Abstract

We investigated the interactions between nickel oxide and silica–alumina supports, which were applied to the catalytic oligomerization of ethylene by powder X-ray diffraction, UV diffuse reflectance spectroscopy, H2 temperature-programmed reduction, and X-ray photoelectron spectroscopy. The catalytic activity was also correlated with the acidity of catalysts determined by NH3 temperature-programmed desorption and pyridine FT-IR spectroscopy. Although all the catalysts had similar Ni contents, their catalytic performances were strongly influenced by the strength of the metal oxide–support interaction. Strong interaction promoted the formation of nickel aluminate on the catalyst surface, and resulted in low catalytic activity due to reducing the amount of nickel oxide active sites. However, weak interaction favored the aggregation of nickel oxide species into larger particles, and thus resulted in low ethylene conversion and selectivity to oligomers. Eventually, the optimal activity was realized at the medium interaction strength, preserving a high amount of both active nickel oxides and acid sites.

Highlights

  • Biofuels and biochemicals have a great deal of interest because of global warming

  • The prepared catalysts were designated as nickel oxide supported on SAs (NiOx/SA)-001, -007, -028, -047, and -386, respectively, according to their

  • The activity and stability of oligomerization are most affected by mass transfer, the large pore sizes in several nanometers of these nickel oxide phase (NiOx)/SA catalysts may have no diffusion limitation problem

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Summary

Introduction

Biofuels and biochemicals have a great deal of interest because of global warming. Among them, bioethanol is one of the most abundant sustainable raw materials of biocarbon sources today [1].Bioethanol-derived ethylene could be widely used in the syntheses of transportation fuels, chemicals, polymer derivatives, etc. [1,2,3]. The heterogeneous oligomerization of ethylene has usually been attempted using Ni-based solid acid catalysts supported on several zeolites such as ZSM-5 [7,8,9,10], Y [11,12,13,14], beta [15], MCM-22 [13,16,17], and MCM-36 [16,17], and ordered mesoporous Al-SBA-15 [18,19], Al-MCM-48, and Al-MCM-41 [13,18,20,21,22,23,24]

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