4 research outputs found

    Promoter Effects on Nickel-Supported Magnesium Oxide Catalysts for the Carbon Dioxide Reforming of Methane

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    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

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    Waste adsorbents generated from treating Cr­(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 Cr­(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 Cr­(VI) species on the reused Cr adsorbent provides enough reactive sites for reaction, but high concentration of Cr­(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

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    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 As­(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 arsenic­(V) removal instead of SiO<sub>2</sub>. The adsorption behavior of As­(V) onto Al<sub>10</sub>-SBA-15 was investigated in aqueous solution using various experimental parameters. The adsorption data of As­(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 arsenic­(V) removal in the wide pH range of 2.0–8.2 and can remove As­(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

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    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
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