Advances in Zeolite Catalytic Processes: Current Trends and Challenges in Processing Nonconventional Feedstocks

A special issue of Processes (ISSN 2227-9717). This special issue belongs to the section "Chemical Processes and Systems".

Deadline for manuscript submissions: 15 July 2025 | Viewed by 1461

Special Issue Editors


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Guest Editor
Instituto de Investigaciones en Catálisis y Petroquímica, Santa Fe, Argentina
Interests: porous catalytic materials; sustainable catalytic processes; diffusion-adsorption-reaction in porous materials; added-value chemicals (fuels, aromatics, olefins, oxygenated); non-conventional feedstocks (fossil, biomass, waste plastics)

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Guest Editor
Instituto de Investigaciones en Catálisis y Petroquímica, Santa Fe 3000, Argentina
Interests: zeolites synthesis; characterization of acid sites; dehydration reactions; alkylation and acylation reactions

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Guest Editor
Centro de Investigación y Tecnología Química, Córdoba 5000, Argentina
Interests: zeolites; porous materials; pyrolysis; advanced oxidation processes

Special Issue Information

Dear Colleagues,

For several decades, a significant number of industrial processes involving separation operations and/or solid-catalyzed reactions have used zeolites as adsorbents as well as catalysts or catalytic supports. Many types of zeolites were developed and used for industrial applications, ranging from their early use in petroleum refineries to their more recent use in environmentally friendly, sustainable chemical processes.

Depending on the catalytic reaction involved, a specific zeolite catalyst can be selected. The three key characteristics of the zeolites—acidity, shape selectivity, and loading property—are responsible for their good performance as catalysts. Since it helps to create active and selective catalysts, strong acidity can be considered the most significant characteristic of zeolites. Nonetheless, weak acidity may be adequate for chemical reactions in some cases, while strong acidity is not always necessary. Different post-synthesis techniques (steaming, dealumination/desilication, ion exchange, metal loading) allow modifying the density, nature, and strength of acid sites as well as the porous structure. The shape of the micropores in zeolite framework, with a size similar to those of a large number of reactive molecules, is responsible for the shape selectivity. This property allows for the regulation of observed activity and selectivity. Moreover, the high specific surface area and acid/base tunable properties allow zeolites to be used as support for metals and metal oxides, ensuring high loads and metal dispersion in the pore system. Novel zeolite catalysts have been prepared combining these three characteristics, in order to reach a good catalytic performance and elongate the catalyst life.

The number of zeolites that are synthesized and studied increases notably year after year, as well as the opportunities to develop novel related (micro/mesoporous) materials with different potential applications. Nevertheless, the variety of zeolites that have been successfully used in commercial processes is limited. Many different zeolite species are not commercially available due to insufficient thermal and mechanical stabilities, as well as the high cost of zeolite synthesis. Among the zeolites that can be recognized as the most classically used in industrial and environmental protection processes, we can mention the following: Y (FAU), in the catalytic cracking of petroleum cuts; ZSM-5 (MFI), in isomerization, alkylation, and aromatization processes, NO reduction, and methanol to olefin conversions; mordenite (MOR), in trans-alkylation, isomerization, and disproportionation reactions; and β (BEA), in the alkylation of benzene and acylation with acetic anhydride.

As zeolites are extremely active in a wide range of catalytic processes due to their adjustable textural and acidic properties and are also thermally stable, they are very promising in processes that require the conversion of non-conventional feedstocks of different origins. Hierarchical zeolites are very efficient in catalyzing reactions involving large molecules, such as those obtained from biomass conversion processes, from the pre-cracking of bulky hydrocarbon compounds, and from the thermal pyrolysis of plastic waste, among others.

This Special Issue aims to address the current trends and challenges in the use of zeolites as catalysts in novel processes involving non-conventional feedstocks. Topics of interest may include (but are not restricted to) the application of zeolite catalysts to intensify the processing of non-conventional feedstocks (both fossil cuts and streams coming from biomass conversion or from the thermal pyrolysis of different wastes, among others). Strategies that enhance the catalytic properties, improve the catalytic performance (activity and selectivity), and the thermal stability and regenerability of catalysts, as well as increase their lifetimes, are welcome.

Dr. Juan Rafael Garcia
Dr. María Eugenia Sad
Dr. Clara Saux
Guest Editors

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Keywords

  • hierarchical zeolites
  • zeolites in compound catalysts
  • structured zeolitic catalysts
  • novel zeotype materials
  • stability, deactivation, and regeneration
  • activity and selectivity improvement

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Published Papers (2 papers)

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Research

17 pages, 3183 KiB  
Article
On the Location and Accessibility of Active Acid Sites in MFI Zeolites Modified by Alkaline Treatment
by Lucas G. Tonutti, Lourdes Vergara, Carlos A. Querini and Bruno O. Dalla Costa
Processes 2024, 12(11), 2567; https://doi.org/10.3390/pr12112567 - 16 Nov 2024
Viewed by 476
Abstract
An MFI zeolite (Si/Al = 40) was desilicated by alkaline treatment in order to generate mesopores. Temperature, alkali concentration and treatment duration were adjusted to maximize mesoporosity while preserving the zeolite structure. Special attention was paid to the characterization of the strength and [...] Read more.
An MFI zeolite (Si/Al = 40) was desilicated by alkaline treatment in order to generate mesopores. Temperature, alkali concentration and treatment duration were adjusted to maximize mesoporosity while preserving the zeolite structure. Special attention was paid to the characterization of the strength and accessibility of the acid sites. The catalysts were tested in the isobutane/butene alkylation, a reaction that is typically catalyzed by zeolites but limited by coke deposition. Additionally, glycerol esterification with acetic acid was used as a test reaction due to the required participation of large pores. The results confirmed that mesopores were successfully generated in the MFI zeolite, and the diffusion through the solid was enhanced, but the active sites were mainly confined to the micropores. Full article
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23 pages, 4537 KiB  
Article
Improvement of Properties of Bio-Oil from Biomass Pyrolysis in Auger Reactor Coupled to Fluidized Catalytic Bed Reactor
by Balkydia Campusano, Michael Jabbour, Lokmane Abdelouahed, Mélanie Mignot, Christine Devouge-Boyer and Bechara Taouk
Processes 2024, 12(11), 2368; https://doi.org/10.3390/pr12112368 - 28 Oct 2024
Viewed by 664
Abstract
The goal of this research work was to investigate the improvement of bio-oil issued from beechwood biomass through catalytic de-oxygenation. Pyrolysis was conducted in an auger reactor and the catalytic treatment was performed in a fluidized catalytic bed reactor. Lab-synthesized Fe-HZSM-5 catalysts with [...] Read more.
The goal of this research work was to investigate the improvement of bio-oil issued from beechwood biomass through catalytic de-oxygenation. Pyrolysis was conducted in an auger reactor and the catalytic treatment was performed in a fluidized catalytic bed reactor. Lab-synthesized Fe-HZSM-5 catalysts with different iron concentrations were tested. BET specific surface area, BJH pore size distribution, and FT-IR technologies were used to characterize the catalysts. Thermogravimetric analysis was used to measure the amount of coke deposited on the catalysts after use. Gas chromatography coupled to mass spectrometry (GC-MS), flame ionization detection (GC-FID), and thermal conductivity detection (GC-TCD) were used to identify and quantify the liquid and gaseous products. The pyrolysis temperature proved to be the most influential factor on the final products. It was observed that a pyrolysis temperature of 500 °C, vapor residence time of 18 s, and solid residence time of 2 min resulted in a maximum bio-oil yield of 53 wt.%. A high percentage of oxygenated compounds, such as phenolic compounds, guaiacols, and the carboxylic acid group, was present in this bio-oil. Catalytic treatment with the Fe-HZSM-5 catalysts promoted gas production at the expense of the bio-oil yield, however, the composition of the bio-oil was strongly modified. These properties of the treated bio-oil changed as a function of the Fe loading on the catalyst, with 5%Fe-HZSM-5 giving the best performance. A higher iron loading of 5%Fe-HZSM-5 could have a negative impact on the catalyst performance due to increased coke formation. Full article
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