4.6 Article

Origin of Morphology Change and Effect of Crystallization Time and Si/Al Ratio during Synthesis of Zeolite ZSM-5

Journal

CHEMCATCHEM
Volume 14, Issue 3, Pages -

Publisher

WILEY-V C H VERLAG GMBH
DOI: 10.1002/cctc.202101248

Keywords

Kinetics; Mechanism of crystallization; Zeolite morphology; Zeolite synthesis; ZSM-5

Funding

  1. German Federal Ministry for Education and Research (BMBF) within the directive Client-II International Partnerships for Sustainable Innovation by FONA3 [033R188A]
  2. Studienstiftung des Deutsches Volkes
  3. Saxony Scholarship Program
  4. Projekt DEAL

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This article focuses on the relationship between Si/Al ratio and zeolite morphology of microporous ZSM-5 and analyzes the impact of this relationship on the synthesis process. The results show that with an increasing Si/Al ratio, the solid-state transformation accelerates and the morphology shifts from small clusters to larger spherical particles. The acid site density and zeolite morphology determine the selectivity during methanol conversion.
Hydrothermal synthesis of ZSM-5 is an often applied but incompletely understood procedure. In comparison to current research efforts that aim to produce complex micro-mesoporous catalysts for the conversion of biogenic and bulky hydrocarbons, this work focuses on the dependency between Si/Al ratio and zeolite morphology of microporous ZSM-5 to understand and to control the synthesis process. In two series of time dependent crystallization, kinetics were analyzed at Si/Al ratio 20 and 100 to optimize the crystallization time. Subsequently, zeolites with different Si/Al ratio were obtained and characterized. The results show a transition from a slow dissolution-recrystallization process to a fast solid-state-transformation with increasing Si/Al ratio. This is followed by a switching morphology from clusters of small agglomerates to bigger spherical particles. Respective acid site density and zeolite morphology determine local residence time, hydride transfer behavior and finally selectivity towards aromatics and higher hydrocarbons during methanol conversion. This background should provide control of even more complex syntheses of porous catalysts.

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