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Enhancement of hydrodeoxygenation catalytic performance through the addition of copper to molybdenum oxide-based catalysts
•Bulk and supported molybdenum catalysts show high selectivity for benzene (∼ 100%).•The carbon support promotes the reduction of molybdenum even under an N2 atmosphere.•Both carbon support and the addition of copper favor phenol conversion.•CuMo/C is the most active and selective catalyst for HDO o...
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Published in: | Molecular catalysis 2023-02, Vol.536, p.112882, Article 112882 |
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Main Authors: | , , , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
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Summary: | •Bulk and supported molybdenum catalysts show high selectivity for benzene (∼ 100%).•The carbon support promotes the reduction of molybdenum even under an N2 atmosphere.•Both carbon support and the addition of copper favor phenol conversion.•CuMo/C is the most active and selective catalyst for HDO of phenol.•A correlation between the HDO rate and the number of oxygen vacancies is observed.
The role of copper promoter and carbon support on the activity, selectivity, and stability of molybdenum oxide was determined for bulk and carbon-supported molybdenum oxide catalysts in phenol hydrodeoxygenation (HDO). The catalytic performance was correlated to the physicochemical properties determined using ICP-AES, XRD, XPS, Raman, TPR, H2O-TPD, and oxygen chemisorption. The results showed that at the studied reaction conditions (atmospheric pressure, 330 ºC, gas phase), the employment of activated carbon as support and the addition of copper improved phenol conversion from 1 (with MoO3) to 28% (with CuMo/C), maintaining high selectivity to benzene (around 100%) while characterization studies evidence the formation of mainly CuMoO4 species in bulk samples and metallic copper, Cu2O, and MoO2 on carbon-supported ones. The incorporation of copper in the molybdenum oxide catalysis promoted the reduction of molybdenum, the creation of oxygen vacancies, and the H• formation, all factors favoring the selective CO bond cleavage. Stability tests of the most active catalysts, Mo/C_H2 and CuMo_H2, showed that deactivation happened, but the direct deoxygenation route remained preferential throughout the reaction time with high selectivity to benzene (up to 98%). Deactivation was related to the lower concentration of available active sites (oxygen vacancies).
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ISSN: | 2468-8231 2468-8231 |
DOI: | 10.1016/j.mcat.2022.112882 |