that metallic silver species promoted
the formation of active enolic species and the complete oxidation
of formate, thus improving the low-temperature activity of HT-catalysts
in the absence of water vapor. Water addition eliminated the formate,
releasing the active Ag<sup>+</sup> sites for enolic species formation,
and thus promoted the low-temperature activity of LT-catalysts. From
a comprehensive point of view, 60% oxidized silver species on Ag/Al<sub>2</sub>O<sub>3</sub> catalysts is the optimal percentage for deNO<i><sub>x</sub></i> performance and water tolerance
Discerning the Role of Ag–O–Al Entities on Ag/γ-Al<sub>2</sub>O<sub>3</sub> Surface in NOx Selective Reduction by Ethanol
Alumina-supported silver catalysts
(Ag/Al<sub>2</sub>O<sub>3</sub>) derived from AlOOH, AlÂ(OH)<sub>3</sub>, and Al<sub>2</sub>O<sub>3</sub> were investigated for the selective
catalytic reduction of
NOx by ethanol. In order to discern the role of support Al skeleton
in anchoring silver species and reducing NOx, the series of alumina-supported
silver catalysts calcined at different temperatures was characterized
by means of <i>in situ</i> DRIFTS, XPS, UV–vis DRS,
XRD, BET, and NMR. It was found that the NO<sub><i>x</i></sub> reduction efficiency order as affected by alumina precursors
could be generally described as AlOOH > Al<sub>2</sub>O<sub>3</sub> ≫ AlÂ(OH)<sub>3</sub>, with the optimum calcination temperature
of 600 °C. XPS and UV–vis results indicated that silver
ions predominated on the Ag/Al<sub>2</sub>O<sub>3</sub> surface. Solid
state NMR suggested that the silver ions might be anchored on Al tetrahedral
and octahedral sites, forming Ag–O–Al<sub>tetra</sub> and Ag–O–Al<sub>octa</sub> entities. With the aid
of NMR and DFT calculation, Al<sub>octa</sub> was found to be the
energetically favorable site to support silver ions. However, DFT
calculation indicated that the Ag–O–Al<sub>tetra</sub> entity can significantly adsorb and activate vital −NCO species
rather than the Ag–O–Al<sub>octa</sub> entity. A strongly
positive correlation between the amount of Al<sub>tetra</sub> structures
and N<sub>2</sub> production rate confirms the crucial role of Al<sub>tetra</sub> in NOx reduction by ethanol
Nature of Ag Species on Ag/γ-Al<sub>2</sub>O<sub>3</sub>: A Combined Experimental and Theoretical Study
The nature of silver species on Ag/Al<sub>2</sub>O<sub>3</sub> catalysts
with different silver loadings was studied by photoelectron spectroscopy
(XPS) and X-ray absorption near-edge spectroscopy (XANES) and extended
X-ray absorption fine structure spectroscopy (EXAFS) combined with
theoretical calculation (DFT). On the basis of selective catalytic
reduction of NO<sub><i>x</i></sub> by ethanol experiments,
it was found that the optimum silver content varies from 1 wt % to
2 wt %. The supported silver species are predominated by +1 oxidation
state ions attached to surface oxygen atoms (Ag–O) under low
silver loading of 2 wt %, which play a crucial role during the HC-SCR
process. An Ag–Ag shell emerged clearly in analysis of EXAFS
data when silver loading was increased to 2 wt %, which was beneficial
for low-temperature activity. The theoretical models for Ag<sub>n</sub><sup>δ+</sup> species (1 ≤ <i>n</i> ≤
4, both ions and oxidized silver clusters) on alumina were consistent
with the coordination structure analysis by EXAFS. The predominant
silver ions are most likely stabilized at isolated tetrahedral Al
sites (Ag–O–Al<sub>IVb</sub>) on the γ-Al<sub>2</sub>O<sub>3</sub> (110) surface. However, the most reactive silver
ion seems to be anchored on a tricoordinate Al<sub>III</sub> site
(Ag–O–Al<sub>III</sub>). Density of states analysis
revealed that the Ag–O–Al<sub>III</sub> entity might
be a very active silver species in terms of the hybridization of Ag,
O, and Al orbitals to promote its catalytic activity
SO<sub>2</sub> Photoaging Enhances the Surface Conversion of NO<sub>2</sub>‑to-HONO on Elemental Carbon
Chemical
interactions between soot and NO2 are believed
to play a significant role in the formation of HONO in the atmosphere.
Despite extensive studies, the present understanding of how soot chemistry
influences HONO formation remains contentious due to the rapid deactivation
of surface reactive sites. In this study, we reveal the novel mechanism
that the photoaging of SO2 can notably accelerate the reduction
of functionalized elemental carbon (EC) in soot by rapidly removing
surface hydroxyl functional groups. The reduced EC can further drive
continuous HONO formation due to the rejuvenation of the surface reduction
reactivity. We verify that the increase in surface vacancy defects
created by the removal of OH groups is the key contributing factor
and the reactive centers driving NO2 adsorption and reduction.
This finding challenges the existing notion that fresh soot is rapidly
deactivated due to the decline in reductive capacity. Our work suggests
that aged graphene-like EC on soot may have a significant effect on
the chemical conversion of NO2-to-HONO in polluted air,
contributing to a better understanding of air pollution chemistry
Spatial Distribution of Brønsted Acid Sites Determines the Mobility of Reactive Cu Ions in the Cu-SSZ-13 Catalyst during the Selective Catalytic Reduction of NO<sub><i>x</i></sub> with NH<sub>3</sub>
The formation of dimer-Cu species, which serve as the
active sites
of the low-temperature selective catalytic reduction of NOx with NH3 (NH3-SCR), relies
on the mobility of CuI species in the channels of the Cu-SSZ-13
catalysts. Herein, the key role of framework Brønsted acid sites
in the mobility of reactive Cu ions was elucidated via a combination
of density functional theory calculations, in situ impedance spectroscopy, and in situ diffuse reflectance
ultraviolet–visible spectroscopy. When the number of framework
Al sites decreases, the Brønsted acid sites decrease, leading
to a systematic increase in the diffusion barrier for [CuÂ(NH3)2]+ and less formation of highly reactive
dimer-Cu species, which inhibits the low-temperature NH3-SCR reactivity and vice versa. When the spatial distribution of
Al sites is uneven, the [CuÂ(NH3)2]+ complexes tend to migrate from an Al-poor cage to an Al-rich cage
(e.g., cage with paired Al sites), which effectively accelerates the
formation of dimer-Cu species and hence promotes the SCR reaction.
These findings unveil the mechanism by which framework Brønsted
acid sites influence the intercage diffusion and reactivity of [CuÂ(NH3)2]+ complexes in Cu-SSZ-13 catalysts
and provide new insights for the development of zeolite-based catalysts
with excellent SCR activity by regulating the microscopic spatial
distribution of framework Brønsted acid sites
Spatial Distribution of Brønsted Acid Sites Determines the Mobility of Reactive Cu Ions in the Cu-SSZ-13 Catalyst during the Selective Catalytic Reduction of NO<sub><i>x</i></sub> with NH<sub>3</sub>
The formation of dimer-Cu species, which serve as the
active sites
of the low-temperature selective catalytic reduction of NOx with NH3 (NH3-SCR), relies
on the mobility of CuI species in the channels of the Cu-SSZ-13
catalysts. Herein, the key role of framework Brønsted acid sites
in the mobility of reactive Cu ions was elucidated via a combination
of density functional theory calculations, in situ impedance spectroscopy, and in situ diffuse reflectance
ultraviolet–visible spectroscopy. When the number of framework
Al sites decreases, the Brønsted acid sites decrease, leading
to a systematic increase in the diffusion barrier for [CuÂ(NH3)2]+ and less formation of highly reactive
dimer-Cu species, which inhibits the low-temperature NH3-SCR reactivity and vice versa. When the spatial distribution of
Al sites is uneven, the [CuÂ(NH3)2]+ complexes tend to migrate from an Al-poor cage to an Al-rich cage
(e.g., cage with paired Al sites), which effectively accelerates the
formation of dimer-Cu species and hence promotes the SCR reaction.
These findings unveil the mechanism by which framework Brønsted
acid sites influence the intercage diffusion and reactivity of [CuÂ(NH3)2]+ complexes in Cu-SSZ-13 catalysts
and provide new insights for the development of zeolite-based catalysts
with excellent SCR activity by regulating the microscopic spatial
distribution of framework Brønsted acid sites
Spatial Distribution of Brønsted Acid Sites Determines the Mobility of Reactive Cu Ions in the Cu-SSZ-13 Catalyst during the Selective Catalytic Reduction of NO<sub><i>x</i></sub> with NH<sub>3</sub>
The formation of dimer-Cu species, which serve as the
active sites
of the low-temperature selective catalytic reduction of NOx with NH3 (NH3-SCR), relies
on the mobility of CuI species in the channels of the Cu-SSZ-13
catalysts. Herein, the key role of framework Brønsted acid sites
in the mobility of reactive Cu ions was elucidated via a combination
of density functional theory calculations, in situ impedance spectroscopy, and in situ diffuse reflectance
ultraviolet–visible spectroscopy. When the number of framework
Al sites decreases, the Brønsted acid sites decrease, leading
to a systematic increase in the diffusion barrier for [CuÂ(NH3)2]+ and less formation of highly reactive
dimer-Cu species, which inhibits the low-temperature NH3-SCR reactivity and vice versa. When the spatial distribution of
Al sites is uneven, the [CuÂ(NH3)2]+ complexes tend to migrate from an Al-poor cage to an Al-rich cage
(e.g., cage with paired Al sites), which effectively accelerates the
formation of dimer-Cu species and hence promotes the SCR reaction.
These findings unveil the mechanism by which framework Brønsted
acid sites influence the intercage diffusion and reactivity of [CuÂ(NH3)2]+ complexes in Cu-SSZ-13 catalysts
and provide new insights for the development of zeolite-based catalysts
with excellent SCR activity by regulating the microscopic spatial
distribution of framework Brønsted acid sites