4 research outputs found
Promoter Effects on Nickel-Supported Magnesium Oxide Catalysts for the Carbon Dioxide Reforming of Methane
The
nickel catalysts supported on bare MgO and its binary Mg–Al,
Mg–La, and Mg–Fe metal oxides were prepared and used
for carbon dioxide reforming of methane to syngas. The effects of
Al, La, and Fe metal oxides on the structural properties, reducibility,
and metal–support interaction of the Ni catalysts supported
on MgO-based binary metal oxide were investigated. The X-ray powder
diffraction (XRD), transmission electron microscopy (TEM), and hydrogen
temperature-programmed reduction (H<sub>2</sub>-TPR) analyses show
that the nickel nanoparticles were highly dispersed on the supports.
It is found that the Al ions can be well-incorporated into the MgO
lattice to form uniform Mg–Al oxides, while isolated lanthanum
oxides and iron oxides were observed in the Mg–La and Mg–Fe
binary systems by TEM, respectively. Ni/Mg–Al metal oxide exhibits
greatly improved catalytic activity, owing to the formation of a homogeneous
Mg–Al oxide matrix with small particle sizes of Ni nanoparticles
compared to bare Ni/MgO. Very low conversions for both CH<sub>4</sub> and CO<sub>2</sub> were obtained on Ni/Mg–La and Ni/Mg–Fe
metal oxides, even at a high temperature of 800 °C, as a result
of the incomplete reduction of the nickel nanoparticles
Recycling Spent Cr Adsorbents as Catalyst for Eliminating Methylmercaptan
Waste
adsorbents generated from treating CrÂ(VI)-containing wastewater
are hazardous materials and generally landfilled or treated by acid
or base desorption, with concomitant high cost and toxic effects.
The present work shows that these Cr adsorbents can be reused as highly
efficient catalysts for treating sulfur-containing VOCs (CH<sub>3</sub>SH), not only avoiding the economic and environmental impact from
the conventional approaches, but also achieving the efficient treatment
of sulfur-containing waste gas. Importantly, these reused Cr adsorbents
exhibit enhanced activity and stability compared with the catalysts
reported elsewhere, indicating a new avenue of green chemistry. The
highly toxic adsorbed CrÂ(VI) species are reduced to a Cr<sub>2</sub>O<sub>3</sub> crystalline phase by calcination and finally immobilized
as a Cr<sub>2</sub>S<sub>3</sub> solid phase while converting and
eliminating CH<sub>3</sub>SH. Still, the presence of CrÂ(VI) species
on the reused Cr adsorbent provides enough reactive sites for reaction,
but high concentration of CrÂ(VI) species causes serious accumulation
of coke deposit on the catalyst, leading to fast deactivation of the
catalyst
Uptake of Arsenic(V) Using Alumina Functionalized Highly Ordered Mesoporous SBA-15 (Al<sub><i>x</i></sub>‑SBA-15) as an Effective Adsorbent
The SBA-15 (a mesoporous SiO<sub>2</sub> material) decorated with
10% aluminum (Al<sub>10</sub>-SBA-15) was found to be an excellent
adsorbent to remove AsÂ(V) from water. The highly dispersed aluminum
species have been obtained over the well-ordered mesoporous Al<sub>10</sub>-SBA-15 adsorbent and act as the active adsorption sites
for arsenicÂ(V) removal instead of SiO<sub>2</sub>. The adsorption
behavior of AsÂ(V) onto Al<sub>10</sub>-SBA-15 was investigated in
aqueous solution using various experimental parameters. The adsorption
data of AsÂ(V) could be fitted more successfully by the Langmuir isotherm
than the Freundlich isotherm model, and the pseudo-second-order equation
described this entire adsorption process well. It is found from the
analysis of kinetic data with the intraparticle diffusion mode that
both the boundary layer (film) diffusion and intraparticle diffusion
may contribute to the rate-limiting steps. Importantly, Al<sub>10</sub>-SBA-15 exhibits high arsenicÂ(V) removal in the wide pH range of
2.0–8.2 and can remove AsÂ(V) from water containing arsenate
of ≤2.235 mg·L<sup>–1</sup> to reach levels in
accordance with the regulations for drinking water purposes (<10
μg·L<sup>–1</sup>). Consequently, Al<sub>10</sub>-SBA-15 is believed to be an effective adsorbent for treating arsenate
contaminated wastewater
Removal of NO<sub><i>x</i></sub> from Flue Gas Using Yellow Phosphorus and Phosphate Slurry as Adsorbent
A composite
slurry containing yellow phosphorus and phosphate slurry
was used to remove NO<sub><i>x</i></sub> from flue gas,
where yellow phosphorus is considered to promote generation of ozone
from oxygen. The latter can oxidize NO to form more water-soluble
N<sub><i>x</i></sub>O<sub><i>y</i></sub> species,
finally converted to HNO<sub>2</sub> and HNO<sub>3</sub>. These acids
can react with phosphate slurry to form PO<sub>4</sub><sup>3–</sup>. Thus, the final solution containing NO<sub>3</sub><sup>–</sup> and PO<sub>4</sub><sup>3–</sup> can be potentially used as
raw material for the production of nitrogen phosphorus compound fertilizer.
Moreover, effects of various parameters on NO<sub><i>x</i></sub> removal efficiency were optimized, and single-factor experiments
together with response surface optimization were applied for optimizing
these parameters. It was indicated that the removal efficiency of
NO<sub><i>x</i></sub> can obtain 99.2% under optimal conditions.
Subsequently, the corresponding reaction mechanisms were discussed.
Therefore, using the mixtures of yellow phosphorus and phosphate slurry
as absorbent not only obtains high NO<sub><i>x</i></sub> removal efficiency, but can avoid the need to dispose of spent liquid
wastes, which provides an attractive approach for controlling NO<sub><i>x</i></sub>. Moreover, the present slurry system can
eliminate NO<sub><i>x</i></sub> and SO<sub>2</sub> simultaneously
with high removal efficiency