Most
industrial hydrogenation processes are conducted under elevated
temperature and pressure. Catalytic transfer hydrogenation/hydrogenolysis,
in the absence of externally added hydrogen, is known to be much more
energy efficient and atom economical. However, the multifunctional
nature of catalyst structure on simultaneous hydrogen generation,
hydrogen transfer, and hydrogenation reactions is largely unexplored.
We reported a design principle and size-dependent behavior of bimetallic
PtPd/C catalysts for transfer hydrogenolysis of bioderived polyols
to renewable glycols as an illustrative example. The central finding
in this work is that, while kinetics of partial dehydrogenation (C–H
cleavage) display size insensitivity, reforming (C–C cleavage)
and hydrogenolysis (C–O cleavage) reactions show strong size-determining
activity and selectivity in the range of 2.0 to 5.3 nm. The synergistic
PtPd/C catalysts lead to a remarkable selectivity of 87% for value-added
glycols and derivatives even under an inert atmosphere. The outcome
from this fundamental study will provide insights into the structural
design of next-generation solid catalysts for energy efficient hydrogenation
processes.