Kinetics of Oxidative Cracking of n‐Hexane to Light Olefins using Lattice Oxygen of a VO_x/SrO‐γAl₂O₃ Catalyst

Abstract

Abstract The kinetics of oxidative cracking of n‐hexane to light olefins using the lattice oxygen of VO x /SrO‐γAl 2 O 3 catalysts has been investigated. Kinetic experiments were conducted in a CREC Riser Simulator (CERC: Chemical Reactor Engineering Center), which mimics fluidized bed reactors. The catalyst's performance is partly attributed to the moderate interaction between active VO x species and the SrO‐γAl 2 O 3 support. This moderate interaction serves to control the release of lattice oxygen to curtail deep oxidation. The incorporation of basic SrO component in the support also helped to moderate the catalyst's acidity to checkmate excessive cracking. Langmuir‐Hinshelwood model was applied to formulate the rate equations. The intrinsic kinetic parameters were obtained by fitting the experimental data to the kinetic model using a nonlinear regression algorithm at a 95% confidence interval, implemented in MATLAB. n ‐Hexane transforms to olefins at a specific reaction rate of 1.33 mol/gcat.s and activation energy of 119.2 kJ/mol. These values when compared with other duplets (i. e., ki° and E A ) for paraffins to olefins, show that indeed olefins are stable products of the oxidative conversion of n ‐hexane over VO x /SrO‐γAl 2 O 3 under a fluidized bed condition. Values of activation energy for all CO x formation routes indicate that intermediate paraffins are likely to be cracked to form CH 4 than to be converted directly to CO x . On the other hand, olefins may transform partly, and directly to CO x (E 9 =9.65 kJ/mol) than to form CH 4 (E 8 =89.1 kJ/mol) in the presence of excess lattice oxygen. Overall, olefins appear to be stable to deep oxidation due to the role of SrO in controlling the amount of lattice oxygen of the catalyst at the reaction temperature.

Topics & Concepts