Fe-ZSM-5 outperforms Al-ZSM-5 in paraffin cracking by increasing the olefinicity of C3-C4 products

• Tetrahedrally coordinated framework-associated Fe 3+ species form strong Lewis acid sites. • Paraffin cracking is initiated by strong Lewis acid sites of Fe-ZSM-5. • Fe-ZSM-5 increases propene, butenes and aromatics selectivity compared with Al-ZSM-5. • Fe 2 O 3 particles does not catalyze paraffin cracking. Iron-modified Al-ZSM-5 increases selectivity to propene, a key petrochemical resulting from fluid catalytic cracking (FCC). However, the type and role of active iron species remain unclear, hindering efforts to streamline the design of selective FCC additives. Here, we investigated Al-free Fe-ZSM-5 catalysts containing iron species in the form of framework Fe 3+ , extra-framework Fe 3+ , oxidic clusters, and oxide micro aggregates in n-octane cracking (FCC model) to assess their effect on catalytic cracking. DR-UV–Vis spectroscopy, 57 Fe Mössbauer Spectroscopy, FTIR studies of pyridine adsorption, and n-octane cracking tests at 500 °C revealed that framework-associated coordinatively unsaturated Fe 3+ species, which induce strong Lewis acidity, are responsible for paraffin cracking initiation, whereas bulk iron oxides on the zeolite surface are inactive. In comparison with Al-ZSM-5, Fe-ZSM-5 increases the olefinicity of the valuable C 3 -C 4 fractions (selectivity to propene and butenes) and promotes aromatization reactions due to the lower relative strength of Fe-induced Brønsted acid sites and dehydrogenation properties. As shown by our 57 Fe Mössbauer study (performed at −269 °C) of the catalyst in calcined, spent, and regenerated states, Fe-ZSM-5 deactivation is associated with the loss of tetrahedrally coordinated Fe 3+ species. Therefore, tuning Fe-ZSM-5 C 3 -C 4 selective FCC additives requires stabilizing framework Brønsted and framework-associated Lewis acid sites while decreasing the concentration of iron oxide species. Ultimately, these findings may enable us to meet the demand for propene derived from FCC cracking, which is expected to grow in the foreseeable future.

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Publication Details

Journal
Chemical Engineering Journal
Published
2024-09-27
DOI
https://doi.org/10.1016/j.cej.2024.156032
Citations
11
Primary Topic
Zeolite Catalysis and Synthesis
Type
article
Field-Weighted Citation Impact
1.74

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article

Fe-ZSM-5 outperforms Al-ZSM-5 in paraffin cracking by increasing the olefinicity of C3-C4 products

Paul Diddams, Jan Přech, A. Iulian Dugulan, Anastasia Kurbanova et al.
11 citations
Chemical Engineering Journal
Zeolite Catalysis and Synthesis
1.74
article

Fe-ZSM-5 outperforms Al-ZSM-5 in paraffin cracking by increasing the olefinicity of C3-C4 products

Paul Diddams, Jan Přech, A. Iulian Dugulan, Anastasia Kurbanova, Kinga Gołą̨bek, Jakub Hraníček, Nicolas Bats, Dominika Zákutná, Ming‐Feng Hsieh
article en
11 citations

Abstract

• Tetrahedrally coordinated framework-associated Fe 3+ species form strong Lewis acid sites. • Paraffin cracking is initiated by strong Lewis acid sites of Fe-ZSM-5. • Fe-ZSM-5 increases propene, butenes and aromatics selectivity compared with Al-ZSM-5. • Fe 2 O 3 particles does not catalyze paraffin cracking. Iron-modified Al-ZSM-5 increases selectivity to propene, a key petrochemical resulting from fluid catalytic cracking (FCC). However, the type and role of active iron species remain unclear, hindering efforts to streamline the design of selective FCC additives. Here, we investigated Al-free Fe-ZSM-5 catalysts containing iron species in the form of framework Fe 3+ , extra-framework Fe 3+ , oxidic clusters, and oxide micro aggregates in n-octane cracking (FCC model) to assess their effect on catalytic cracking. DR-UV–Vis spectroscopy, 57 Fe Mössbauer Spectroscopy, FTIR studies of pyridine adsorption, and n-octane cracking tests at 500 °C revealed that framework-associated coordinatively unsaturated Fe 3+ species, which induce strong Lewis acidity, are responsible for paraffin cracking initiation, whereas bulk iron oxides on the zeolite surface are inactive. In comparison with Al-ZSM-5, Fe-ZSM-5 increases the olefinicity of the valuable C 3 -C 4 fractions (selectivity to propene and butenes) and promotes aromatization reactions due to the lower relative strength of Fe-induced Brønsted acid sites and dehydrogenation properties. As shown by our 57 Fe Mössbauer study (performed at −269 °C) of the catalyst in calcined, spent, and regenerated states, Fe-ZSM-5 deactivation is associated with the loss of tetrahedrally coordinated Fe 3+ species. Therefore, tuning Fe-ZSM-5 C 3 -C 4 selective FCC additives requires stabilizing framework Brønsted and framework-associated Lewis acid sites while decreasing the concentration of iron oxide species. Ultimately, these findings may enable us to meet the demand for propene derived from FCC cracking, which is expected to grow in the foreseeable future.

Chemical Engineering JournalVol. 499
Charles University (CZ), Johnson Matthey (United Kingdom) (GB), Delft University of Technology (NL)
Univerzita Karlova v Praze, Ministerstvo Školství, Mládeže a Tělovýchovy, European Research Council, Faculty of Science, Prince of Songkla University
Openalex Percentile: Top 16%
Zeolite Catalysis and Synthesis
1.74
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