Promoting active site renewal in heterogeneous olefin metathesis catalysts

As an atom-efficient strategy for the large-scale interconversion of olefins, heterogeneously catalysed olefin metathesis sees commercial applications in the petrochemical, polymer and speciality chemical industries 1 . Notably, the thermoneutral and highly selective cross-metathesis of ethylene and...

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Published inNature (London) Vol. 617; no. 7961; pp. 524 - 528
Main Authors Gani, Terry Z. H., Berkson, Zachariah J., Zhu, Ran, Kang, Jong Hun, Di Iorio, John R., Chan, Ka Wing, Consoli, Daniel F., Shaikh, Sohel K., Copéret, Christophe, Román-Leshkov, Yuriy
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LanguageEnglish
Published London Nature Publishing Group UK 18.05.2023
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Abstract As an atom-efficient strategy for the large-scale interconversion of olefins, heterogeneously catalysed olefin metathesis sees commercial applications in the petrochemical, polymer and speciality chemical industries 1 . Notably, the thermoneutral and highly selective cross-metathesis of ethylene and 2-butenes 1 offers an appealing route for the on-purpose production of propylene to address the C 3 shortfall caused by using shale gas as a feedstock in steam crackers 2 , 3 . However, key mechanistic details have remained ambiguous for decades, hindering process development and adversely affecting economic viability 4 relative to other propylene production technologies 2 , 5 . Here, from rigorous kinetic measurements and spectroscopic studies of propylene metathesis over model and industrial WO x /SiO 2 catalysts, we identify a hitherto unknown dynamic site renewal and decay cycle, mediated by proton transfers involving proximal Brønsted acidic OH groups, which operates concurrently with the classical Chauvin cycle. We show how this cycle can be manipulated using small quantities of promoter olefins to drastically increase steady-state propylene metathesis rates by up to 30-fold at 250 °C with negligible promoter consumption. The increase in activity and considerable reduction of operating temperature requirements were also observed on MoO x /SiO 2 catalysts, showing that this strategy is possibly applicable to other reactions and can address major roadblocks associated with industrial metathesis processes. The authors identify a dynamic site renewal and decay cycle, mediated by proton transfers involving proximal Brønsted acidic OH groups, which operates concurrently with the Chauvin cycle and could address roadblocks associated with industrial metathesis processes.
AbstractList As an atom-efficient strategy for the large-scale interconversion of olefins, heterogeneously catalysed olefin metathesis sees commercial applications in the petrochemical, polymer and speciality chemical industries1. Notably, the thermoneutral and highly selective cross-metathesis of ethylene and 2-butenes1 offers an appealing route for the on-purpose production of propylene to address the C3 shortfall caused by using shale gas as a feedstock in steam crackers2,3. However, key mechanistic details have remained ambiguous for decades, hindering process development and adversely affecting economic viability4 relative to other propylene production technologies2,5. Here, from rigorous kinetic measurements and spectroscopic studies of propylene metathesis over model and industrial WOx/SiO2 catalysts, we identify a hitherto unknown dynamic site renewal and decay cycle, mediated by proton transfers involving proximal Brønsted acidic OH groups, which operates concurrently with the classical Chauvin cycle. We show how this cycle can be manipulated using small quantities of promoter olefins to drastically increase steady-state propylene metathesis rates by up to 30-fold at 250 °C with negligible promoter consumption. The increase in activity and considerable reduction of operating temperature requirements were also observed on MoOx/SiO2 catalysts, showing that this strategy is possibly applicable to other reactions and can address major roadblocks associated with industrial metathesis processes.
As an atom-efficient strategy for the large-scale interconversion of olefins, heterogeneously catalysed olefin metathesis sees commercial applications in the petrochemical, polymer and speciality chemical industries . Notably, the thermoneutral and highly selective cross-metathesis of ethylene and 2-butenes offers an appealing route for the on-purpose production of propylene to address the C shortfall caused by using shale gas as a feedstock in steam crackers . However, key mechanistic details have remained ambiguous for decades, hindering process development and adversely affecting economic viability relative to other propylene production technologies . Here, from rigorous kinetic measurements and spectroscopic studies of propylene metathesis over model and industrial WO /SiO catalysts, we identify a hitherto unknown dynamic site renewal and decay cycle, mediated by proton transfers involving proximal Brønsted acidic OH groups, which operates concurrently with the classical Chauvin cycle. We show how this cycle can be manipulated using small quantities of promoter olefins to drastically increase steady-state propylene metathesis rates by up to 30-fold at 250 °C with negligible promoter consumption. The increase in activity and considerable reduction of operating temperature requirements were also observed on MoO /SiO catalysts, showing that this strategy is possibly applicable to other reactions and can address major roadblocks associated with industrial metathesis processes.
As an atom-efficient strategy for the large-scale interconversion of olefins, heterogeneously catalysed olefin metathesis sees commercial applications in the petrochemical, polymer and speciality chemical industries 1 . Notably, the thermoneutral and highly selective cross-metathesis of ethylene and 2-butenes 1 offers an appealing route for the on-purpose production of propylene to address the C 3 shortfall caused by using shale gas as a feedstock in steam crackers 2 , 3 . However, key mechanistic details have remained ambiguous for decades, hindering process development and adversely affecting economic viability 4 relative to other propylene production technologies 2 , 5 . Here, from rigorous kinetic measurements and spectroscopic studies of propylene metathesis over model and industrial WO x /SiO 2 catalysts, we identify a hitherto unknown dynamic site renewal and decay cycle, mediated by proton transfers involving proximal Brønsted acidic OH groups, which operates concurrently with the classical Chauvin cycle. We show how this cycle can be manipulated using small quantities of promoter olefins to drastically increase steady-state propylene metathesis rates by up to 30-fold at 250 °C with negligible promoter consumption. The increase in activity and considerable reduction of operating temperature requirements were also observed on MoO x /SiO 2 catalysts, showing that this strategy is possibly applicable to other reactions and can address major roadblocks associated with industrial metathesis processes. The authors identify a dynamic site renewal and decay cycle, mediated by proton transfers involving proximal Brønsted acidic OH groups, which operates concurrently with the Chauvin cycle and could address roadblocks associated with industrial metathesis processes.
Author Zhu, Ran
Kang, Jong Hun
Consoli, Daniel F.
Gani, Terry Z. H.
Chan, Ka Wing
Copéret, Christophe
Shaikh, Sohel K.
Berkson, Zachariah J.
Román-Leshkov, Yuriy
Di Iorio, John R.
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PublicationCentury 2000
PublicationDate 2023-05-18
PublicationDateYYYYMMDD 2023-05-18
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  year: 2023
  text: 2023-05-18
  day: 18
PublicationDecade 2020
PublicationPlace London
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PublicationSubtitle International weekly journal of science
PublicationTitle Nature (London)
PublicationTitleAbbrev Nature
PublicationTitleAlternate Nature
PublicationYear 2023
Publisher Nature Publishing Group UK
Nature Publishing Group
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Snippet As an atom-efficient strategy for the large-scale interconversion of olefins, heterogeneously catalysed olefin metathesis sees commercial applications in the...
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SubjectTerms 140/131
140/133
639/638/77/885
639/638/77/887
Alkenes
Catalysts
Decay
Humanities and Social Sciences
Metathesis
multidisciplinary
Operating temperature
Petrochemicals
Polymers
Propylene
Science
Science (multidisciplinary)
Shale
Shale gas
Silicon dioxide
Temperature
Temperature requirements
Title Promoting active site renewal in heterogeneous olefin metathesis catalysts
URI https://link.springer.com/article/10.1038/s41586-023-05897-w
https://www.ncbi.nlm.nih.gov/pubmed/37198312
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