12 research outputs found
Insight into the Synergic Effect of Fe-SSZ-13 Zeolite and FeMnTiZrO<sub><i>x</i></sub> Catalyst with Enhanced Reactivity in NH<sub>3</sub>–SCR of NO<sub><i>x</i></sub>
The
relatively low activity at low temperatures and poor performance
at high temperatures with low N2 selectivity are the major
problems of Fe-SSZ-13 zeolite and Mn-based metal oxides for NH3 selective catalytic reduction (SCR) of NOx, respectively. Hybrid catalysts have been prepared by mechanically
mixing Fe(1.6)-SSZ-13 zeolite and Fe0.2Mn0.4TiZr0.03Ox to remedy the defects
of both catalysts. The optimized mass ratio of zeolite and metal oxide
components in hybrid catalysts is 7:1, which shows superior NH3 SCR performances with NO conversion above 80% and N2O yield below 12 ppm at wide-temperature window ranging from 200
to 550 °C. NO-TPD and in situ DRIFTS studies
indicate that the metal oxide component in hybrid catalyst can provide
more active nitrite/nitrate species as well as more active sites for
NH3 activation to promote low-temperature activity. The
migration of active intermediate from NO on the metal oxide component
to react with NH3 adsorbed on zeolite component may be
responsible for the enhancement of low-temperature activity. Strong
adsorption of NH3 on zeolite component during SCR reaction
can hinder NH3 oxidation, so high NO conversions and N2 selectivity at high temperatures are maintained for hybrid
catalyst. These insightful understandings on the synergic effect may
be beneficial to rational design of high-performance hybrid catalysts
in NH3-SCR reaction
<i>In Situ</i> High Temperature High Pressure MAS NMR Study on the Crystallization of AlPO<sub>4</sub>‑5
A damped
oscillating crystallization process of AlPO<sub>4</sub>-5 at the presence
of small amount of water is demonstrated by <i>in situ</i> high temperature high pressure multinuclear MAS
NMR. Crystalline AlPO<sub>4</sub>-5 is formed from an intermediate
semicrystalline phase via continuous rearrangement of the local structure
of amorphous precursor gel. Activated water catalyzes the rearrangement
via repeatedly hydrolysis and condensation reaction. Strong interactions
between organic template and inorganic species facilitate the ordered
rearrangement. During the crystallization process, excess water, phosphate,
and aluminums are expelled from the precursor. The oscillating crystallization
reflects mass transportation between the solid and liquid phase during
the crystallization process. This crystallization process is also
applicable to AlPO<sub>4</sub>-5 crystallized in the presence of a
relatively large amount of water
Impact of Adsorption Configurations on Alcohol Dehydration over Alumina Catalysts
The
dehydration of alcohols to value-added chemicals using alumina
catalysts has been industrialized decades ago; however, despite years
of fundamental research, the molecular-level understanding of the
reaction process is still lacking. Herein, the dehydration reactions
of ethanol on two representative aluminas, i.e.,
γ-Al2O3 and five-coordinated Al-rich Al2O3-nanosheet (Al2O3-NS),
are comparatively investigated by a combination of solid-state NMR
spectroscopy and reaction evaluations. NMR results reveal that the
presence of hydroxyl groups nearby the Lewis acid sites (LASs) leads
to different ethanol adsorption modes. The surface hydroxyls nearby
LASs interfere with ethanol adsorption, which causes the methyl group
to move away from the alumina surface and hinders the elimination
of β-H, resulting in low reaction activity. In addition, the
desorption property of surface hydroxyls will affect the dehydration
reaction as they participate in the catalytic reaction cycles. Such
effects may also explain the lower reaction activities for diethyl
ether to ethylene compared with ethanol. Although both four- and five-coordinated
Als are the possible active sites for ethanol dehydration, the reactivity
of alcohol dehydration may also be substantially affected by the local
environment of undercoordinated Als besides coordination numbers.
These new insights demonstrate that the host–guest interaction
regulated by the local environment of active sites plays an important
role in the catalytic reaction
Untangling Framework Confinements: A Dynamical Study on Bulky Aromatic Molecules in MFI Zeolites
In MFI zeolites, differentiating the molecular dynamics
as a function
of pore structures, that is, straight-channel versus zigzag-channel
versus channel-intersection, has always been challenging, mainly due
to small differences in pore size but is of great interest because
these subtle structural differences can remarkably influence shape
selectivity. Herein, 1,2,4-trimethyl benzene (1,2,4-TMB), a characteristic
molecule larger than the 10-MR channel diameter, while smaller than
the channel intersection, is chosen to probe the pore-confined dynamical
behaviors in MFI via 2H NMR spectroscopy and density functional
theory calculations. Our results show that in the absence of acid
sites, that is, in the siliceous MFI silicalite-1, 1,2,4-TMBs can
only diffuse along the straight channels; while at equilibrium, they
incline to occupy the channel intersections with structure-defined
orientations. Furthermore, a series of dynamic motions of 1,2,4-TMBs
under different types of pore confinements are revealed and evaluated
at a molecular level over a wide range of timescales, concluded, in
short, as methyl C3-rotation > 112°-flip
> 90°-flip > translational diffusion. With the presence
of acid
sites, that is, in H-ZSM-5; however, 1,2,4-TMBs are strongly adsorbed
on Brønsted acid sites and the confined motions are further impeded.
The findings in this work may provide insights to the catalytic roles
of polymethyl-benzene intermediates, including 1,2,4-TMB, which usually
serve as active centers or deactivation precursors in zeolite-based
hydrocarbon conversion processes
Dynamic Structural Changes of SiO<sub>2</sub> Supported Pt–Ni Bimetallic Catalysts over Redox Treatments Revealed by NMR and EPR
SiO<sub>2</sub> supported Pt–Ni bimetallic catalysts with
different nickel loadings were prepared and their structural changes
after redox treatments were studied by XRD, NMR, and EPR. It is found
that the paramagnetic Ni species are mainly located on the surface
of silica lattice. The relaxation of detected <sup>29</sup>Si nuclei
in our samples is mainly governed by a spin-diffusion mechanism. The
paramagnetic effects are reflected in the spin–lattice relaxation
of Q<sup>4</sup> species, with the oxidized samples presenting faster
relaxation rates than the corresponding reduced ones. Meanwhile the
Q<sup>3</sup> species, which are in close contact with the paramagnetic
nickel centers, are “spectrally invisible”. In reducing
atmosphere Ni gradually diffuses into Pt NPs to form PtNi alloys.
While under oxidization treatment, the alloyed Ni atoms migrate outward
from the core of Pt NPs and are oxidized. The main EPR spectrum results
from reduced nickel species, and the reduced samples show stronger
EPR signal than the corresponding oxidized ones. However, in the reduced
samples, the superparamagnetic or ferromagnetic metallic Ni particles
were inside the PtNi NPs, making their influence on the <sup>29</sup>Si relaxation in the SiO<sub>2</sub> support weaker than the oxidized
samples
Nature of Five-Coordinated Al in γ‑Al<sub>2</sub>O<sub>3</sub> Revealed by Ultra-High-Field Solid-State NMR
Five-coordinated
Als (Al(V)) on the surface of aluminas play important
roles when they are used as catalysts or catalyst supports. However,
the comprehensive characterization and understanding of the intrinsic
structural properties of the Al(V) remain a challenge, due to the
very small amount in commonly used aluminas. Herein, the surface structures
of γ-Al2O3 and Al(V)-rich Al2O3 nanosheets (Al2O3–NS)
have been investigated and compared in detail by multinuclear high-field
solid-state NMR. Thanks to the high resolution and sensitivity of
ultra-high-field (up to 35.2 T) NMR, the arrangements of surface Als
were clearly demonstrated, which are substantially different from
the bulk phase in γ-Al2O3 due to the structure
reconstruction. It reveals for the first time that most of the commonly
observed Al(V)s tend to exist as aggregated states on the surface
of γ-Al2O3, like those in amorphous Al2O3–NS liable to structure reconstruction.
Our new insights into surface Al(V) species may help in understanding
the structure–function relationship of alumina
Pt/Fe-TiO<sub>2</sub>‑Catalyzed Selective Carbonyl Hydrogenation: Fe-Promoted Hydrogen Spillover
PtFe catalysts have demonstrated
their unique properties
in the
hydrogenation of carbonyl compounds, but the promotion effect of Fe
is still under debate. Herein, a series of Pt/Fe-TiO2 catalysts
with controllable Fe dispersion and similar Pt particle size were
prepared as model catalysts to elucidate the role of Fe in the selective
hydrogenation of furfural to furfuryl alcohol. The catalytic data
suggest that the states of Fe significantly affect the catalytic performance
of Pt/Fe-TiO2 and Pt/Fe-TiO2 with dispersed
Fe oligomers is ca. 20-fold more active than Pt/TiO2. The
combined results of reaction kinetic analysis and characterizations
suggest that the high activity of Pt/Fe-TiO2 in furfural
hydrogenation is mainly attributed to the promotion effect of Fe in
hydrogen spillover, a phenomenon seldom reported for PtFe catalysts.
The remote hydrogen spillover test by a physical mixture of Pt/TiO2 and Fe-TiO2 implies that the dispersed Fe oligomers
on TiO2 are more favorable to enhance the hydrogen spillover
than large Fe aggregates, which is possibly related with the high
electron/charge conductivity of the former one. This explains the
higher activity of Pt/Fe-TiO2 with dispersed Fe oligomers
than with large Fe aggregates. The use of model catalysts is beneficial
to elucidate the key factors affecting the catalytic performance of
multicomponent catalysts and sheds light on the catalyst design
The Role of Organic and Inorganic Structure-Directing Agents in Selective Al Substitution of Zeolite
Organic
and inorganic structure-directing agents (SDAs) impact
Al distributions in zeolite, but the insights into how SDAs manipulate
Al distribution have not been elucidated yet. Herein, the roles of
different SDAs such as cyclohexylamine (CHA), hexamethylenimine (HMI),
and Na+ in selective Al substitution of MCM-49 zeolite
are investigated comprehensively by multinuclear solid-state NMR.
The results demonstrate that MCM-49 synthesized with HMI shows relatively
more T6 and T7 Al, while more T2 Al
is observed using CHA. The formation of T2 Al in both MCM-49(HMI)
and MCM-49(CHA) is derived from Na+, while protonated HMIs
show bias in incorporation of T6 and T7 Al.
Most HMIs are occluded in protonated status, and about half of CHAs
are occluded in nonprotonated status. The close spatial proximity
between nonprotonated CHAs and Na+ synergistically promotes
the formation of zeolite structure, leading to more Na+ ions occluded in the zeolite channel with preferential T2 Al substitution
Mapping Al Distributions in SSZ-13 Zeolites from <sup>23</sup>Na Solid-State NMR Spectroscopy and DFT Calculations
Al
distributions and locations of corresponding nonframework cations
in SSZ-13 zeolites have significant impact on their catalytic and
adsorption properties. Herein, we demonstrate the feasibility of elucidating
Na<sup>+</sup> locations and correlated Al distributions in a series
of Na-SSZ-13 zeolites with Si/Al ratios ranging from 4 to 48 by combining <sup>23</sup>Na MQ MAS NMR spectroscopy and DFT calculations. As only
one crystallographically inequivalent T site exists in CHA cages,
the isolated Al and the Al pair (Al–O–Si–O–Si–O–Al)
and (Al–O–Si–O–Al) in 6-membered ring
(MR) distributions and the corresponding Na<sup>+</sup> locations
are clearly discriminated. In the high-silica Na-SSZ-13 zeolite, Na<sup>+</sup> ions are mainly located at the 6-MR SIIa0 site corresponding
to one Al substitution in the CHA cage. However, a small amount of
the Al pair in 6-MR is still observable even with an Si/Al ratio of
48, corresponding to two Na<sup>+</sup> ions located at 6-MR SIIa1
and 8-MR SIII’a1 sites, respectively. With more Al substitutions
in the CHA cage, a portion of Na<sup>+</sup> ions with high mobility
among different SII sites may result in the SIII’b site. In
Al-rich SSZ-13 zeolite (Si/Al = 4), the presence of Si(2Al) and Si(3Al)
may lead to Na<sup>+</sup> being located at 6-MR SIIa2, with <sup>23</sup>Na NMR signals exhibiting relatively large quadrupolar interactions,
and at 8-MR SIII’a2, with NMR signals overlapped with that
of the SIII’a1 site. This approach may expand its application
in discrimination of Al distributions in other zeolites to gain deeper
understanding of the relationship between the structure and the property
for their applications in catalysis and adsorption
Direct Detection of Reactive Gallium-Hydride Species on the Ga<sub>2</sub>O<sub>3</sub> Surface <i>via</i> Solid-State NMR Spectroscopy
Surface
metal hydrides (M–H) are ubiquitous in heterogeneous
catalytic reactions, while the detailed characterizations are frequently
hindered by their high reactivity/low concentration, and the complicated
surface structures of the host solids, especially in terms of practical
solid catalysts. Herein, combining instant quenching capture and advanced
solid-state NMR methodology, we report the first direct and unambiguous
NMR evidence on the highly reactive surface gallium hydrides (Ga–H)
over a practical Ga2O3 catalyst during direct
H2 activation. The spectroscopic effects of 69Ga and 71Ga isotopes on the 1H NMR signal are
clearly differentiated and clarified, allowing a concrete discrimination
of the Ga–H signal from the hydroxyl crowd. Accompanied with
quantitative and two-dimensional NMR spectroscopical methods, as well
as density functional theory calculations, information on the site
specification, structural configuration, and formation mechanism of
the Ga–H species has been revealed, along with the H2 dissociation mechanism. More importantly, the successful spectroscopic
identification and isolation of the surface Ga–H allow us to
clearly reveal the critical but ubiquitous intermediate role of this
species in catalytic reactions, such as propane dehydrogenation and
CO2 hydrogenation reactions. The analytic approach presented
in this work can be extended to other M–H analysis, and the
insights will benefit the design of more efficient Ga-based catalysts
