13 research outputs found
Single-Atom Alloy PdāAg Catalyst for Selective Hydrogenation of Acrolein
PdāAg
alloy catalysts with very dilute amounts of Pd were
synthesized. EXAFS results demonstrated that when the concentration
of Pd was as low as 0.01 wt %, Pd was completely dispersed as isolated
single atoms in Ag nanoparticles. The activity for the hydrogenation
of acrolein was improved by the presence of these isolated Pd atoms
due to the creation of sites with lower activation energy for H<sub>2</sub> dissociation. In addition, for the same particle size, the
0.01% Pd/8% Ag alloy nanoparticles exhibited higher selectivity than
their monometallic counterparts, suggesting that the Pd atom may act
as a site for the favorable bonding of the acrolein molecule for facile
hydrogenation of the aldehyde functionality
Direct Synthesis of Low-Coordinate Pd Catalysts Supported on SiO<sub>2</sub> via Surface Organometallic Chemistry
Highly
dispersed low-coordinate Pd sites on SiO<sub>2</sub> are
fabricated by grafting the Pd<sup>II</sup> PCP-pincer complex (<sup>tBu</sup>PCP)ĀPdāOH (<sup>tBu</sup>PCP = 2,6-C<sub>6</sub>H<sub>3</sub>(CH<sub>2</sub>P<sup>t</sup>Bu<sub>2</sub>)<sub>2</sub>) on
SiO<sub>2</sub>, followed by calcination with ozone (100 Ā°C)
and reduction with H<sub>2</sub> (300 Ā°C). The chemisorption
process and structure of this organometallic complex on SiO<sub>2</sub> is established by solution-phase <sup>1</sup>H and <sup>31</sup>P NMR and solid-state <sup>31</sup>P CPMAS NMR spectroscopy, XPS,
DRIFTS, and AC-HAADF-STEM. The CO adsorption properties of the Pd
centers reveal a surprisingly high fraction of adsorption sites where
CO is bound in a linear fashion, indicative of low-coordinate Pd.
Furthermore, enhanced selectivity of these catalyst centers in aerobic
alcohol oxidation versus a control catalyst argues that these low-coordinate
sites are the catalytically active sites
Isolated Fe<sup>II</sup> on Silica As a Selective Propane Dehydrogenation Catalyst
We report a comparative study of
isolated Fe<sup>II</sup>, iron
oxide particles, and metallic nanoparticles on silica for non-oxidative
propane dehydrogenation. It was found that the most selective catalyst
was an isolated Fe<sup>II</sup> species on silica prepared by grafting
the open cyclopentadienide iron complex, bisĀ(2,4-dimethyl-1,3-pentadienide)
ironĀ(II) or FeĀ(<i>o</i>Cp)<sub>2</sub>. The grafting and
evolution of the surface species was elucidated by <sup>1</sup>H NMR,
diffuse reflectance infrared Fourier transform spectroscopy and X-ray
absorption spectroscopies. The oxidation state and local structure
of surface Fe were characterized by X-ray absorption near-edge structure
(XANES) and extended X-ray absorption fine structure. The initial
grafting of iron proceeds by one surface hydroxyl SiāOH reacting
with FeĀ(<i>o</i>Cp)<sub>2</sub> to release one diene ligand
(<i>o</i>CpH), generating a SiO<sub>2</sub>-bound Fe<sup>II</sup>(<i>o</i>Cp) species, <b>1-Fe</b><i><b>o</b></i><b>Cp</b>. Subsequent treatment with
H<sub>2</sub> at 400 Ā°C leads to loss of the remaining diene
ligand and formation of nanosized iron oxide clusters, <b>1-C</b>. Dispersion of these Fe oxide clusters occurs at 650 Ā°C, forming
an isolated, ligand-free Fe<sup>II</sup> on silica, <b>1-Fe</b><sup><b>II</b></sup>, which is catalytically active and highly
selective (ā¼99%) for propane dehydrogenation to propene. Under
reaction conditions, there is no evidence of metallic Fe by in situ
XANES. For comparison, metallic Fe nanoparticles, <b>2-NP-Fe</b><sup><b>0</b></sup>, were independently prepared by grafting
FeĀ[NĀ(SiMe<sub>3</sub>)<sub>2</sub>]<sub>2</sub> onto silica, <b>2-FeN*</b>, and reducing it at 650 Ā°C in H<sub>2</sub>. The
Fe NPs were highly active for propane conversion but showed poor selectivity
(ā¼14%) to propene. Independently prepared Fe oxide clusters
on silica display a low activity. The sum of these results suggests
that selective propane dehydrogenation occurs at isolated Fe<sup>II</sup> sites
Pushing the Limits on MetalāOrganic Frameworks as a Catalyst Support: NU-1000 Supported Tungsten Catalysts for <i>o</i>āXylene Isomerization and Disproportionation
Acid-catalyzed skeletal
CāC bond isomerizations are important
benchmark reactions for the petrochemical industries. Among those, <i>o</i>-xylene isomerization/disproportionation is a probe reaction
for strong BrĆønsted acid catalysis, and it is also sensitive
to the local acid site density and pore topology. Here, we report
on the use of phosphotungstic acid (PTA) encapsulated within NU-1000,
a Zr-based metalāorganic framework (MOF), as a catalyst for <i>o</i>-xylene isomerization at 523 K. Extended X-ray absorption
fine structure (EXAFS), <sup>31</sup>P NMR, N<sub>2</sub> physisorption,
and X-ray diffraction (XRD) show that the catalyst is structurally
stable with time-on-stream and that WO<sub><i>x</i></sub> clusters are necessary for detectable rates, consistent with conventional
catalysts for the reaction. PTA and framework stability under these
aggressive conditions requires maximal loading of PTA within the NU-1000
framework; materials with lower PTA loading lost structural integrity
under the reaction conditions. Initial reaction rates over the NU-1000-supported
catalyst were comparable to a control WO<sub><i>x</i></sub>-ZrO<sub>2</sub>, but the NU-1000 composite material was unusually
active toward the transmethylation pathway that requires two adjacent
active sites in a confined pore, as created when PTA is confined in
NU-1000. This work shows the promise of metalāorganic framework
topologies in giving access to unique reactivity, even for aggressive
reactions such as hydrocarbon isomerization
Stabilizing Single-Atom and Small-Domain Platinum via Combining Organometallic Chemisorption and Atomic Layer Deposition
Oxide-supported single-atom
Pt materials are prepared by combining
surface organometallic chemisorption with atomic layer deposition
(ALD). Here Pt is supported as a discrete monatomic āpincerā
complex, stabilized by an atomic layer deposition (ALD) derived oxide
overcoat, and then calcined at 400 Ā°C under O<sub>2</sub>. ALD-derived
Al<sub>2</sub>O<sub>3</sub>, TiO<sub>2</sub>, and ZnO overlayers are
effective in suppressing Pt sintering and significantly stabilizing
single Pt atoms. Furthermore, this procedure decreases the overall
Pt nuclearity (ā¼1 nm average particle diameter) versus bare
Pt (ā¼3.8 nm average diameter), as assayed by aberration corrected
HAADF-STEM. The TiO<sub>2</sub> and ZnO overcoats are significantly
more effective at stabilizing single-atom Pt species and decreasing
the overall Pt nuclearity than Al<sub>2</sub>O<sub>3</sub> overcoats.
Vibrational spectroscopy of adsorbed CO also shows that oxidized Pt
species commonly thought to be single Pt atoms are inactive for catalytic
oxidation of adsorbed CO. CO chemisorption measurements show site
blockage by the ALD overcoats
Correction to āComputationally Guided Discovery of Catalytic Cobalt-Decorated MetalāOrganic Framework for Ethylene Dimerizationā
Correction to āComputationally Guided Discovery
of Catalytic Cobalt-Decorated MetalāOrganic Framework for Ethylene
Dimerization
General Method for Determination of the Surface Composition in Bimetallic Nanoparticle Catalysts from the L Edge Xāray Absorption Near-Edge Spectra
Bimetallic PtPd on silica nanoparticle catalysts have
been synthesized,
and their average structure has been determined by Pt L<sub>3</sub> and Pd K edge extended X-ray absorption fine-structure spectroscopy.
The bimetallic structure is confirmed from elemental line scans by
scanning transmission electron microscopy of the individual 2-nm-sized
particles. A general method is described to determine the surface
composition of bimetallic nanoparticles even when both metals adsorb;
for example, CO, by combining the quantitative characterization by
X-ray absorption near-edge structure spectra at L edges with CO adsorption
with the adsorption stoichiometry determined by Fourier transform
infrared spectroscopy. Determination of the surface composition leads
to a better understanding of the changes in catalytic chemistry that
accompany alloy formation. Although monometallic Pt and Pd have similar
turnover rates for neopentane hydrogenolysis and isomerization, on
the basis of the surface composition, it appears that in the bimetallic
PtPd catalysts, the rate and products are determined predominantly
by Pt with little contribution from surface Pd. Density functional
theory calculations indicate that the center of the Pt d-band density
of states shifts to higher energy, or closer to the Fermi level, whereas
that in Pd shifts to lower energy away from the Fermi level. Similarly,
the calculated enthalpy of CO adsorption increases on Pt, but decreases
on Pd. It is speculated that because of the very low surface coverage
of the neopentane reaction intermediates, only surface atoms that
form the strongest bonds are catalytically activeīøthat is,
Ptīørather than all surface atoms. The dominant role of Pd,
therefore, appears to be to (slightly) modify Pt rather than to contribute
to the catalytic conversion
Fine-Tuning the Activity of MetalāOrganic Framework-Supported Cobalt Catalysts for the Oxidative Dehydrogenation of Propane
Few-atom cobalt-oxide
clusters, when dispersed on a Zr-based metalāorganic
framework (MOF) NU-1000, have been shown to be active for the oxidative
dehydrogenation (ODH) of propane at low temperatures (<230 Ā°C),
affording a selective and stable propene production catalyst. In our
current work, a series of promoter ions with varying Lewis acidity,
including NiĀ(II), ZnĀ(II), AlĀ(III), TiĀ(IV) and MoĀ(VI), are anchored
as metal-oxide,hydroxide clusters to NU-1000 followed by CoĀ(II) ion
deposition, yielding a series of NU-1000-supported bimetallic-oxo,hydroxo,aqua
clusters. Using difference envelope density (DED) analyses, the spatial
locations of the promoter ions and catalytic cobalt ions are determined.
For all samples, the promoter ions are sited between pairs of Zr<sub>6</sub> nodes along the MOF <i>c</i>-axis, whereas the
location of the cobalt ions varies with the promoter ions. These NU-1000-supported
bimetallic-oxide clusters are active for propane ODH after thermal
activation under O<sub>2</sub> to open a cobalt coordination site
and to oxidize CoĀ(II) to CoĀ(III), as evidenced by operando X-ray absorption
spectroscopy at the Co K-edge. In accord with the decreasing Lewis
acidity of the promoter ion, catalytic activity increases in the following
order: MoĀ(VI) < TiĀ(IV) < AlĀ(III) < ZnĀ(II) < NiĀ(II). The
finding is attributed to increasing ease of formation of CoĀ(III)āO<sup>ā¢</sup> species and stabilization of a cobaltĀ(III)-oxyl/propane
transition state as the Lewis acidity of the promoter ions decreases.
The results point to an increasing ability to fine-tune the structure-dependent
activity of MOF-supported heterogeneous catalysts. Coupled with mechanistic
studiesīøcomputational or experimentalīøthis ability may
translate into informed prediction of improved catalysts for propane
ODH and other chemical reactions
MetalāOrganic Framework Supported Cobalt Catalysts for the Oxidative Dehydrogenation of Propane at Low Temperature
Zr-based metalāorganic
frameworks (MOFs) have been shown
to be excellent catalyst supports in heterogeneous catalysis due to
their exceptional stability. Additionally, their crystalline nature
affords the opportunity for molecular level characterization of both
the support and the catalytically active site, facilitating mechanistic
investigations of the catalytic process. We describe herein the installation
of CoĀ(II) ions to the Zr<sub>6</sub> nodes of the mesoporous MOF,
NU-1000, via two distinct routes, namely, solvothermal deposition
in a MOF (SIM) and atomic layer deposition in a MOF (AIM), denoted
as Co-SIM+NU-1000 and Co-AIM+NU-1000, respectively. The location of
the deposited Co species in the two materials is determined via difference
envelope density (DED) analysis. Upon activation in a flow of O<sub>2</sub> at 230 Ā°C, both materials catalyze the oxidative dehydrogenation
(ODH) of propane to propene under mild conditions. Catalytic activity
as well as propene selectivity of these two catalysts, however, is
different under the same experimental conditions due to differences
in the Co species generated in these two materials upon activation
as observed by <i>in situ</i> X-ray absorption spectroscopy.
A potential reaction mechanism for the propane ODH process catalyzed
by Co-SIM+NU-1000 is proposed, yielding a low activation energy barrier
which is in accord with the observed catalytic activity at low temperature
A Hafnium-Based MetalāOrganic Framework as a Nature-Inspired Tandem Reaction Catalyst
Tandem catalytic systems, often inspired
by biological systems,
offer many advantages in the formation of highly functionalized small
molecules. Herein, a new metalāorganic framework (MOF) with
porphyrinic struts and Hf<sub>6</sub> nodes is reported. This MOF
demonstrates catalytic efficacy in the tandem oxidation and functionalization
of styrene utilizing molecular oxygen as a terminal oxidant. The product,
a protected 1,2-aminoalcohol, is formed selectively and with high
efficiency using this recyclable heterogeneous catalyst. Significantly,
the unusual regioselective transformation occurs only when an Fe-decorated
Hf<sub>6</sub> node and the Feāporphyrin strut work in concert.
This report is an example of concurrent orthogonal tandem catalysis