Abstract

To study how calcination temperature influences the structural properties and catalytic performance of a novel amorphous NiP/Hβ catalyst, amorphous NiP/Hβ catalysts calcined at different temperatures were prepared for n-hexane isomerization. The optimum calcination temperature was determined, and the effect of calcination temperature on the structural properties of the catalysts was investigated using different characterization methods, such as XRD, TPD and so on. It was found that the optimum calcination temperature was 200 °C. Simultaneously, the amorphous NiP/Hβ catalyst showed good application potential as a non-noble metal catalyst. Calcination temperatures from 100 to 400 °C had almost no effect on pore properties. Meanwhile, the acid properties of the amorphous NiP/Hβ catalyst were affected very little by calcination temperature. By increasing calcination temperature, the dispersion state of amorphous NiP became worse at 300 °C, and then the structure of NiP changed from an amorphous structure into a crystalline structure at 400 °C. In addition, the catalyst became more difficult to reduce with the increase in calcination temperature. Combined with the results of n-hexane isomerization catalyzed by different samples, the mechanism by which calcination temperature affects n-hexane isomerization over catalyst was revealed. It was shown that for the amorphous NiP/Hβ catalyst, calcination temperature influences the catalytic performance mainly by affecting the dispersion degree and structure of active components.

Highlights

  • In recent years, the isomerization of light alkanes has had an increasingly significant effect on improving the octane number of gasoline [1,2,3,4,5]

  • Nitrogen adsorption isotherms for 10 wt% NiP/Hβ calcined at different temperatures are displayed

  • Nitrogen adsorption isotherms for 10 wt% NiP/Hβ calcined at different temperatures are displayed in Figure 1, which show similar configurations and belong to the type I+IV isotherm

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Summary

Introduction

The isomerization of light alkanes has had an increasingly significant effect on improving the octane number of gasoline [1,2,3,4,5]. Cleaner production has attracted more and more attention in various fields [10,11]. Bifunctional metal/acid catalysts are extensively applied in the isomerization of light alkanes, and their active components are usually noble metals such as Pt and Pd [12,13,14,15,16]. Because of the existence of noble metals, the cost of catalysts is high, and their sulfur resistance is poor. Research into non-noble metal catalysts has attracted a lot of attention [17,18]

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