Research Advances in Zeolites and Zeolite-Based Catalysts

A special issue of Catalysts (ISSN 2073-4344). This special issue belongs to the section "Catalytic Materials".

Deadline for manuscript submissions: 20 September 2024 | Viewed by 617

Special Issue Editor


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Guest Editor
Department of Chemical Engineering, Instituto Superior de Engenharia de Lisboa, Instituto Politécnico de Lisboa, 1950-007 Lisboa, Portugal
Interests: heterogeneous catalysis; zeolites; hierarchical zeolites; bifunctional catalysts; carbon materials; porous silicas
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Special Issue Information

Dear Colleagues,

Zeolites are a class of crystalline inorganic materials with a wide range of applications in molecular separation and adsorption, and especially, as heterogeneous catalysts or catalyst supports. The microporous nature of these materials can act as microreactors, where the native active sites or introduced species, such as metals, promote the occurrence of catalytic reactions. However, the small size of the pores can also hinder the access of larger molecules, making the development of a secondary pore system, generally mesopores, through synthesis or post-synthesis strategies, a very appelaing pathway to broaden the application of these materials.

The aim of this Special Issue is to begin the discussion concerning the synthesis, modification, and functionalization of zeolites, aiming to prepare innovative and effective catalysts or catalyst supports for heterogeneous catalytic reactions.

Dr. Angela Martins
Guest Editor

Manuscript Submission Information

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Submitted manuscripts should not have been published previously, nor be under consideration for publication elsewhere (except conference proceedings papers). All manuscripts are thoroughly refereed through a single-blind peer-review process. A guide for authors and other relevant information for submission of manuscripts is available on the Instructions for Authors page. Catalysts is an international peer-reviewed open access monthly journal published by MDPI.

Please visit the Instructions for Authors page before submitting a manuscript. The Article Processing Charge (APC) for publication in this open access journal is 2700 CHF (Swiss Francs). Submitted papers should be well formatted and use good English. Authors may use MDPI's English editing service prior to publication or during author revisions.

Keywords

  • zeolites
  • hierarchical zeolites
  • synthesis and post-synthesis modification strategies
  • heterogeneous catalysts
  • metal-loaded zeolites

Published Papers (1 paper)

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16 pages, 4774 KiB  
Article
Pt3Mn/SiO2 + ZSM-5 Bifunctional Catalyst for Ethane Dehydroaromatization
by Shan Jiang, Che-Wei Chang, William A. Swann, Christina W. Li and Jeffrey T. Miller
Catalysts 2024, 14(6), 365; https://0-doi-org.brum.beds.ac.uk/10.3390/catal14060365 - 4 Jun 2024
Viewed by 436
Abstract
Ethane dehydroaromatization (EDA) is a potentially attractive process for converting ethane to valuable aromatics such as benzene, toluene, and xylene (BTX). In this study, a Pt3Mn/SiO2 + ZSM-5 bifunctional catalyst was used to investigate the effect of dehydrogenation and the [...] Read more.
Ethane dehydroaromatization (EDA) is a potentially attractive process for converting ethane to valuable aromatics such as benzene, toluene, and xylene (BTX). In this study, a Pt3Mn/SiO2 + ZSM-5 bifunctional catalyst was used to investigate the effect of dehydrogenation and the Brønsted acid catalyst ratio, hydrogen partial pressure, and reaction temperature on the product distributions for EDA. Pt3Mn/SiO2 + ZSM-5 with a 1/1 weight ratio showed the highest ethane conversion rate and BTX formation rate. Ethylene is initially formed by dehydrogenation by the Pt3Mn catalyst, which undergoes secondary reactions on ZSM-5, forming C3+ reaction intermediates. The latter form final products of CH4 and BTX. At conversions from 15 to 30%, the BTX selectivities are 82–90%. For all bifunctional catalysts, the ethane conversion significantly exceeds the ethane–ethylene equilibrium conversion due to reaction to secondary products. Low H2 partial pressures did not significantly alter the product selectivity or conversion. However, higher H2 partial pressures resulted in increased methane and decreased BTX selectivity. The excess hydrogen saturated the olefin intermediates to form alkanes, which produced methane by monomolecular cracking on ZSM-5. With an increasing reaction temperature from 550 °C to 650 °C, the benzene selectivity increased, while the highest BTX selectivity was obtained at 600 to 650 °C. Full article
(This article belongs to the Special Issue Research Advances in Zeolites and Zeolite-Based Catalysts)
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