Abstract

In heterogeneous catalysis, olefin oligomerization is typically performed on immobilized transition metal ions, such as Ni2+ and Cr3+. Here we report that silica-supported, single site catalysts containing immobilized, main group Zn2+ and Ga3+ ion sites catalyze ethylene and propylene oligomerization to an equilibrium distribution of linear olefins with rates similar to that of Ni2+. The molecular weight distribution of products formed on Zn2+ is similar to Ni2+, while Ga3+ forms higher molecular weight olefins. In situ spectroscopic and computational studies suggest that oligomerization unexpectedly occurs by the Cossee-Arlman mechanism via metal hydride and metal alkyl intermediates formed during olefin insertion and β-hydride elimination elementary steps. Initiation of the catalytic cycle is proposed to occur by heterolytic C-H dissociation of ethylene, which occurs at about 250 °C where oligomerization is catalytically relevant. This work illuminates new chemistry for main group metal catalysts with potential for development of new oligomerization processes.

Highlights

  • In heterogeneous catalysis, olefin oligomerization is typically performed on immobilized transition metal ions, such as Ni2+ and Cr3+

  • These results are consistent with previous single site structures reported for Ga3+, Zn2+, and Ni2+ hydrogenation and dehydrogenation catalysts[22,23,26,27]. These structures differ from organometallic catalysts where metal alkyls, like trimethylgallium, were grafted to a SiO2 support resulting in M–M bonds[28,29,30]

  • This work demonstrates that isolated, Ga3+ and Zn2+ ion sites on inert SiO2 support catalyze olefin oligomerization following the Cossee–Arlman mechanism which is generally accepted for transition metal catalysts

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Summary

Introduction

Olefin oligomerization is typically performed on immobilized transition metal ions, such as Ni2+ and Cr3+. Chevron Philips (Gulf) and others utilize similar catalysts under similar reaction conditions[6] Such homogeneous catalysts often require aluminum–alkyl cocatalysts to form the initial metal–alkyl reaction intermediate. Separation and regeneration of homogenous catalysts is generally not possible; there is interest in development of heterogeneous catalysts, which are readily separated from the products and can be regenerated The latter include immobilized Ni2+ sites on zeolite (BEA, MFI), or mesoporous aluminosilicates (MCM-41) and other high surface area oxide supports which sometimes generate Brønsted acid sites during the reaction, leading to bifunctional catalysis[10,12,13,14,15,16,17]. Ni-alkyl and hydrides are proposed key reaction intermediates, and olefin insertion and β-hydride elimination are the key elementary reaction steps, though limited spectroscopic evidence exists[18,19]

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