TY - JOUR
T1 - Efficient Synthesis of Cyclohexanol and Ethanol via the Hydrogenation of Acetic Acid-Derived Cyclohexyl Acetate with the CuxAl1Mn2−x Catalysts
AU - Song, Tongyang
AU - Chen, Wei
AU - Qi, Yuanyuan
AU - Wu, Peng
AU - Zhu, Zhirong
AU - Li, Xiaohong
N1 - Publisher Copyright:
© 2021 Wiley-VCH GmbH
PY - 2021/7/7
Y1 - 2021/7/7
N2 - The hydrogenation of cyclohexyl acetate (CHA), derived from the esterification of acetic acid and cyclohexene, not only alleviates the overcapacity of acetic acid, but also produces value-added cyclohexanol (CHOL) and ethanol at a low cost. Herein, we prepared Cu1Al1, Cu1Mn1 and CuxAl1Mn2−x catalysts via a deposition-precipitation method for the hydrogenation of CHA to CHOL and ethanol. As a result, the ternary CuxAl1Mn2−x catalysts exhibited superior behaviors to Cu1Al1 and Cu1Mn1. To our delight, Cu1Al1Mn1 had a 95.0 % CHA conversion and 93.6 % selectivity to CHOL along with 97.6 % selectivity to ethanol in a batch reactor. Based on detailed characterization, the ternary CuxAl1Mn2−x catalysts possessed more uniformed dispersion of Cu particles, less aggregation and larger BET specific surface area than the binary catalysts. Furthermore, Cu1Al1Mn1 possessed the highest Cu0/(Cu0+Cu+) molar ratio, the highest (Mn2++Mn3+)/Mn4+ molar ratio and the most abundant surface oxygen vacancies, facilitating the adsorption and activation of CHA and hydrogen. In addition, Cu1Al1Mn1 had excellent stability (>500 h) in a fixed-bed reactor.
AB - The hydrogenation of cyclohexyl acetate (CHA), derived from the esterification of acetic acid and cyclohexene, not only alleviates the overcapacity of acetic acid, but also produces value-added cyclohexanol (CHOL) and ethanol at a low cost. Herein, we prepared Cu1Al1, Cu1Mn1 and CuxAl1Mn2−x catalysts via a deposition-precipitation method for the hydrogenation of CHA to CHOL and ethanol. As a result, the ternary CuxAl1Mn2−x catalysts exhibited superior behaviors to Cu1Al1 and Cu1Mn1. To our delight, Cu1Al1Mn1 had a 95.0 % CHA conversion and 93.6 % selectivity to CHOL along with 97.6 % selectivity to ethanol in a batch reactor. Based on detailed characterization, the ternary CuxAl1Mn2−x catalysts possessed more uniformed dispersion of Cu particles, less aggregation and larger BET specific surface area than the binary catalysts. Furthermore, Cu1Al1Mn1 possessed the highest Cu0/(Cu0+Cu+) molar ratio, the highest (Mn2++Mn3+)/Mn4+ molar ratio and the most abundant surface oxygen vacancies, facilitating the adsorption and activation of CHA and hydrogen. In addition, Cu1Al1Mn1 had excellent stability (>500 h) in a fixed-bed reactor.
KW - Chemoselective hydrogenation
KW - Cu-based catalyst
KW - Cyclohexanol
KW - Cyclohexyl acetate
KW - Ethanol
UR - https://www.scopus.com/pages/publications/85105827102
U2 - 10.1002/cctc.202100284
DO - 10.1002/cctc.202100284
M3 - 文章
AN - SCOPUS:85105827102
SN - 1867-3880
VL - 13
SP - 3099
EP - 3111
JO - ChemCatChem
JF - ChemCatChem
IS - 13
ER -