Structure-performance descriptors and the role of Lewis acidity in the methanol-to-propylene process

The combination of well-defined acid sites, shape-selective properties and outstanding stability places zeolites among the most practically relevant heterogeneous catalysts. The development of structure-performance descriptors for processes that they catalyse has been a matter of intense debate, bot...

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Veröffentlicht in:Nature chemistry Jg. 10; H. 8; S. 804 - 812
Hauptverfasser: Yarulina, Irina, De Wispelaere, Kristof, Bailleul, Simon, Goetze, Joris, Radersma, Mike, Abou-Hamad, Edy, Vollmer, Ina, Goesten, Maarten, Mezari, Brahim, Hensen, Emiel J M, Martínez-Espín, Juan S, Morten, Magnus, Mitchell, Sharon, Perez-Ramirez, Javier, Olsbye, Unni, Weckhuysen, Bert M, Van Speybroeck, Veronique, Kapteijn, Freek, Gascon, Jorge
Format: Journal Article
Sprache:Englisch
Veröffentlicht: England Nature Publishing Group 01.08.2018
Schlagworte:
Acidity
Alkenes
Catalysis
Catalysts
Coking
Direct conversion
Lewis acid
Methanol
Propylene
Zeolites
ISSN:1755-4330, 1755-4349, 1755-4349
Online-Zugang:Volltext
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Zusammenfassung:The combination of well-defined acid sites, shape-selective properties and outstanding stability places zeolites among the most practically relevant heterogeneous catalysts. The development of structure-performance descriptors for processes that they catalyse has been a matter of intense debate, both in industry and academia, and the direct conversion of methanol to olefins is a prototypical system in which various catalytic functions contribute to the overall performance. Propylene selectivity and resistance to coking are the two most important parameters in developing new methanol-to-olefin catalysts. Here, we present a systematic investigation on the effect of acidity on the performance of the zeolite 'ZSM-5' for the production of propylene. Our results demonstrate that the isolation of Brønsted acid sites is key to the selective formation of propylene. Also, the introduction of Lewis acid sites prevents the formation of coke, hence drastically increasing catalyst lifetime.
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ISSN:1755-4330
1755-4349
1755-4349
DOI:10.1038/s41557-018-0081-0