Abstract

Modelling and optimization of chemical reactors require a good understanding of the reactions mechanism with the corresponding kinetic description. Therefore, high quality kinetic data are needed, which can be challenging to obtain, especially for fast and highly exothermic reactions such as the CO2 methanation. Traditionally, kinetic studies rely on measuring the exit gas composition (1 data point per species and experiment) using differential reactors with diluted catalyst beds and reactants to avoid temperature change. Therefore, an optically accessible catalytic channel reactor was designed, which allowed for the chance to gather spatially-resolved information on axial gas composition and catalyst surface temperature, specifically by means of a movable sampling capillary and shortwave infrared-thermography (SWIR), respectively. A catalyst coated plate was placed at the bottom of the channel, while a set of two quartz glass plates covers the top. In the current study 35 data points per gas species were collect for 1 experiment conducted under laminar flow conditions at 425 °C. Catalyst surface temperature determined via a SWIR camera was not influenced by polyatomic molecules partaking in the reaction and thus did not falsify the kinetic data. The catalyst mass distribution along the reactor axis was determined, enabling the development of a correct reactor model for kinetic parameter estimation and model discrimination.

Highlights

  • Kinetic data of heterogeneous catalyzed reactions are collected with small laboratory packed bed reactors either with or without gas recirculation

  • They are usually operated as differential reactors measuring the exit-gas composition under conditions where transport resistances are negligible

  • As the coating process might alter catalyst properties due to the addition of binder and solvent, the surfaces areas of the fresh ordered mesoporous alumina catalyst (OMA)-15Ni catalyst and the catalyst slurry used for the washcoating were analyzed

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Summary

Introduction

Kinetic data of heterogeneous catalyzed reactions are collected with small laboratory packed bed reactors either with or without gas recirculation. They are usually operated as differential reactors (i.e., conversion

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