TY - JOUR
T1 - Selective Deoxygenation of Aqueous Furfural to 2-Methylfuran over Cu0/Cu2O·SiO2 Sites via a Copper Phyllosilicate Precursor without Extraneous Gas
AU - Li, Bolong
AU - Li, Lulu
AU - Sun, Hao
AU - Zhao, Chen
N1 - Publisher Copyright:
© 2018 American Chemical Society.
PY - 2018/9/4
Y1 - 2018/9/4
N2 - Furfural (FUL) is substantially produced by the polymeric xylan fraction of hemicellulose with the presence of acids, and 2-methyl furan (2-MF) produced from FUL is an important biogasoline additive. Here, we report that 2-MF can be selectively formed from FUL with a 90% yield at 220 °C within 2 h over Cu0/Cu2O·SiO2 sites via a copper phyllosilicate precursor without extraneous gas. Methanol is used for in situ generating of highly pure hydrogen (92% content), and the almost CO free atmosphere avoids the poison on the Cu sites. The structure-activity relationship shows that Cu0 or Cu2O or physically mixed Cu0 and Cu2O is inactive, but the hydrogen-reduced copper phyllosilicate sample comprising abundant Cu0/Cu2O·SiO2 sites with interfaces demonstrates high activities in both reactions of methanol decomposition and FUL hydrodeoxygenation (HDO). The network for converting FUL to 2-MF includes tandem steps of FUL hydrogenation and furfural alcohol (FOL) hydrogenolysis to target 2-MF, accompanied by the side-reactions of hydrogenation of furan rings and ring opening of 2-MF. The kinetics modeling shows that the rational manipulation of reaction parameters of temperatures, reaction times, and H2 amounts is the key for attaining high yields of 2-MF. Eventually, the crude aqueous FUL solution with 10 wt % water can be selectivity hydrodeoxygenated to 2-MF (close to 90% yield) at the used catalytic conditions.
AB - Furfural (FUL) is substantially produced by the polymeric xylan fraction of hemicellulose with the presence of acids, and 2-methyl furan (2-MF) produced from FUL is an important biogasoline additive. Here, we report that 2-MF can be selectively formed from FUL with a 90% yield at 220 °C within 2 h over Cu0/Cu2O·SiO2 sites via a copper phyllosilicate precursor without extraneous gas. Methanol is used for in situ generating of highly pure hydrogen (92% content), and the almost CO free atmosphere avoids the poison on the Cu sites. The structure-activity relationship shows that Cu0 or Cu2O or physically mixed Cu0 and Cu2O is inactive, but the hydrogen-reduced copper phyllosilicate sample comprising abundant Cu0/Cu2O·SiO2 sites with interfaces demonstrates high activities in both reactions of methanol decomposition and FUL hydrodeoxygenation (HDO). The network for converting FUL to 2-MF includes tandem steps of FUL hydrogenation and furfural alcohol (FOL) hydrogenolysis to target 2-MF, accompanied by the side-reactions of hydrogenation of furan rings and ring opening of 2-MF. The kinetics modeling shows that the rational manipulation of reaction parameters of temperatures, reaction times, and H2 amounts is the key for attaining high yields of 2-MF. Eventually, the crude aqueous FUL solution with 10 wt % water can be selectivity hydrodeoxygenated to 2-MF (close to 90% yield) at the used catalytic conditions.
KW - 2-Methyl furan
KW - Cu/SiO catalysts
KW - Furfural
KW - Methanol dehydrogenation
KW - Selective hydrogenation
UR - https://www.scopus.com/pages/publications/85051121862
U2 - 10.1021/acssuschemeng.8b02425
DO - 10.1021/acssuschemeng.8b02425
M3 - 文章
AN - SCOPUS:85051121862
SN - 2168-0485
VL - 6
SP - 12096
EP - 12103
JO - ACS Sustainable Chemistry and Engineering
JF - ACS Sustainable Chemistry and Engineering
IS - 9
ER -