Amorphous Cr2WO6-Modified WO3 Nanowires with a Large Specific Surface Area and Rich Lewis Acid Sites: A Highly Efficient Catalyst for Oxidative Desulfurization

The oxidative desulfurization (ODS) of fuel oils is of great significance for environmental protection, and the development of efficient ODS heterogeneous catalysts is highly desired. Herein, we have designed and synthesized a novel material of amorphous Cr₂WO₆-modified WO₃ (a-Cr₂WO₆/WO₃) nanowires (3-6 nm) with a large specific surface area of 289.5 m²·g^-1 and rich Lewis acid sites. The formation of such a unique nanowire is attributed to the adsorption of Cr³⁺ cations on non-(001) planes of WO₃. In the ODS process, the a-Cr₂WO₆/WO₃ nanowires can efficiently oxidize benzothiophene (BT), dibenzothiophene (DBT), and 4,6-dimethyldibenzothiophene (4,6-DMDBT) to their corresponding sulfones in a quasi-microemulsion reaction system and possess the highest activity (E_a = 55.4 kJ/mol) for DBT: 99.0% of 15,000 ppm DBT with 2600 ppm S can be removed (70 °C, H₂O₂ as the oxidant). The improvement in ODS activity from most of WO₃ catalysts is owing to the sufficient active sites and enhanced adsorption of DBT on the basis of structural features of a-Cr₂WO₆/WO₃ nanowires. Combined with free radical capture experiments, a possible ODS mechanism of W(O₂) peroxotungstate route based on surface -OH groups is reasonably proposed. Moreover, the a-Cr₂WO₆/WO₃ nanowires have good stability and can be synthesized on a large scale, suggesting its potential applications as an efficient heterogeneous catalyst.

Fabrication of various morphological forms of a g-C3N4-supported MoO3 catalyst for the oxidative desulfurization of dibenzothiophene

The tubular structure of g-C₃N₄ supported-MoO₃ catalysts exhibits an excellent desulfurization performance due to full exposure of active sites.

Preparation of CoWO4/g-C3N4 and its Ultra-Deep Desulfurization Property

The ultra-deep desulfurization of fuel oil has become inevitable for environmental protection. Here, CoWO4/g-C3N4 was used as a catalyst, H2O2 as an oxidant, and 1-ethyl-3-methylimidazolium ethylsulfate ([EMIM][EtSO4], IL) as an extractant for the oxidative desulfurization of model oil. Scanning electron microscopy, FT-IR spectroscopy, N2 adsorption isotherms, and X-ray diffraction were used to confirm the morphology, structure, and properties of the catalysts. The influence of calcination temperature, loading dose of cobalt, amount of H2O2, reaction temperature, and other parameters were investigated. The removal rate of sulfide in model oil could reach 92.9 % at 80°C in 180 min under the optimal operation conditions (V(oil) = 5 mL, T = 80°C, m(catalyst) = 0.03 g, V(H2O2) = 0.4 mL, t = 180 min, V(IL) = 1.0 mL). In addition, the catalyst was reused five times with no significant reduction in the catalytic activity.

A multicomponent assembly approach for the design of deep desulfurization heterogeneous catalysts

An assembly approach has been employed for the preparation of a multi-component heterogeneous catalyst showing high efficiency in deep desulfurization processes.