4.6 Article

Reaction regeneration cycle of Mo/HZSM-5 catalyst in methane dehydroaromatization with the addition of oxygen-containing components

期刊

APPLIED CATALYSIS A-GENERAL
卷 647, 期 -, 页码 -

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ELSEVIER
DOI: 10.1016/j.apcata.2022.118916

关键词

Methane dehydroaromatization; Mo; H-ZSM-5 catalyst; Reaction regeneration; Deactivation; Oxygen-containing components

资金

  1. project of Liaoning Province Natural Science Fund Project, China
  2. [LJKZ0298]

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The study investigated the impact of oxygen-containing gas components on the reaction regeneration cycle of methane dehydroaromatization (MDA). The results indicated that the addition of oxygen components can prolong the reaction time but cannot prevent the deactivation of the regenerated catalyst. After regeneration, the species and texture properties of the catalyst were restored, leading to complete recovery of methane conversion and aromatic formation. However, the increase in the size of Mo species during regeneration disrupted carbon deposition and significantly reduced methane dissociation. The crystallinity and number of strong acid sites of the catalyst decreased to a stable level before the collapse of the zeolite framework, without hindering aromatic formation. The recovered large-sized Mo species may accelerate the irreversible collapse of the zeolite framework, thereby destroying the Mo/HZSM-5 catalyst.
Reaction regeneration cycle of methane dehydroaromatization (MDA) with oxygen-containing gas components was studied. XRD, BET, Raman, NH3-TPD, O2-TG/DTG, TEM and 27Al-NMR were used to monitor textural structure, Mo species, and acid sites of catalyst before and after regeneration. Addition of oxygen components can extend reaction time per pass but cannot prevent the deactivation of regenerated catalyst. MoO3 species, acidity, and texture properties of Mo/HZSM-5 was identical after first regeneration, which may account for complete recovery of methane conversion and aromatic formation. During regeneration, the inevitable increase in Mo species size disrupts carbon deposition and significantly reduces methane dissociation. The crystallinity and number of strong acid sites of Mo/HZSM-5 catalyst decreased to a stable level before the collapse of zeolite framework without hindering aromatic formation. The recovered large-sized Mo species may accelerate the collapse of zeolite framework, irreversibly destroying Mo/HZSM-5 catalyst.

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