10 research outputs found
Hollow and Yolk–Shell Co-N-C@SiO<sub>2</sub> Nanoreactors: Controllable Synthesis with High Selectivity and Activity for Nitroarene Hydrogenation
The
use of hollow and yolk–shell nanocomposites is an effective
route to enhance catalytic performance. A strategy that allows precise
control of the nanocomposites was developed to synthesize novel hollow
and yolk–shell SiO2 nanoreactors of Co-N-C@SiO2, which used ZIF-67 as the hard template and also as the source
for active sites. A size dependence of the nanoreactor structure was
observed. Large size of ZIF-67 gave yolk–shell Y-Co-N-C@SiO2 while small size of crystals gave hollow H-Co-N-C@SiO2. The hydrogenation reaction results showed that the Co-N-C@SiO2 catalyst exhibited a high selectivity (>99%) to aniline
and gave an activity (35.3 h–1) ∼3.3 times
higher than that of Co/SiO2 (11.8 h–1). The excellent performance was attributed to that Co nanoparticles
were doped in the N-C framework where they formed Co-Nx species and that the HSN had a void structure that
had a reduced diffusion limitation
Enhanced Selectivity in the Hydrogenation of Acetylene due to the Addition of a Liquid Phase as a Selective Solvent
The
selective hydrogenation of acetylene is usually a gas-phase
reaction. In this work, a liquid phase was introduced as a selective
solvent to improve the selectivity to ethylene by coupling absorption
to the reaction. The catalyst was 0.01% Pd supported on a low surface
area silica. <i>N</i>-methyl-2-pyrrolidone (NMP) was used
as a selective solvent, and decane was used as a nonselective solvent
for comparison. The liquid-phase hydrogenation was carried out in
a stirred flat bottom flask operated in gas continuous and liquid
batch mode, and the gas-phase hydrogenation was carried out in a fixed
bed reactor. The selectivity to ethylene in the gas-phase hydrogenation
was 50–70%. In contrast, the highest selectivity to ethylene
in the NMP liquid-phase hydrogenation was increased to 96%, while
in decane it had the same value as in the gas phase. In NMP, a low
reaction temperature below 80 °C did not give a high selectivity
to ethylene because the relatively high ethylene solubility in NMP
led to deep hydrogenation and the high acetylene solubility caused
more oligomerization. Good catalyst stability was obtained under the
optimized conditions of a relatively low space velocity, H<sub>2</sub>:C<sub>2</sub>H<sub>2</sub> ratio above 10, and reaction temperature
above 80 °C. Significant deactivation also occurred in NMP under
other conditions due to oligomerization
Supported Ultrafine NiCo Bimetallic Alloy Nanoparticles Derived from Bimetal–Organic Frameworks: A Highly Active Catalyst for Furfuryl Alcohol Hydrogenation
Highly dispersed
NiCo bimetallic alloy nanoparticles have been
successfully immobilized on the SiO<sub>2</sub> frameworks by using
heteronuclear metal–organic frameworks (MOFs) as metal alloy
precursors. Catalyst characterizations revealed that the average size
of NiCo alloy particles was less than 1 nm, with a total metal loading
of about 20 wt %. As compared to individual Ni or Co MOF-derived catalysts
and the catalysts prepared by the conventional impregnation method,
the ultrafine NiCo/SiO<sub>2</sub>-MOF catalyst showed a much better
catalytic performance in the catalytic hydrogenation of furfuryl alcohol
(FA) to tetrahydrofurfuryl alcohol (THFA) under mild conditions, giving
99.8% conversion of FA and 99.1% selectivity to THFA. It was found
that a significant synergistic effect existed between Co and Ni within
the subnanometer NiCo/SiO<sub>2</sub>-MOF catalyst, which was 2 and
20 times more active than Ni/SiO<sub>2</sub>-MOF and Co/SiO<sub>2</sub>-MOF, respectively
Insights into the Activity Screening and Hydroformylation Kinetics of Rh-Based Bimetallic Phosphides
Heterogeneous
hydroformylation is of great industrial
and economic interest. Here, we proposed a screening strategy to search
highly active Rh-based bimetallic phosphide catalysts and successfully
predicted Rh7Pd1P4 as a new active
site, which was more active than other phosphide catalysts. Experimental
verifications confirmed the synthesis of bimetallic phosphides and
the activity enhancement for styrene hydroformylation. The kinetics
of styrene hydroformylation was studied based on the rate-determining
step (RDS) achieved from density functional theory (DFT) calculations.
The proposed two-parameter kinetics was more consistent with the experimental
data than previously used first-order or zero-order models. By changing
the reaction pressure, the RDS could be identified by experiments
with the help of the kinetic model. The RDS identified from the experiments
and the kinetic model agreed well with the DFT calculations, which
further proved the accuracy of the kinetic model
Highly Selective Hydrogenation of Furfural to Cyclopentanone over a NiFe Bimetallic Catalyst in a Methanol/Water Solution with a Solvent Effect
The
aqueous phase hydrogenation of furfural to cyclopentanone over
a NiFe bimetallic catalyst was investigated for the efficient utilization
of biomass-derived compounds. Catalyst characterization by XRD, EDS
mapping, and TPR revealed significant synergetic effects in the NiFe/SBA-15
catalyst. With NiFe/SBA-15, cyclopentanone selectivity was increased
to 78.4% from 46.1% with Ni/SBA-15. The use of different supports
showed that weak acidity favors cyclopentanone formation. The solvent
played an important role: methanol/water solutions with different
compositional ratios gave significantly changed product distributions.
With pure methanol, and methanol-dominated and water-dominated solutions,
respectively, the main product was furfuryl alcohol, tetrahydrofurfuryl
alcohol, and cyclopentanone. Furfural in the water inhibited THFA
formation, which led furfural to preferentially produce cyclopentanone.
At the optimized reaction temperature, NiFe/SBA-15 in water gave 99.8%
furfural conversion and 90% cyclopentanone yield at 300 min, which
was much better than most reported nonprecious metal catalysts
High-Performance Ni<sub>3</sub>P Catalyst for CO Hydrogenation of Ethyl Levulinate: Ni<sup>δ+</sup> as Outstanding Adsorption Sites
It
is important but challenging to develop non-noble metal catalysts
with high activity and selectivity for biomass conversion. The activation
of CO bond is a crucial step in biomass upgradation. Herein,
a series of Ni-xP/Al2O3 catalysts
with different P/Ni molar ratios were prepared for the conversion
of ethyl levulinate to γ-valerolactone. The developed Ni-0.38P/Al2O3 catalyst was 5.4 times more active than conventional
Ni/Al2O3 based on turnover frequency and significantly
outperformed the state-of-the-art non-noble metal catalysts. The unique
catalytic performance was ascribed to the formation of Ni3P phase, which was identified by several characterizations. The results
of DFT calculation and characterization by XPS and CO-FTIR revealed
that electron was transferred from Ni to P with the formation of Niδ+ sites. In situ FTIR for the surface reaction indicated
that Niδ+ acted as a new active site to activate
the CO bond, which rendered the high intrinsic activity of
Ni3P for the CO hydrogenation of EL
Nano-H-ZSM‑5 with Short <i>b</i>‑Axis Channels as a Highly Efficient Catalyst for the Synthesis of Ethyl Levulinate from Furfuryl Alcohol
For the ethanolysis of biomass-derived
furfuryl alcohol (FA) to
value-added ethyl levulinate (EL), the development of an efficient
solid acid catalyst is very important for industrial application with
high FA concentration. Herein, a H-ZSM-5 catalyst with nano b-axis channels (NB-H-ZSM-5) was synthesized and used for
the conversion of FA. Detailed catalyst characterization proved that
the NB-H-ZSM-5 catalysts (Si/Al = 25∼125) with ∼70 nm b-axis channels were successfully prepared. The NB-H-ZSM-5
catalyst with Si/Al = 75 showed the highest activity. Its structural
characteristics allowed for fast diffusion of reactants and products
and full utilization of active sites, which endowed it with higher
activity compared to commercial H-ZSM-5 (C-H-ZSM-5). Its moderate
acidity effectively inhibited the polymerization of FA even at a high
FA concentration of 20 wt %. The spent catalyst was easily regenerated
by coke burn-off to give a good recyclability. Furthermore, based
on the proposed reaction network, a method of physically mixing the
NB-H-ZSM-5 (75) catalyst with a small amount of Amberlyst-15 was proposed
to further increase the EL yield from 64.7 to 82.1% at an FA concentration
of 6 wt %
Highly Effective Removal of Pharmaceutical Compounds from Aqueous Solution by Magnetic Zr-Based MOFs Composites
In
this research, the magnetic UiO-66-NH2 composites
were prepared and applied as adsorbents for the effective removal
of salicylic acid (SA) and acetylsalicylic acid (ASA) from aqueous
media. The as-prepared adsorbent inherits both the excellent properties
of metal organic frameworks and the magnetic separation property of
magnetic material, which makes the magnetic UiO-66-NH2 composite
exhibit a rapid separation rate and high capacity. The adsorption
kinetics were well fitted with the pseudo-second-order model, and
the adsorption isotherm could be well explained using the Langmuir
isotherm. The dominant mechanism for adsorption of SA and ASA was
hydrogen-bonding, the affinity of carboxyl groups with Zr–O
clusters, and electrostatic interactions. The high adsorption capacities,
easy separation process, fast adsorption kinetics, and satisfactory
reusability of the magnetic UiO-66-NH2 give it fantastic
potential as adsorbents for adsorptive separation of pharmaceutical
contaminants from aqueous media
Interaction between Single Metal Atoms and UiO-66 Framework Revealed by Low-Dose Imaging
Atomically dispersed metals encapsulated
in metal–organic
frameworks (MOFs) have attracted extensive attention in catalysis
and energy fields. Amino groups were considered conducive to the formation
of single atom catalysts (SACs) due to the strong metal–linker
interactions. Here, atomic details of Pt1@UiO-66 and Pd1@UiO-66-NH2 are revealed using low-dose integrated
differential phase contrast scanning transmission electron microscopy
(iDPC-STEM). Single Pt atoms locate on the benzene ring of p-benzenedicarboxylic acid (BDC) linkers in Pt@UiO-66,
while single Pd atoms are adsorbed by the amino groups in Pd@UiO-66-NH2. However, Pt@UiO-66-NH2 and Pd@UiO-66 show obvious
clusters. Therefore, amino groups do not always favor the formation
of SACs, and density functional theory (DFT) calculations indicate
that a moderate binding strength between metals and MOFs is preferred.
These results directly reveal the adsorption sites of single metal
atoms in UiO-66 family, paving the way for understanding the interaction
between single metal atoms and the MOFs
