11 research outputs found
Syntheses and crystal structures of four lanthanide complexes based on two tri-protonated hexacarboxylic acids of 1,2,3,4,5,6-cyclohexane-hexacarboxylic acid and mellitic acid
<div><p>Four lanthanide complexes with two tri-protonated hexacarboxylic acids [1,2,3,4,5,6-cyclohexane-hexacarboxylic acid (H<sub>6</sub>chhc) and mellitic acid (H<sub>6</sub>Mel)], [Pr(H<sub>3</sub>chhc)(DMF)<sub>3</sub>(H<sub>2</sub>O)]·H<sub>2</sub>O (<b>1</b>), Nd(H<sub>3</sub>chhc)(DMF)<sub>3</sub> (<b>2</b>), [Er(H<sub>2</sub>O)<sub>8</sub>]·(H<sub>3</sub>Mel)·9(H<sub>2</sub>O) (<b>3</b>), and [Yb(H<sub>2</sub>O)<sub>8</sub>]·(H<sub>3</sub>Mel)·8.5(H<sub>2</sub>O) (<b>4</b>), have been synthesized in solution at room temperature and characterized by elemental analysis, IR spectrum, and single-crystal X-ray diffraction. The crystal structures of <b>1</b> and <b>2</b> are made up of a (4<sup>4</sup>, 6<sup>2</sup>) 2-D network extended infinitely parallel to the (1 0 0) plane. The H<sub>3</sub>chhc<sup>3−</sup> anions assume a <i>cis</i>-<i>e,a,e,a,e,a</i>-conformation with the central ring in chair-shaped configuration. In <b>3</b> and <b>4</b>, the H<sub>3</sub>Mel<sup>3−</sup> as counter ions are interconnected by hydrogen bonds to form 2-D organic supramolecular layers. The coordination modes and abilities of H<sub>6</sub>chhc and mellitic acid are discussed and compared. The luminescences of <b>1–4</b> have been investigated.</p></div
Surfactant-Mediated One-Pot Method To Prepare Pd–CeO<sub>2</sub> Colloidal Assembled Spheres and Their Enhanced Catalytic Performance for CO Oxidation
A simple,
one-pot method to fabricate ordered, monodispersed Pd–CeO<sub>2</sub> colloidal assembled spheres (CASs) was developed using the
surfactant-mediated solvothermal approach, which involves a tunable
self-assembled process by carefully controlling different chemical
reactions. The evolution process and formation mechanism of the CASs
were thoroughly investigated by time-controlled and component-controlled
experiments. For CO oxidation, this CAS nanocatalyst exhibited much
higher catalytic activity and thermal stability than Pd/CeO<sub>2</sub> prepared by an impregnation method, and its complete CO conversion
temperature is ∼120 °C. The enhanced catalytic performance
for CO oxidation could be attributed to the synergistic effect of
highly dispersed PdO species and Pd<sup>2+</sup> ions incorporated
into the CeO<sub>2</sub> lattice. For this CAS catalyst, each sphere
can be viewed as a single reactor, and its catalytic performance can
be further improved after being supported on alumina, which is obviously
higher than results previously reported. Furthermore, this method
was used to successfully prepare M–CeO<sub>2</sub> CASs (M
= Pt, Cu, Mn, Co), showing further that this is a new and ideal approach
for fabricating active and stable ceria-based materials
Effect of One-Pot Rehydration Process on Surface Basicity and Catalytic Activity of Mg<sub><i>y</i></sub>Al<sub>1‑a</sub>REE<sub><i>a</i></sub>O<sub><i>x</i></sub> Catalyst for Aldol Condensation of Citral and Acetone
The
liquid phase synthesis of pseudoionones (PS) by the cross-aldol
condensation of citral and acetone was investigated over MgAl mixed
oxides containing rare earth elements (REE = Y, La, Eu), which were
obtained from corresponding REE-modified hydrotalcite materials after
calcination. The results showed that the unmodified and La(Eu)-modified
MgAl mixed oxide catalysts showed relatively low activity, and Y-modified
MgAl mixed oxides presented an unexpected high catalytic activity.
PS selectivity of ∼85% and citral conversion of 100% were achieved
at 60 °C for 3 h. On the basis of the characterizations of the
structural, textural, and basic properties, it was found that Mg<sub>3</sub>Al<sub>1‑a</sub>Y<sub>a</sub>O<sub><i>x</i></sub> catalysts exhibited relatively well-developed small flake
morphology with high surface area and pore volume, resulting in exposure
of more basic sites on the catalyst surface. The formation of PS over
Mg<sub>3</sub>Al<sub>1‑a</sub>Y<sub>a</sub>O<sub><i>x</i></sub> may be accompanied by gradual modification of the catalyst
surface to form re-Mg<sub>3</sub>Al<sub>1‑a</sub>Y<sub>a</sub>O<sub><i>x</i></sub> through a rehydration process with
produced water, which reconverts the O<sup>2–</sup> basic sites
to OH<sup>–</sup> basic groups. Unlike La and Eu elements,
the presence of Y could promote this “one-pot” or <i>in situ</i> rehydration process of MgAl mixed oxides during
the aldol reaction. This Y-modified MgAl mixed oxides after a one-pot
rehydration process with active Brønsted basic sites is responsible
for the high activity in the cross-aldol condensation of citral and
acetone
Production of Ethylene Glycol and Its Monoether Derivative from Cellulose
The efficient usage of lignocellulosic
biomass is of great significance
for large-scale low-cost biomass conversion to biofuels and other
useful chemicals. Here, an interesting catalytic process was reported
related to converting cellulose into ethylene glycol (EG) and ethylene
glycol monoether (EGME) in methanol over a Ru/NbOPO<sub>4</sub> catalyst,
with the cleavage of a C–C bond by NbOPO<sub>4</sub> and further
hydrogenation by supported Ru particles. The influence of reaction
temperature, hydrogen pressure, and reaction time was systematically
investigated and showed that a 54.5% total yield of EG and EGME could
be obtained at 220 °C in 3 M Pa H<sub>2</sub>, which was an exciting
result. Meanwhile, the effect of solvent was also studied in detail.
It was shown that methanol played an important role in the production
of EG and EGME, especially in the cleavage of the C–C bond.
Methanol could protect the CO bond in glucose produced from
cellulose through acetalization, thus prevent its hydrogenation, and
led to the production of EG and EGME. Furthermore, the influence of
dopants (W, Sn, Ni, Cu) was further investigated, and it was found
that only the Ru–Ni/NbOPO<sub>4</sub> catalyst was more effective
through limiting the further hydrogenolysis of products (EG and EGME)
to CO and alkanes, and as high as 64% total yield of EG+EGME was achieved.
Moreover, the Ru–Ni/NbOPO<sub>4</sub> catalyst showed good
reusability, which can be reused at least four times with a little
loss in EG and EGME yield
A Highly Effective Catalyst of Sm-MnO<sub><i>x</i></sub> for the NH<sub>3</sub>‑SCR of NO<sub><i>x</i></sub> at Low Temperature: Promotional Role of Sm and Its Catalytic Performance
Sm-Mn mixed oxide catalysts prepared
by the coprecipitation method
were developed, and their catalytic activities were tested for the
selective catalytic reduction (SCR) of NO with ammonia at low temperature.
The results showed that the amount of Sm markedly influenced the activity
of the MnO<sub><i>x</i></sub> catalyst for SCR, that the
activity of the Sm-Mn mixed oxide catalyst exhibited a volcano-type
tendency with an increase in the Sm content, and that the appropriate
mole ratio of Sm to Mn in the catalyst was 0.1. In addition, the presence
of Sm in the MnO<sub><i>x</i></sub> catalyst can obviously
enhance both water and sulfur dioxide resistances. The effect of Sm
on the physiochemical properties of the Sm-MnO<sub><i>x</i></sub> catalyst were investigated by XRD, low-temperature N<sub>2</sub> adsorption, XPS, and FE-SEM techniques. The results showed that
the presence of Sm in the Sm-MnO<sub><i>x</i></sub> catalyst
can restrain the crystallization of MnO<sub><i>x</i></sub> and increase its surface area and the relative content of both Mn<sup>4+</sup> and surface oxygen (O<sub>S</sub>) on the surface of the
Sm-MnO<sub><i>x</i></sub> catalyst. NH<sub>3</sub>-TPD,
NO-TPD, and in situ DRIFT techniques were used to investigate the
absorption of NH<sub>3</sub> and NO on the Sm-MnO<sub><i>x</i></sub> catalyst and their surface reactions. The results revealed
that the presence of Sm in the Sm<sub>0.1</sub>-MnO<sub><i>x</i></sub> catalyst can increase the absorption amount of NH<sub>3</sub> and NO on the catalyst and does not vary the SCR reaction mechanism
over the MnO<sub><i>x</i></sub> catalyst: that is, the coexistence
of Eley–Rideal and Langmuir–Hinshelwood mechanisms (bidentate
nitrate is the active intermediate), in which the Eley–Rideal
mechanism is predominant
Effect of Ceria Crystal Plane on the Physicochemical and Catalytic Properties of Pd/Ceria for CO and Propane Oxidation
Ceria nanocrystallites with different
morphologies and crystal
planes were hydrothermally prepared, and the effects of ceria supports
on the physicochemical and catalytic properties of Pd/CeO<sub>2</sub> for the CO and propane oxidation were examined. The results showed
that the structure and chemical state of Pd on ceria were affected
by ceria crystal planes. The Pd species on CeO<sub>2</sub>-R (rods)
and CeO<sub>2</sub>-C (cubes) mainly formed Pd<sub><i>x</i></sub>Ce<sub>1–<i>x</i></sub>O<sub>2−σ</sub> solid solution with −Pd<sup>2+</sup>–O<sup>2–</sup>–Ce<sup>4+</sup>– linkage. In addition, the PdO<sub><i>x</i></sub> nanoparticles were dominated on the surface
of Pd/CeO<sub>2</sub>-O (octahedrons). For the CO oxidation, the Pd/CeO<sub>2</sub>-R catalyst showed the highest catalytic activity among three
catalysts, its reaction rate reached 2.07 × 10<sup>–4</sup> mol g<sub>Pd</sub><sup>–1</sup> s<sup>–1</sup> at
50 °C, in which CeO<sub>2</sub>-R mainly exposed the (110) and
(100) facets with low oxygen vacancy formation energy, strong reducibility,
and high surface oxygen mobility. TOF of Pd/CeO<sub>2</sub>-R (3.78
× 10<sup>–2</sup> s<sup>–1</sup>) was much higher
than that of Pd/CeO<sub>2</sub>-C (6.40 × 10<sup>–3</sup> s<sup>–1</sup>) and Pd/CeO<sub>2</sub>-O (1.24 × 10<sup>–3</sup> s<sup>–1</sup>) at 50 °C, and its activation
energy (<i>E</i><sub>a</sub>) was 40.4 kJ/mol. For propane
oxidation, the highest reaction rate (8.08 × 10<sup>–5</sup> mol g<sub>Pd</sub><sup>–1</sup> s<sup>–1</sup> at
300 °C) was obtained over the Pd/CeO<sub>2</sub>-O catalyst,
in which CeO<sub>2</sub>-O mainly exposed the (111) facet. There are
strong surface Ce–O bonds on the ceria (111) facet, which favors
the existence of PdO particles and propane activation. The turnover
frequency (TOF) of the Pd/CeO<sub>2</sub>-O catalyst was highest (3.52
× 10<sup>–2</sup> s<sup>–1</sup>) at 300 °C
and its <i>E</i><sub>a</sub> value was 49.1 kJ/mol. These
results demonstrate the inverse facet sensitivity of ceria for the
CO and propane oxidation over Pd/ceria
Incorporating Rich Mesoporosity into a Ceria-Based Catalyst via Mechanochemistry
Ceria-based materials
possessing mesoporous structures afford higher
activity than the corresponding bulk materials in CO oxidation and
other catalytic applications, because of the wide pore channel and
high surface area. The development of a direct, template-free, and
scalable technology for directing porosity inside ceria-based materials
is highly welcome. Herein, a family of mesoporous transition-metal-doped
ceria catalysts with specific surface areas up to 122 m<sup>2</sup> g<sup>–1</sup> is constructed by mechanochemical grinding.
No templates, additives, or solvents are needed in this process, while
the mechanochemistry-mediated restructuring and the decomposing of
the organic group led to plentiful mesopores. Interestingly, the copper
species are evenly dispersed in the ceria matrix at the atomic scale,
as observed in high resolution scanning transmission electron microscopy
in high angle annular dark field. The copper-doped ceria materials
show good activity in the CO oxidation
Low-Temperature Methane Combustion over Pd/H-ZSM-5: Active Pd Sites with Specific Electronic Properties Modulated by Acidic Sites of H‑ZSM‑5
Pd/H-ZSM-5
catalysts could completely catalyze CH<sub>4</sub> to
CO<sub>2</sub> at as low as 320 °C, while there is no detectable
catalytic activity for pure H-ZSM-5 at 320 °C and only a conversion
of 40% could be obtained at 500 °C over pure H-ZSM-5. Both the
theoretical and experimental results prove that surface acidic sites
could facilitate the formation of active metal species as the anchoring
sites, which could further modify the electronic and coordination
structure of metal species. PdO<sub><i>x</i></sub> interacting
with the surface Brönsted acid sites of H-ZSM-5 could exhibit
Lewis acidity and lower oxidation states, as proven by the XPS, XPS
valence band, CO-DRIFTS, pyridine FT-IR, and NH<sub>3</sub>-TPD data.
Density functional theory calculations suggest PdO<sub><i>x</i></sub> groups to be the active sites for methane combustion, in the
form of [AlO<sub>2</sub>]Pd(OH)-ZSM-5. The stronger Lewis acidity
of coordinatively unsaturated Pd and the stronger basicity of oxygen
from anchored PdO<sub><i>x</i></sub> species are two key
characteristics of the active sites ([AlO<sub>2</sub>]Pd(OH)-ZSM-5)
for methane combustion. As a result, the PdO<sub><i>x</i></sub> species anchored by Brønsted acid sites of H-ZSM-5 exhibit
high performance for catalytic combustion of CH<sub>4</sub> over Pd/H-ZSM-5
catalysts
Synthesis of Nonspherical Mesoporous Silica Ellipsoids with Tunable Aspect Ratios for Magnetic Assisted Assembly and Gene Delivery
Despite the extensive application of ellipsoidal micro-/nanoparticles,
the synthesis of shape anisotropic ellipsoids is rare because of the
minimization of surface free energy that favors simple spherical shape
rather than complex nonspherical shape. We present the synthesis of
silica ellipsoids with hexagonal mesostructure via the organic–inorganic
cooperative assembly in the presence of cosolvents (KCl and ethanol).
The aspect ratio of ellipsoids can be tuned systematically by controlling
the concentration of ethanol. Transmission electron microscopy (TEM)
shows that the ellipsoid possesses one-dimensional (1-D) pore channels
parallel to the major axis, and the electron tomography (ET) technique
shows that the ellipsoid has indeed hexagonal prism morphology in
the middle and ellipsoidal morphology at two tips. A mechanism for
the formation of mesoporous silica ellipsoids has been proposed. Importantly,
magnetite/silica composite ellipsoids were prepared through a nanocasting
route and can be used as building blocks to organize into ordered
arrays in response to an external magnetic field. In addition, after
functionalized with amino-groups, the amino-modified anisotropic magnetite/silica
ellipsoids can be further used as carriers for delivering oligo-DNA-Cy3
into tumor cells, showing potential in directed self-assembly and
drug/gene delivery
Synthesis of Nonspherical Mesoporous Silica Ellipsoids with Tunable Aspect Ratios for Magnetic Assisted Assembly and Gene Delivery
Despite the extensive application of ellipsoidal micro-/nanoparticles,
the synthesis of shape anisotropic ellipsoids is rare because of the
minimization of surface free energy that favors simple spherical shape
rather than complex nonspherical shape. We present the synthesis of
silica ellipsoids with hexagonal mesostructure via the organic–inorganic
cooperative assembly in the presence of cosolvents (KCl and ethanol).
The aspect ratio of ellipsoids can be tuned systematically by controlling
the concentration of ethanol. Transmission electron microscopy (TEM)
shows that the ellipsoid possesses one-dimensional (1-D) pore channels
parallel to the major axis, and the electron tomography (ET) technique
shows that the ellipsoid has indeed hexagonal prism morphology in
the middle and ellipsoidal morphology at two tips. A mechanism for
the formation of mesoporous silica ellipsoids has been proposed. Importantly,
magnetite/silica composite ellipsoids were prepared through a nanocasting
route and can be used as building blocks to organize into ordered
arrays in response to an external magnetic field. In addition, after
functionalized with amino-groups, the amino-modified anisotropic magnetite/silica
ellipsoids can be further used as carriers for delivering oligo-DNA-Cy3
into tumor cells, showing potential in directed self-assembly and
drug/gene delivery