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 in | Nature (London) Vol. 617; no. 7961; pp. 524 - 528 |
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Main Authors | , , , , , , , , , |
Format | Journal Article |
Language | English |
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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. |
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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. |
Author_xml | – sequence: 1 givenname: Terry Z. H. orcidid: 0000-0003-0357-6390 surname: Gani fullname: Gani, Terry Z. H. organization: Department of Chemical Engineering, Massachusetts Institute of Technology (MIT), Department of Chemistry and Applied Biosciences, ETH Zurich – sequence: 2 givenname: Zachariah J. surname: Berkson fullname: Berkson, Zachariah J. organization: Department of Chemistry and Applied Biosciences, ETH Zurich – sequence: 3 givenname: Ran surname: Zhu fullname: Zhu, Ran organization: Department of Chemical Engineering, Massachusetts Institute of Technology (MIT) – sequence: 4 givenname: Jong Hun surname: Kang fullname: Kang, Jong Hun organization: Department of Chemical Engineering, Massachusetts Institute of Technology (MIT) – sequence: 5 givenname: John R. surname: Di Iorio fullname: Di Iorio, John R. organization: Department of Chemical Engineering, Massachusetts Institute of Technology (MIT) – sequence: 6 givenname: Ka Wing surname: Chan fullname: Chan, Ka Wing organization: Department of Chemistry and Applied Biosciences, ETH Zurich – sequence: 7 givenname: Daniel F. surname: Consoli fullname: Consoli, Daniel F. organization: Department of Chemical Engineering, Massachusetts Institute of Technology (MIT) – sequence: 8 givenname: Sohel K. surname: Shaikh fullname: Shaikh, Sohel K. organization: Research & Development Center, Saudi Aramco – sequence: 9 givenname: Christophe orcidid: 0000-0001-9660-3890 surname: Copéret fullname: Copéret, Christophe email: ccoperet@ethz.ch organization: Department of Chemistry and Applied Biosciences, ETH Zurich – sequence: 10 givenname: Yuriy orcidid: 0000-0002-0025-4233 surname: Román-Leshkov fullname: Román-Leshkov, Yuriy email: yroman@mit.edu organization: Department of Chemical Engineering, Massachusetts Institute of Technology (MIT) |
BackLink | https://www.ncbi.nlm.nih.gov/pubmed/37198312$$D View this record in MEDLINE/PubMed |
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CitedBy_id | crossref_primary_10_1021_acs_jpcc_3c07027 crossref_primary_10_1021_jacs_3c02201 crossref_primary_10_1021_acscatal_3c02045 crossref_primary_10_1021_acscatal_4c01700 crossref_primary_10_1016_j_jcat_2023_115117 crossref_primary_10_1016_j_ymben_2023_12_012 crossref_primary_10_1021_acs_jpcc_4c01305 crossref_primary_10_1039_D3CY01264F crossref_primary_10_1002_adma_202313661 crossref_primary_10_1002_chem_202400860 crossref_primary_10_1002_cctc_202301139 crossref_primary_10_1021_acs_langmuir_3c03748 |
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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 |
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