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Methane aromatization study on M-Mo2C/HZSM-5 (M = Ce or Pd or Nb) nano materials

Nagaraju Pasupulety, Abdulla Yahya Abdullah Alzahrani, Muhammad A. Daous, Hafedh Driss, L. Petrov

2021Journal of Materials Research and Technology15 citationsDOIOpen Access PDF

Abstract

The aim of this work is to understand the influence of second metals (M = Ce or Pd or Nb) on Mo 2 C active phase reduction into metallic molybdenum and on surface MoO x species of M-Mo 2 C/HZSM-5 catalysts studied for methane dehydroaromatization at 700 °C with GHSV 1800 mL. g cat −1 . h −1 . The fresh and spent catalysts were characterized by using ATR-FTIR, HRTEM/STEM, BET surface area , XRD , TPO, NH 3 -TPD-mass, XPS and H 2 -TPR techniques. Essentially, the highest benzene yield of 8.4% on Pd–Mo 2 C/HZSM-5 catalyst for 10 h of continuous operation was associated with limited Mo 2 C active phase reduction into metallic molybdenum at Pd–Mo proximity via Pd 2+ to Pd 0 step and promoted coke burning through reduced carbon deposits formation. Further, the surface reduction of CeO 2 to Ce 2 O 3 decreased the methane conversion due to sluggish MoO x species transformation to Mo 2 C active phase. On the other side, Nb 2 O 5 primarily reduced into NbO 2 /NbO resulted in surface MoO x species and external surface Mo 2 C particles eventually produced superior coke via CH 4 decomposition on Nb–Mo 2 C/HZSM-5 catalyst. The decreasing order of benzene yield after 10 h of reaction at 700 °C as follows: Pd–Mo 2 C/HZSM-5 (8.4%) > Mo 2 C/HZSM-5 (7.4%) > Nb–Mo 2 C/HZSM-5 (5.8%) > Ce–Mo 2 C/HZSM-5 (5.2%).

Topics & Concepts

CatalysisMolybdenumMaterials scienceBenzeneX-ray photoelectron spectroscopyMethaneMetalSpace velocityInorganic chemistryDecompositionCokeNuclear chemistryChemistrySelectivityChemical engineeringMetallurgyOrganic chemistryEngineeringCatalytic Processes in Materials ScienceZeolite Catalysis and SynthesisCatalysis and Hydrodesulfurization Studies
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