Abstract

A novel approach to the in situ regeneration of a spent alumina-supported cobalt–iron catalyst for catalytic methane decomposition is reported in this work. The spent catalyst was obtained after testing fresh catalyst in catalytic methane decomposition reaction during 90 min. The regeneration evaluated the effect of forced periodic cycling; the cycles of regeneration were performed in situ at 700 °C under diluted O2 gasifying agent (10% O2/N2), followed by inert treatment under N2. The obtained regenerated catalysts at different cycles were tested again in catalytic methane decomposition reaction. Fresh, spent, and spent/regenerated materials were characterized using X-ray powder diffraction (XRD), transmission electron microscopy (TEM), laser Raman spectroscopy (LRS), N2-physisorption, H2-temperature programmed reduction (H2-TPR), thermogravimetric analysis (TGA), and atomic absorption spectroscopy (AAS). The comparison of transmission electron microscope and X-ray powder diffraction characterizations of spent and spent/regenerated catalysts showed the formation of a significant amount of carbon on the surface with a densification of catalyst particles after each catalytic methane decomposition reaction preceded by regeneration. The activity results confirm that the methane decomposition after regeneration cycles leads to a permanent deactivation of catalysts certainly provoked by the coke deposition. Indeed, it is likely that some active iron sites cannot be regenerated totally despite the forced periodic cycling.

Highlights

  • The reduction of catalytic activity over time is an issue of considerable and continuing concern in industrial practices of catalytic processes

  • This study focused on identifying the nature of the carbon deposits formed after each catalytic methane decomposition (CMD) testing that precedes the regeneration cycles; in addition, the obtained yields of hydrogen were quantified to understand the reaction’s mechanism

  • Because of the materials’ complexity, structural and textural properties and morphology of spent/regenerated catalysts were examined using X-ray diffraction (XRD), transmission electron microscopy (TEM), laser Raman spectroscopy (LRS), N2 -physisorption, hydrogen temperature programmed reduction (H2 -TPR), and thermogravimetric analysis (TGA), and the carbon amount was evaluated by atomic absorption spectrometry (AAS)

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Summary

Introduction

The reduction of catalytic activity over time is an issue of considerable and continuing concern in industrial practices of catalytic processes. Catalyst replacement and process shutdown could cost the industry very large financial resources every year. The catalyst deactivation changes extensively; for example, in the case of catalytic methane decomposition, catalyst deterioration may be on the scale of seconds, whereas in NH3 synthesis the Fe-catalyst may stay for 5–10 years. It is unavoidable that all catalysts drop their activities. Hydrogen is a pure fuel source which can replace fossil fuels. It can be utilized to run numerous devices like fuel cells, engines, vehicles, and electric devices [1].

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