Abstract

Heterogeneous catalysts for production of linear α-olefins from ethylene were prepared by the direct reaction of the α-diimine ligand [L: R-N=C(R')-C(R')=N-R; R' = Me and R = 2,6-Me2Ph (L5), 2,5-Me2Ph (L1), 2-MePh (L2), or Ph (L3); R' = 1,8-naphth-diyl and R = Ph (L4)] and Ni2+ ion-exchanged fluorotetrasilicic mica. Only high molecular weight polyethylene was obtained in the reaction using the L5/Ni2+-Mica procatalyst activated by AlEt3 (TEA) as an activator, whereas the TEA-activated L1- and L2/Ni2+-Mica procatalysts afforded a mixture of a large amount of low-molecular weight polyethylene and a small amount of oligomers having 4-22 carbons. The procatalyst consisting of Ni2+-Mica and the L3 ligand that possesses non-substituted phenyl groups on the iminonitrogen atoms effectively promoted the oligomerization of ethylene after its activation with TEA, resulting in the fact that the ethylene oligomers were produced with a moderate catalytic activity (101 g-ethylene g-cat−1 h−1 at 0.7 MPa-ethylene) in the presence of TEA. When the backbone was varied from the butane moiety (L3) to acenaphthene (L4), the solid product dramatically increased. The weight percentage of the oligomers in the total products increased with the increasing reaction temperature; however, an insignificant increase in the oligomers was observed when the ethylene pressure was decreased.

Highlights

  • Introduction αOlefins of carbon number 4–20 are important basic products in the chemical industry, and these are used as the comonomer in the ethylene/α-olefin copolymerization, the raw material of long-chain alcohols, and the base material of synthetic lubricant oil [1,2]

  • We developed new heterogeneous catalysts, which were prepared through the intercalation of the ligand into the late transition-metal ion exchanged clay mineral, and the coordination of the bis(imono)pyridine or α-diimine ligand to the interlayer metal ion; these catalysts showed a high activity for the polymerization of ethylene in the presence of MAO, and alkyl aluminum compounds [14,15]

  • Our previous report indicated that the procatalyst prepared from the Ni2+-Mica and the ligand L5 having 2,6-dimethylphenyl groups on the iminonitrogen atoms [Ph'-N=C(Me)-C(Me)=N-Ph', Ph' = 2,6-Me2Ph] afforded both a high catalytic activity and high molecular-weight polyethylene that included methyl branches formed by the “chain walking” mechanism [15]

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Summary

Results and Discussion

The effects of the reaction temperature and ethylene pressure on the productivity of the oligomers were investigated using the L3/Ni2+-Mica procatalyst When the temperature was raised from 50 °C to higher temperatures (Runs 3, 5, and 6), the productivity dramatically decreased with the increasing weight ratio of the C4–C22 products to total products This increasing ratio of the oligomers is due to the relative increase in the rate of the chain transfer reaction to the rate of the propagation, and this trend is in good agreement with the trends observed for the ethylene polymerization using other polymerization catalysts. This difference was due to the weaker reactivity of TIBA than that of TEA

Characterization of Procatalysts
Experimental Section
Ligand Synthesis
Procatalyst Preparation
Characterization of Procatalyst
Ethylene Oligomerization
Conclusions
Full Text
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