α-Olefin trimers are used at a bulk scale as top-tier
lubricant
base oils, with putative future applications as diesel fuels obtainable
from renewable ethylene. α-Olefin trimers are conventionally
obtained in the cationic oligomerization process, during which a range
of n-mers are simultaneously generated alongside
severe skeleton rearrangement. In this context, catalysts that can
selectively convert α-olefin to its trimers are valuable. However,
few examples have been reported. Herein, we report selective α-olefin
trimerization catalysts constructed via the modification of the Chevron–Phillips
ethylene trimerization catalytic system and avoiding the use of expensive
activators, such as methylaluminoxane (MAO), B(C6F5)3, and [B(C6F5)4]− salt, despite the typical Chevron–Phillips
system being inactive for α-olefin. A catalytic system Cr(acac)3/[2,5-Me2C4H2N–Al(iBu)3]−Na+/(iBu)3Al demonstrating
high turnover numbers exceeding 10,000 (31 kg/g-Cr for 1-decene),
generating trimers selectively without other higher or lower fractions,
was developed, confirmed by simulated distillation gas chromatography
analysis. The hypothesized η5-pyrrolide chromium
active species was partially confirmed by the structure elucidation
of [η5-Me2C4H2N–AlMe3]Cr(Me)[CH2C6H4(ortho-NMe2)-κ2
C,N]. The prepared 1-decene trimers (after hydrogenation) exhibited
an advantageously higher viscosity index than the commercial product
PAO-4.0 (128 vs 123). Fluids demonstrating similar lubricant characteristics
to either the 1-decene trimers or PAO-4.0 were obtained by using a
1-octene/1-dodecene blend.