Hydrodeoxygenation of guaiacol over physically mixed Co/TiO2 and WO3/TiO2 catalysts

被引:10
|
作者
Kim, Hyungjoo [1 ,2 ]
Lim, Yong Hyun [1 ,2 ]
Park, Jae Hyun [1 ,2 ]
Ha, Jeong-Myeong [3 ]
Kim, Do Heui [1 ,2 ]
机构
[1] Seoul Natl Univ, Sch Chem & Biol Engn, 1 Gwanak Ro, Seoul 08826, South Korea
[2] Seoul Natl Univ, Inst Chem Proc, 1 Gwanak Ro, Seoul 08826, South Korea
[3] Korea Inst Sci & Technol KIST, Clean Energy Res Ctr, Seoul 02792, South Korea
基金
新加坡国家研究基金会;
关键词
SELECTIVE HYDRODEOXYGENATION; ACTIVE-SITES; PHENOLS; HYDROGENATION; ACIDITY; SOLVENT; ARENES; CRESOL; PD/C;
D O I
10.1039/d3gc04400a
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
To replace the noble metals used in hydrodeoxygenation (HDO) catalysts, guaiacol HDO was conducted using various transition metal-loaded catalysts. Co/TiO2 was highly active for guaiacol HDO, enabling a more economic removal of the methoxy groups compared to the Ru/TiO2 catalyst, resulting in superior cyclohexanol selectivity. When a WO3 promoter was added to the Co catalyst to enhance its oxygen removal ability, the conversion of guaiacol was severely reduced because the co-impregnated WOx species decreased the number of exposed Co sites. To avoid this phenomenon, Co and WO(3 )were isolated by physically mixing Co/TiO2 and WO3/TiOv, where 100% conversion and oxygen removal could be achieved under 10 bar H-2 at 250(degrees)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 WO3/TiO2, and the catalytic activity could be successfully recovered by simple calcination at 400 C-degrees. 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.
引用
收藏
页码:2692 / 2704
页数:13
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