Catalytic
upgrading of ethanol, as a platform molecule from biomass
to higher alcohols (C4–12), is a low-carbon route
for value-added chemical production. However, the products are generally
obtained in low selectivity due to the uncontrollable reactivity of
intermediates that cause a complex reaction network. In this study,
we show that unsaturated intermediates of aldehydes can be rapidly
hydrogenated by surface hydrogen species during the ethanol upgrading
process, thereby greatly inhibiting the cyclization reaction of aldehydes.
Specifically, the product distributions on the Cu-hydroxyapatite (Cu-HAP)
catalyst shift stepwise to higher alcohols from aromatic oxygenates
with the partial pressure of hydrogen increasing from 0 to 95 kPa.
Kinetic measurements and in situ ethanol infrared results indicated
that the intermediates during this process are acetaldehyde and 2-butenal.
Combined with physical structure and chemical state analysis of the
catalyst, we found that Cu sites catalyze the hydrogenation of the
CC bond of 2-butenal under a hydrogen atmosphere. The C–C
coupling of ethanol to higher alcohols over Cu-HAP follows the Guerbet
mechanism. In comparison, on bare HAP, n-butanol
is formed as a primary product even though little amount of acetaldehyde
was detected, indicating that ethanol proceeds mainly in a direct
coupling process to yield higher alcohols. This study introduces an
efficient ethanol valorization approach that is enabled by subtle
control of the intermediate conversion over the Cu-HAP catalyst by
the hydrogen partial pressure.