A mechanistic study of a rhenium
catalyzed monoalkylation of phenols
is described. Reaction kinetics reveals a zero-order dependence on
both alkene and phenol and a half order dependence on catalyst. Isotopic
labeling studies, competition experiments, kinetic isotope effects,
and Hammett analysis together afford experimental data consistent
with a reversible C–H activation step and an irreversible hydrometalation
process. The turnover-limiting step is identified as catalyst deaggregation.
NMR studies of binary mixtures of catalyst and a single substrate
(alkene or phenol) as well as those of reaction mixtures identify
potential intermediates and off-cycle species. Despite the numerous
Re complexes formed in these mixtures, the overall reaction is both
high yielding and highly selective for monoalkylation of phenols.