Both
alkyl esters and γ-valerolactone (GVL) derived from
levulinic acid (LA) have applications as renewable transportation
fuel/fuel additives. Non-noble metal cobalt supported on La2O3 catalyst was developed for efficient cascade LA hydrogenation
to GVL via esterification. LA hydrogenation in methanol alone yielded
methyl levulinate (MeLA) as a major product along with 43% of GVL.
Interestingly, hydrogenation in water gave almost complete selectivity
to GVL; nevertheless, it was associated with significant metal leaching.
Suppression of metal leaching and enhancement in selectivity to GVL
could be achieved by a methanol/water (95:5) solvent system. XRD analysis
of La2O3-supported catalysts evidenced the characteristic
peaks of a mixture of La2O3 and La(OH)3 phases. Basicity, as well as acidity, of the catalyst as determined
by CO2 and NH3 TPD was due to these La2O3, Co–La, and La(OH)3 phases which
played an important role in directing the product selectivity in levulinic
acid hydrogenation. At the low temperature of 160 °C, almost
equal selectivities of MeLA (47%) and GVL (43%) were observed, while
higher temperature (200 °C) favored further hydrogenation of
MeLA to GVL (75%). Similarly, with an increase in reaction time to
9 h, the GVL selectivity achieved was as high as 80%. The selectivity
to MeLA and GVL in LA hydrogenation over Co/La2O3 catalyst can be altered by suitably adjusting the reaction conditions.