Universal oxygen removal of depolymerized lignin molecules
is a
desirable route to funnel complex mixtures of bioderived molecules
to high-demand “drop-in” petrochemical intermediates
(aromatics and alkenes). Molybdenum oxide-based catalysts are of great
interest for this valorization strategy, as they have shown proficiency
in removing a wide range of oxygen functionalities without excess
hydrogen consumption or aromatic ring saturation. Despite these advantages,
MoO3 has demonstrated a propensity to saturate aliphatic
molecules to low-value alkanes during deoxygenation, decreasing the
economic potential of the conversion process. To better inform mitigation
strategies, detailed kinetic experiments were applied to various alcohol-,
aldehyde-, and ketone-containing model compounds to infer potential
reaction pathways and mechanisms for forming alkene and alkane products.
Consistent differences in product distribution, reaction rates, oxygenate,
and H2 orders were observed to exist between carbonyls
and their alcohol analogs, allowing for the determination that the
hydrogenation of carbonyls to alcohols is required and kinetically
limiting for HDO on MoO3. It is also proposed that carbonyls
competitively adsorb at hydrogenation-active hydroxyl species, leading
to aldol condensation reactions and a negative carbonyl order for
the rate of HDO. Once adsorbed/formed on oxygen vacancies, MoO3 likely mediates hetero- and homolytic cleavage of alcohol
C–O bonds to create a combination of carbocation and free radical
intermediates. Both intermediates can then proceed through a dehydration
or hydrogenolysis pathway to directly form alkenes or alkanes, respectively,
at varying rates depending on the stabilization of the reactive carbon
by electron-donating constituents. This effect led to primary oxygen
functional groups yielding the lowest initial selectivity to alkenes
(∼50%). Further, kinetic analysis of cyclohexene and 1-pentene
feeds showed that alkenes weakly adsorb onto HDO-active oxygen vacancies
to undergo a sequential hydrogenation reaction. This low adsorption
strength of alkenes relative to those of oxygen-containing molecules
prevents further conversion of the initial HDO products.