10 research outputs found
Hydrodesulfurization of Dibenzothiophene over MCM-41-Supported Pd and Pt Catalysts
Three series of aluminosilicate MCM-41 (Al-MCM-41) were
synthesized
using different aluminum sources, including aluminum isopropoxide
(AlM-I), pseudoboehmite, and aluminum sulfate, by a hydrothermal method.
The hydrodesulfurization (HDS) performance of the Al-MCM-41-supported
Pd and Pt catalysts prepared with chlorided precursors were evaluated
with dibenzothiophene (DBT) as the model sulfur-containing molecule,
in comparison with those supported on a siliceous MCM-41 (SiM). Pd/SiM
and Pt/SiM were not promising for DBT HDS because of their relatively
low activities and the rapid irreversible deactivation. Pd and Pt
supported on the acidic Al-MCM-41 materials showed higher dispersion
and enhanced HDS performances. AlM-I, which possessed the strongest
acidity, was the most promising among the mesoporous materials investigated.
The deactivated Pd/AlM-I and Pt/AlM-I can be reversibly regenerated
by H<sub>2</sub> reduction. DBT HDS over the Pd catalysts predominantly
took the hydrogenation (HYD) pathway, whereas the direct desulfurization
(DDS) pathway and HYD pathway were comparable for the Pt catalysts.
Increasing the support acidity had no positive effect on the DDS activity
of Pd but significantly enhanced its HYD activity, while the increase
in the rate constant of DDS pathway was close to that of the HYD pathway
for Al-MCM-41-supported Pt catalysts. The effect of the acid properties
of the supports on the HDS performance of Pd and Pt catalysts was
discussed by considering the formation of “electronic-deficient”
particles and the hydrogen spillover process
Synthesis of Co-Doped Tungsten Phosphide Nanoparticles Supported on Carbon Supports as High-Efficiency HER Catalysts
Tungsten
phosphide (WP) is believed to be a promising electrocatalyst
in the electrochemical hydrogen evolution reaction (HER) for its unique
catalytic performances. Nevertheless, its further application is severely
limited by the agglomeration caused by the high preparation temperature
(over 600 °C). Herein, we adopt a citric acid-guided two-stage
aging method to prepare Co-doped WP with small particle size and higher
dispersity on the surface of seven different carbon supports. Co is
successfully incorporated into the lattice of WP, causing preferable
catalytic performance. The introduction of seven different carbon
supports enhances electronic metal-supported interaction and proves
this two-stage aging method universal. The as-derived CoWP-CA/KB (two-step
aging) featured a low overpotential of 111 mV to achieve a current
density of 10 mA cm–2, along with a desirable Tafel
slope of 58 mV dec–1, outperforming most of the
WP-based electrocatalysts. Besides, the electrode possesses excellent
stability for 60 h without significant attenuation. Its remarkable
performance results from its structure (delicate particle size, uniform
dispersion, and large specific surface area) and its electrocatalytic
properties (large electrochemically active surface area, excellent
electrical conductivity, enhanced interfacial charge transfer kinetics,
and high turnover frequency). This novel synthesis strategy will be
pivotal for designing robust non-noble metal-based electrocatalysts
with high HER activity and durability to meet the future keen demand
for hydrogen
Nanocatalysts Derived from Copper Phyllosilicate for Selective Hydrogenation of Quinoline
1,2,3,4-Tetrahydroquinoline (py-THQ) is a vital intermediate
that
is used in the production of medicines, agricultural chemicals, and
other fine chemicals and is synthesized through the selective hydrogenation
of quinoline. In this work, copper phyllosilicate catalysts were prepared
by four different synthesis methods: deposition precipitation, ammonia
evaporation, a urea-assisted gel method, and hydrothermal treatment.
It was found that the different synthesis strategies led to different
actual loadings of copper in the precursors. The optimal catalyst
showed a py-THQ selectivity of 99.9% at a full conversion of quinoline
in ethanol at 100 °C and 3.0 MPa H2 for 2 h. The remarkable
enhancement of the performance may be attributed to the small particle
size, the coexistence of Cu0 and Cu+, and the
strong interaction of copper phyllosilicate by the deposition precipitation
preparation method. The characterization results showed that Cu0 and Cu+ were generated during the restoration
process and were derived from CuO and layered copper phyllosilicates,
respectively. Additionally, the ratio of Cu+/(Cu+ + Cu0) changed with the reduction temperature. The strategy
of the catalyst design and synthesis developed in this work has potential
applications in other nitrogen heterocyclic hydrogenation reactions
Efficient Ni<sub>2</sub>P/SiO<sub>2</sub> Catalysts with Enhanced Performance for the Hydrogenation of 4,6-Dimethyldibenzothiophene and Phenanthrene
Highly dispersed Ni2P catalysts (Ni2P/SiO2-DPx) were prepared by reducing
the passivation-free
precursors, which were obtained through the phosphidation of nickel
phyllosilicate with sodium hypophosphite. The strong metal–support
interaction of nickel phyllosilicate and the mild phosphidation conditions
prevented the agglomeration of Ni particles and resulted in a smaller
Ni2P particle size. The superior catalytic performance
of the as-prepared Ni2P/SiO2-DP catalysts was
evaluated in hydrodesulfurization (HDS) of 4,6-dimethyldibenzothiophene
and the hydrogenation of phenanthrene, in comparison with Ni2P/SiO2-IM and CoMoS/γ-Al2O3 prepared from a conventional incipient wetness impregnation method.
The passivation-free Ni-P/SiO2-DPx precursors
showed great storage stability, and Ni2P/SiO2-DP derived from the stored Ni-P/SiO2-DP precursors exhibited
negligible loss of HDS activity. This method provides a potential
preparation strategy for the industrial applications of transition
metal phosphides without the temperature-programmed reduction and
the subsequent passivation process
Selective Hydrodeoxygenation of Furfural to 2‑Methylfuran over Silica-Supported MoP Catalysts under Mild Conditions
In the catalytic conversion of biomass-derived furfural
to 2-methylfuran,
a concerted combination of hydrogenation and hydrogenolysis is required.
Highly dispersed MoP catalysts supported on SiO2 were prepared
by incipient impregnation with the aid of citric acid and subsequent
temperature-programmed hydrogen reduction. The prepared MoP/SiO2 exhibited a markedly high performance in the selective hydrodeoxygenation
of furfural to 2-methylfuran. A full conversion of furfural with 96.3%
selectivity to 2-methylfuran under mild reaction conditions (120 °C,
1.0 MPa, WHSV: 0.3 h–1) was obtained with over 20%
MoP/SiO2 in a continuous fixed bed reactor. The oxophilicity
of Mo species and surface acidity of MoP might enhance the adsorption
of furfural and the subsequent cleavage of the C–O bond of
the intermediate furfuryl alcohol, leading to considerably high selectivity
to 2-methylfuran. The complexion of Mo species with citric acid improved
the dispersion of MoP particles due to the controllable decomposition
of the complex in the course of preparation. Although the activity
of MoP/SiO2 decreased gradually with the reaction time
in 50 h, it could be restored by in situ hydrogen
reduction
Fabrication of a Monolith Reactor in a Copper Tube by Polymerization of Acetylene for Flow Catalysis
Continuous-flow processing is considered
as a disruptive technology
in the synthesis of active pharmaceutical ingredients and other fine
chemicals. However, it remains extremely challenging to immobilize
heterogeneous catalysts in the channels of microreactors in a facile
and flexible manner. In the present investigation, a polymer monolith
coiled copper reactor was fabricated by Cu-catalyzed polymerization
of acetylene at atmospheric pressure in the temperature range of 290–370
°C. The polymerization yielded a cotton-like structure of carbonaceous
fibers, which were able to assemble by themselves to form a monolith
inside the copper tube. The characterization results revealed that
unsaturated CC groups, which are favorable for post-surface
modification, were present on the carbonaceous fibers. After air oxidation
at 160 °C for 10 h, a fraction of the CC groups were
converted to CO groups. By strong interaction with CO
groups, Pd was immobilized in the polymer monolith by circulating
an ethanol solution of palladium acetate through the copper tube.
A 1000 mm-long monolith tube reactor with an inner diameter of 2 mm
with a Pd loading of 1.15 wt % was fabricated and used in the continuous
Suzuki–Miyaura coupling reaction. An ethanol–water (2:1
in volume) solution of iodobenzene (0.0125 M), phenylboronic acid
(0.0188 M), and potassium carbonate (0.0250 M) was used as the feed,
and the reaction took place at 100 °C and 1.0 MPa. The selectivity
to biphenyl was kept at >99% with complete conversion of iodobenzene
in a 100 h run
Fabrication of a Monolith Reactor in a Copper Tube by Polymerization of Acetylene for Flow Catalysis
Continuous-flow processing is considered
as a disruptive technology
in the synthesis of active pharmaceutical ingredients and other fine
chemicals. However, it remains extremely challenging to immobilize
heterogeneous catalysts in the channels of microreactors in a facile
and flexible manner. In the present investigation, a polymer monolith
coiled copper reactor was fabricated by Cu-catalyzed polymerization
of acetylene at atmospheric pressure in the temperature range of 290–370
°C. The polymerization yielded a cotton-like structure of carbonaceous
fibers, which were able to assemble by themselves to form a monolith
inside the copper tube. The characterization results revealed that
unsaturated CC groups, which are favorable for post-surface
modification, were present on the carbonaceous fibers. After air oxidation
at 160 °C for 10 h, a fraction of the CC groups were
converted to CO groups. By strong interaction with CO
groups, Pd was immobilized in the polymer monolith by circulating
an ethanol solution of palladium acetate through the copper tube.
A 1000 mm-long monolith tube reactor with an inner diameter of 2 mm
with a Pd loading of 1.15 wt % was fabricated and used in the continuous
Suzuki–Miyaura coupling reaction. An ethanol–water (2:1
in volume) solution of iodobenzene (0.0125 M), phenylboronic acid
(0.0188 M), and potassium carbonate (0.0250 M) was used as the feed,
and the reaction took place at 100 °C and 1.0 MPa. The selectivity
to biphenyl was kept at >99% with complete conversion of iodobenzene
in a 100 h run
Aqueous Phase Hydrodeoxygenation of Phenol over Ni<sub>3</sub>P‑CePO<sub>4</sub> Catalysts
Unsupported Ni<sub>3</sub>P-CePO<sub>4</sub> catalysts were prepared
by coprecipitation, followed by drying, calcination, and temperature-programmed
reduction. The prepared catalysts were characterized by XRD, N<sub>2</sub> adsorption–desorption, TEM, STEM-EDS elemental mapping,
XPS, NH<sub>3</sub>-TPD, FT-IR of adsorbed pyridine, and H<sub>2</sub>-TPR. Their catalytic performances in hydrodeoxygenation (HDO) were
investigated using an aqueous solution of phenol (5.0 wt %) as the
feed. CePO<sub>4</sub> was generated in coprecipitation and stable
in the subsequent drying, calcination, and temperature-programmed
reduction (final temperature 500 °C). It is shown that the addition
of CePO<sub>4</sub> resulted in enhanced HDO activity, and a maximum
activity appeared at a Ce/Ni ratio of 0.3. The presence of CePO<sub>4</sub> improved the dispersion of Ni<sub>3</sub>P significantly,
leading to enhanced hydrogenation activity. CePO<sub>4</sub> served
as the major dehydration sites as well because of its surface acidity
(mainly Lewis acid). In addition, the kinetics of the aqueous phase
HDO of phenol and cyclohexanol catalyzed by Ni<sub>3</sub>P and by
Ni<sub>3</sub>P-CePO<sub>4</sub> with Ce/Ni ratio of 0.3 were investigated
Interwoven Molecular Chains Obtained by Ionic Self-Assembly of Two Iron(III) Porphyrins with Opposite and Mismatched Charges
We
report ionic self-assembly of positively charged FeIII meso-tetra(N-methyl-4-pyridyl) porphyrin
(FeIIINMePyP) with negatively charged FeIII meso-tetra(4-sulfonatophenyl) porphyrin (FeIIITPPS4), leading to the formation of flower-like nanostructures
composed of unprecedented three-dimensional (3D) entangled chains
of porphyrin dimers. Molecular dynamics (MD) simulations show that
the 3D entanglement of porphyrin chains closely correlates to mismatched
charges present in porphyrin dimers like [FeIII(H2O)2NMePyP]5+/[FeIII(H2O)2TPPS4]3– that requires
extra interactions or entanglement with neighboring ones to achieve
electric neutrality. Interestingly, the interwoven chains bring in
excellent thermal stability as evidenced by well maintenance of the
flower-like morphology after pyrolysis at 775 °C in argon, which
is in good agreement of high-temperature MD simulations. Meanwhile,
heat treatment of the flower-like porphyrin nanostructure leads to
the formation of a non-noble metal electrocatalyst (NNME) with largely
inherited morphology. This exemplifies a new approach by combining
ionic self-assembly with subsequent pyrolysis for the synthesis of
NNMEs with desired control over the morphology of template-free NNMEs
that has rarely been achieved prior to this study. Furthermore, our
electrocatalyst exhibits excellent activity and durability toward
oxygen reduction reaction as well as much better methanol tolerance
compared with commercial Pt/C in alkaline solutions
