Hydrodeoxygenation of guaiacol over physically mixed Co/TiO and WO/TiO catalysts

To replace the noble metals used in hydrodeoxygenation (HDO) catalysts, guaiacol HDO was conducted using various transition metal-loaded catalysts. Co/TiO 2 was highly active for guaiacol HDO, enabling a more economic removal of the methoxy groups compared to the Ru/TiO 2 catalyst, resulting in superior cyclohexanol selectivity. When a WO 3 promoter was added to the Co catalyst to enhance its oxygen removal ability, the conversion of guaiacol was severely reduced because the co-impregnated WO x species decreased the number of exposed Co sites. To avoid this phenomenon, Co and WO 3 were isolated by physically mixing Co/TiO 2 and WO 3 /TiO 2 , where 100% conversion and oxygen removal could be achieved under 10 bar H 2 at 250 °C. The cause of the catalyst deactivation was systematically investigated by magnetic separation of the physical mixture of the catalysts after the reaction, followed by a series of characterization studies. Temperature-programmed-oxidation mass spectroscopy and Raman spectroscopy revealed that the deposition of carbonaceous species was the main contributor to the deactivation of WO 3 /TiO 2 , and the catalytic activity could be successfully recovered by simple calcination at 400 °C. This study provides insights into the development of economical and efficient physically mixed HDO catalysts using transition metals, and contributes to the understanding of the deactivation and regeneration of physically mixed HDO catalysts. The physically mixed Co/TiO 2 and WO 3 /TiO 2 catalysts exhibited excellent catalytic performance in the hydrodeoxygenation of guaiacol, and the deactivated catalyst could be successfully regenerated after magnetic separation.