Abstract

A commercial heterogeneous Ni–Mo/Al2O3 catalyst was tested for the oxidative dehydrogenation (ODH) reaction of n-butane with different oxidant species: O2, CO2 and N2O.

Highlights

  • One of the main tasks of the chemical industry today is the production of large amounts of organic compounds.[1]

  • Selectivity towards BD was low, while the amount of CO2 formed increases with temperature, which may be due to the increase of coke deposition at lower oxygen-to-butane molar ratios.[2]

  • At lower oxygento-butane molar ratios, more oxygen is used to burn the coke deposited on the catalyst surface, leaving no oxygen available for oxidative dehydrogenation (ODH)

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Summary

Introduction

One of the main tasks of the chemical industry today is the production of large amounts of organic compounds.[1]. NiMoO4 shows potential for ODH of lighter paraffins, ethane, propane and n-butane.[8,14]

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