Methanol to olefins
(MTO) reaction over H-RUB-50 zeolite, an eight-membered
ring (8-MR) and cavity-type zeolite, presents higher selectivity for
ethene. The host–guest interaction was dissected and used to
explain the cavity-controlled reaction route and product selectivity.
By the aid of the in situ 13C MAS NMR spectroscopy, GC-MS, 12C/13C-methanol switch experiments, and theoretical
calculations, the methylbenzenium cations, methylcyclopentenyl cations
(triMB+, tetraMB+, and triMCP+),
and their deprotonated forms with less methyl groups substitution
were captured over LEV zeolite and confirmed as the critical reaction
intermediates. The energetic span model was employed to identify the
preferred reaction mechanism and provide the theoretical evidence
to understand product selectivity. The side-chain methylation mechanism
was theoretically predicated to be the energetically favorable route
for olefins generation with the participation of these active intermediates.
Paring cycle with trimethlycyclopentadienyl cation as the intermediate
makes less contribution to ethene formation due to the relatively
large energy span. Based on the overall evaluation of the catalytic
cycle, the difference of energy span of the whole reaction pathway
for ethene and propene formation can give direct theoretical evidence
for product selectivity. Additional study to the steps for generating
precursors of ethene and propene offers extra support on the understanding
of product selectivity and the dominant generation of ethene. This
study captured the critical intermediates and established a rational
and energetically feasible route of light olefins generation from
MTO reaction over H-RUB-50. More importantly, it is exhibited that
cavity controls the product selectivity via the important steric constraint
for the formation of critical intermediates and the proceeding of
critical reaction steps, based on the understanding of the host–guest
interaction of the cavity-type zeolite catalyzed MTO reaction.