Abstract
Unsupported molybdenum carbide catalyst was prepared by a nonthermal plasma carburization (PC) method. The input voltage (50, 60, 70, 80, 90, 100, and 110 V) and discharge time (2, 3, and 4 h) were optimized. Pure β-Mo2C was prepared at input voltage of 90 V for 4 h (Mo2C-PC). In comparison, a molybdenum carbide catalyst (Mo2C-TPC) was prepared by the conventional temperature-programmed reduction carburization. Mo2C-PC had smaller crystal size (7.4 nm), as estimated by the Scherrer equation (XRD), and more active sites (Mo2+), as determined by XPS. TEM characterization revealed that there was no obvious agglomeration of Mo2C-PC particles, whereas agglomerative particles and a carbon layer could be observed in Mo2C-TPC. Mo2C-PC and Mo2C-TPC were evaluated in the hydrodeoxygenation (HDO) of guaiacol, phenol, and anisole, using a stainless-steel tubular reactor. The results showed that both the conversion of phenolic compounds and the selectivity to aromatic hydrocarbons over Mo2C-PC were higher than those of Mo2C-TPC at low temperatures (< 300 °C). The TOF of Mo2C-PC(0.37 s−1) was close to that of Mo2C-TPC (0.32 s−1) in HDO of guaiacol, suggesting that the enhanced performance could be ascribed to reduced particles, increased Mo sites (Mo2+) and suppressed carbon deposit.
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Acknowledgements
This research was financially supported by the Natural Science Foundation of China (21972014, 22172012, 22172015, 21872014) and International S&T Cooperation Program of China (2016YFE0109800).
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Yu, Z., Yu, Z., Wang, Y. et al. Hydrodeoxygenation of Guaiacol to Aromatic Hydrocarbons over Mo2C Prepared in Nonthermal Plasma. Plasma Chem Plasma Process 42, 1069–1083 (2022). https://doi.org/10.1007/s11090-022-10257-z
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DOI: https://doi.org/10.1007/s11090-022-10257-z