An
in-depth investigation of a dual homogeneous catalyst system
for the coupling of alkanes and alkenes based on an early-/late-transition-metal
pairing is reported. The system is composed of Cp*TaCl2(alkene) for alkene dimerization and pincer-iridium hydrides for
alkane/alkene transfer hydrogenation. Because there is no kinetically
relevant interaction between the two catalysts, the tandem mechanism
can be entirely described using the two independent catalytic cycles.
The alkene dimerization mechanism is characterized by an entropically
disfavored pre-equilibrium between Cp*TaCl2(1-hexene) +
1-hexene and Cp*TaCl2(metallacyclopentane) (ΔH° = −22(2) kcal/mol; ΔS° = −16(2) eu); thus, the overall rate of alkene dimerization
is positive order in 1-hexene (exhibiting saturation kinetics), and
increases only modestly with temperature. In contrast, the rate of
1-hexene/n-heptane transfer hydrogenation catalyzed
by t-Bu[PCP]IrH4 is inverse order in 1-hexene
and increases substantially with temperature. Styrene has been investigated
as an alternate sacrificial hydrogen acceptor. Styrene dimerization
catalyzed by Cp*TaCl2(alkene) is considerably slower than
1-hexene dimerization. The conversion of styrene/heptane mixtures
by the Ta/Ir tandem system leads to three product types: styrene dimers,
coupling of styrene and heptane, and heptene dimers (from heptane).
Through careful control of reaction conditions, the production of
heptene dimers can be favored, with up to 58% overall yield of heptane-derived
products and cooperative TONs of up to 12 and 10 for Ta and Ir catalysts,
respectively. There is only slight inhibition of Ir-catalyzed styrene/n-heptane transfer hydrogenation under the tandem catalysis
conditions.