Abstract

The transformation of sunflower oil (SO) and waste cooking oil (WCO) into green diesel over co-precipitated nickel–zirconia catalysts was studied. Two series of catalysts were prepared. The first series included catalysts with various Ni loadings prepared using zirconium oxy-chloride, whereas the second series included catalysts with 60–80 wt % Ni loading prepared using zirconium oxy-nitrate as zirconium source. The catalysts were characterized and evaluated in the transformation of SO into green diesel. The best catalysts were also evaluated for green diesel production using waste cooking oil. The catalysts performance for green diesel production is mainly governed by the Ni surface exposed, their acidity, and the reducibility of the ZrO2. These characteristics depend on the preparation method and the Zr salt used. The presence of chlorine in the catalysts drawn from the zirconium oxy-chloride results to catalysts with relatively low Ni surface, high acidity and hardly reduced ZrO2 phase. These characteristics lead to relatively low activity for green diesel production, whereas they favor high yields of wax esters. Ni-ZrO2 catalysts with Ni loading in the range 60–80 wt %, prepared by urea hydrothermal co-precipitation method using zirconium oxy-nitrate as ZrO2 precursor salt exhibited higher Ni surface, moderate acidity, and higher reducibility of ZrO2 phase. The latter catalysts were proved to be very promising for green diesel production.

Highlights

  • IntroductionCarbon dioxide emission is implicated for global warming due to the combustion of fossil fuels

  • Carbon dioxide emission is implicated for global warming due to the combustion of fossil fuels.On the other hand, the increasing demand for energy causes progressive depletion of oil reserves.the planet is facing a climate change and an energy crisis [1,2,3]

  • The performance of Ni-ZrO2 catalysts for green diesel production is mainly governed by the Ni surface exposed, their acidity, and the reducibility of the ZrO2 phase confirming the synergy between metallic Ni and oxygen defects in the ZrO2 surface

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Summary

Introduction

Carbon dioxide emission is implicated for global warming due to the combustion of fossil fuels. An increasing interest has emerged in recent years for developing non-sulphided nickel-based catalysts [13] This is because the noble metals are characterized by their high cost and limited availability, whereas using the conventional h.d.s catalysts an unwanted S-contamination of the produced green diesel is very probable [19]. High specific surface area mesoporous materials with very small nickel nanocrystals supported on small alumina nanograins and very active in the SDO of sunflower oil (SO) have been obtained [22]. These results encourage us to extend our study to co-precipitated nickel–zirconia catalysts. To the best of our knowledge, a study dealing with the SDO of SO and/or WCO over nickel–zirconia non-sulfided catalysts is not yet reported

Catalyst Preparation
First Series of Catalysts
80 Cwtand
Second Series of Catalysts
Inspection of this figure catalysts
Ni under the
15. Inspection thisthe figure clearly shows that the
Feedstock
Materials
Activation
Scanning Electron Microscopy
Determination of the Texture
X-ray Diffraction
X-ray Photoelectron Spectroscopy
Temperature Programmed Reduction
Acidity Measurements
Catalytic Tests
Chromatographic and GC-MS Analysis
Conclusions

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