Supported Molybdenum Oxides for the Aldol Condensation Reaction of Acetaldehyde
Supported Molybdenum Oxides for the Aldol Condensation Reaction of Acetaldehyde
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DOI:
10.1016/j.jcat.2022.03.002
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发表时间:
2022-03
影响因子:
7.3
通讯作者:
M. Rasmussen;Sean Najmi;Giada Innocenti;A. Medford;Carsten Sievers;J. Will Medlin
中科院分区:
文献类型:
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作者:
M. Rasmussen;Sean Najmi;Giada Innocenti;A. Medford;Carsten Sievers;J. Will Medlin
The (retro-)aldol condensation reaction is an important chemical transformation in the upgrading of biomass-derived compounds into fuels and valuable specialty chemicals. In this study, we found that supported molybdenum oxide (MoOx) catalysts were active and selective for the aldol condensation of acetaldehyde to crotonaldehyde under steady-state reactor conditions. Through a combination of transmission electron microscopy (TEM), ultraviolet–visible (UV–VIS) diffuse reflectance spectroscopy, Fourier transform infrared (FTIR) spectroscopy of adsorbed pyridine, and steady-state reactor testing, we determined that highly dispersed MoOxhas a strong interaction with a γ-Al2O3support resulting in optimal catalyst performance at low weight loadings. In contrast, MoOxparticles supported on SiO2have a weaker interaction with the support, resulting in a monotonic relationship between Mo loading and aldol condensation activity. The Lewis acid site density and strength are important parameters for predicting aldol condensation activity across all samples. The concentration of weak acid sites had a poor correlation with aldol condensation activity, most likely because these sites are too weak to activate acetaldehyde for the reaction. Medium and strong acid sites both had good correlations to aldol condensation activity. Results from X-ray absorption near edge structure (XANES) and acetaldehyde temperature programmed desorption (TPD) indicated that partially reduced MoOxwas more active for aldol condensation, but pretreatment in reducing or oxidizing environments had no significant effect on steady-state catalytic activity. Characterization of spent catalyst samples through temperature programmed oxidation (TPO) and thermogravimetric analysis (TGA) revealed that catalysts with high densities of strong acid sites tended to form more carbonaceous deposits on the surface over the course of the reaction.