Abstract
Abstract: We have examined the role of support oxygen vacancies in the gas phase hydrogenation of furfural over Au/TiO2 and Au/CeO2 prepared by deposition–precipitation. Both catalysts exhibited a similar Au particle size distribution (1–6 nm) and mean (2.8–3.2 nm). Excess H2 consumption during TPR is indicative of partial support reduction, which was confirmed by O2 titration. Gold on CeO2 with a higher redox potential exhibited a greater oxygen vacancy density. A lower furfural turnover frequency (TOF) was recorded over Au/CeO2 than Au/TiO2 and is linked to suppressed H2 chemisorption capacity and strong –C=O interaction at oxygen vacancies that inhibited activity. Gold on non-reducible Al2O3 as benchmark exhibited greater H2 uptake and delivered the highest furfural TOF. Full selectivity to the target furfuryl alcohol was achieved over Au/TiO2 and Au/Al2O3 at 413 K and over Au/CeO2 at 473 K with hydrogenolysis to 2-methylfuran at higher reaction temperature (523 K). A surface reaction mechanism is proposed to account for the activity/selectivity response. Graphical Abstract: [Figure not available: see fulltext.]
Original language | English |
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Pages (from-to) | 1-7 |
Number of pages | 7 |
Journal | Catalysis Letters |
Early online date | 23 Oct 2017 |
DOIs | |
Publication status | E-pub ahead of print - 23 Oct 2017 |
Keywords
- Furfural
- Furfuryl alcohol
- Oxygen vacancies
- Selective hydrogenation
- Supported Au
ASJC Scopus subject areas
- Catalysis
- General Chemistry
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Fernando Cardenas-Lizana
- School of Engineering & Physical Sciences - Assistant Professor
- School of Engineering & Physical Sciences, Institute of Mechanical, Process & Energy Engineering - Assistant Professor
Person: Academic (Research & Teaching)