Typically, to meet emission regulations, the selective catalytic reduction of NOX with NH3 (NH3-SCR) technology cause NH3 emissions owing to high NH3/NOX ratios to meet emission regulations. In this study, V-Cu/BN-Ti was used to remove residual NOX and NH3. Catalysts were evaluated for selective catalytic oxidation of NH3 (NH3-SCO) in the NH3-SCR reaction at 200–300 °C. The addition of vanadium and copper increased the number of Brønsted and Lewis acid sites available for the reaction by increasing the ratio of V5+ and forming Cu+ species, respectively. Furthermore, h-BN was dispersed in the catalyst to improve the content of vanadium and copper species on the surface. NH3 and NOX conversion were 98% and 91% at 260 °C, respectively. Consequently, slipped NH3 (NH3-Slip) emitted only 2% of the injected ammonia. Under SO2 conditions, based on the NH3 oxidation reaction, catalytic deactivation was improved by addition of h-BN. This study suggests that h-BN is a potential catalyst that can help remove residual NOX and meet NH3 emission regulations when placed at the bottom of the SCR catalyst layer in coal-fired power plants.
Nitrous oxide (N2O) is a potent greenhouse gas with a global warming potential > 310 times that of CO2. Owing to its rapid increase in atmospheric concentrations from industrial emissions, N2O poses increasing environmental concerns. Among the various N2O abatement technologies, catalytic decomposition can directly convert N2O into harmless N2 and O2 without generating secondary pollutants. In this study, Co3O4 spinel catalysts were synthesized using a polymer-assisted precipitation method, using polyvinyl alcohol, polyvinylpyrrolidone, or polyethylene glycol (PEG) as N2O decomposition catalysts. The PEG-mediated synthesis method yielded the most active catalyst with superior N2O decomposition efficiency. Structural and surface analyses confirmed that PEG facilitated the formation of Co2+-enriched surface sites and abundant oxygen vacancies, which are crucial active sites for N2O adsorption and activation. Moreover, these features improved the redox properties and electron transfer behavior of the resulting catalyst. In particular, the PEG-derived 5Co3O4/CeO2 catalyst exhibited enhanced N2O decomposition activity and stability even in the presence of coexisting N2O and O2, highlighting its potential for real-world applications. This study provides an effective synthetic route for Co3O4-based catalysts and potential opportunities for wide applications in industrial N2O removal.
This study investigates the catalytic activity and surface behaviors of V2O5 catalysts modified with promoter components to improve low-temperature activity and suppress SO2-to-SO3 oxidation. Moreover, we fabricated corrugated-type catalysts using glass fiber sheets as substrates, because powdered catalysts revealed limitations for practical applications. The modified catalysts were prepared via a slurry mixing method using vanadium precursor with different promoters such as W, Nb, Zr, Mo, Ce, Fe supported on TiO2. The catalysts were fabricated into slurry coating type catalysts using glass fiber sheets and the catalytic activity, specific surface area, and acid sites were investigated. The performance of corrugated-type catalyst and oxidation of SO2 to SO3 over a wide temperature range were evaluated using a Micro-Reactor. Our results showed that adding a promoter improves the catalytic performance of VW/Ti catalysts by enhancing surface acidity. The results varied depending on the catalyst loading and promoter components over a wide temperature range. Among them, VWNb/Ti catalysts exhibited the highest NOx conversion of 80.9% at 350 °C despite the high gaseous velocity (AV of 51 m·h−1) and the large flow rate of 20 L·min−1, with the lowest Ea of 13.7 kJ·mol−1. Among the evaluated promoters, Nb exhibited the most favorable balance of activity and SO2-to-SO3 oxidation. These results suggest that the Nb modification strategy can be extended to commercial SCR catalysts, providing a practical approach for improving catalytic performance.