Boron-based nonmetallic materials (such as B2O3 and BN) emerge as promising catalysts for selective
oxidation of
light alkanes by O2 to form value-added products, resulting
from their unique advantage in suppressing CO2 formation.
However, the site requirements and reaction mechanism of these boron-based
catalysts are still in vigorous debate, especially for methane (the
most stable and abundant alkane). Here, we show that hexagonal BN
(h-BN) exhibits high selectivities to formaldehyde
and CO in catalyzing aerobic oxidation of methane, similar to Al2O3-supported B2O3 catalysts,
while h-BN requires an extra induction period to
reach a steady state. According to various structural characterizations,
we find that active boron oxide species are gradually formed in situ
on the surface of h-BN, which accounts for the observed
induction period. Unexpectedly, kinetic studies on the effects of
void space, catalyst loading, and methane conversion all indicate
that h-BN merely acts as a radical generator to induce
gas-phase radical reactions of methane oxidation, in contrast to the
predominant surface reactions on B2O3/Al2O3 catalysts. Consequently, a revised kinetic model
is developed to accurately describe the gas-phase radical feature
of methane oxidation over h-BN. With the aid of in
situ synchrotron vacuum ultraviolet photoionization mass spectroscopy,
the methyl radical (CH3
•) is further
verified as the primary reactive species that triggers the gas-phase
methane oxidation network. Theoretical calculations elucidate that
the moderate H-abstraction ability of predominant CH3
• and CH3OO• radicals renders
an easier control of the methane oxidation selectivity compared to
other oxygen-containing radicals generally proposed for such processes,
bringing deeper understanding of the excellent anti-overoxidation
ability of boron-based catalysts.