Lauren Kilburn, Diamarys Salomé Rivera, Elizabeth E. Bickel Rogers, Rajamani Gounder, David D. Hibbitts
{"title":"用计算与实验相结合的方法评估MFI沸石中孔隙环境对丙烯寡聚动力学的影响","authors":"Lauren Kilburn, Diamarys Salomé Rivera, Elizabeth E. Bickel Rogers, Rajamani Gounder, David D. Hibbitts","doi":"10.1021/acscatal.5c00392","DOIUrl":null,"url":null,"abstract":"The consequences of Brønsted acid site location in MFI zeolites were investigated for propene oligomerization. Adsorbates in MFI may reside in smaller channels (∼5.5 Å diam.) or larger channel intersections (∼7 Å diam.), with tighter confinement expected to enhance both stabilizing dispersive interactions and destabilizing steric constraints. MFI samples synthesized using tetrapropylammonium (TPA<sup>+</sup>) as the structure directing agent have higher fractions of acid sites near intersections, while samples synthesized with 1,4-diazabicyclo[2.2.2]octane (DABCO) or ethylenediamine (EDA) have higher fractions of acid sites within channels. Measured propene dimerization rates (per H<sup>+</sup>, 315 kPa C<sub>3</sub>H<sub>6</sub>, 503 K, 1.6 H<sup>+</sup>/u.c.) are ∼9 times higher on MFI-DABCO/MFI-EDA than MFI-TPA. Because propene oligomerization is transport-limited in MFI at these conditions, experimentally measured rates are proportional to both effective kinetic (<i>k</i><sub>eff</sub>) and diffusion (<i>D</i><sub>e</sub>) constants. DFT was therefore used to investigate the kinetic influences of void environment in isolation of transport effects. Adsorption free energies for C<sub>3</sub> and C<sub>6</sub> alkenes and dimerization free energy barriers were calculated at all 12 T-sites present in the MFI framework and all accessible O-sites around each T-site. C<sub>3</sub> preferentially adsorbs as H-bonded propene with similar energies in all void environments, while C<sub>6</sub> alkenes are destabilized by 10–56 kJ mol<sup>–1</sup> and dimerization transition states are destabilized by 29–102 kJ mol<sup>–1</sup>, on average, in the channels relative to intersections. The stability of C<sub>3</sub> and C<sub>6</sub> alkenes and dimerization transition states is largely governed by steric penalties arising from distortion of the MFI framework that outweigh stronger dispersive interactions with decreasing void size, even for species as small as C<sub>3</sub>. Given that DFT predicts <i>k</i><sub>eff</sub> values are lower at acid sites in smaller channel voids of MFI, higher measured rates on MFI samples synthesized using DABCO or EDA must reflect less severe diffusion restrictions and, in turn, higher <i>D</i><sub>e</sub> values.","PeriodicalId":9,"journal":{"name":"ACS Catalysis ","volume":"75 2 1","pages":""},"PeriodicalIF":11.3000,"publicationDate":"2025-04-16","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Assessing the Influence of Void Environment in MFI Zeolites on Propene Oligomerization Kinetics Using a Combined Computational and Experimental Approach\",\"authors\":\"Lauren Kilburn, Diamarys Salomé Rivera, Elizabeth E. Bickel Rogers, Rajamani Gounder, David D. Hibbitts\",\"doi\":\"10.1021/acscatal.5c00392\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"The consequences of Brønsted acid site location in MFI zeolites were investigated for propene oligomerization. Adsorbates in MFI may reside in smaller channels (∼5.5 Å diam.) or larger channel intersections (∼7 Å diam.), with tighter confinement expected to enhance both stabilizing dispersive interactions and destabilizing steric constraints. MFI samples synthesized using tetrapropylammonium (TPA<sup>+</sup>) as the structure directing agent have higher fractions of acid sites near intersections, while samples synthesized with 1,4-diazabicyclo[2.2.2]octane (DABCO) or ethylenediamine (EDA) have higher fractions of acid sites within channels. Measured propene dimerization rates (per H<sup>+</sup>, 315 kPa C<sub>3</sub>H<sub>6</sub>, 503 K, 1.6 H<sup>+</sup>/u.c.) are ∼9 times higher on MFI-DABCO/MFI-EDA than MFI-TPA. Because propene oligomerization is transport-limited in MFI at these conditions, experimentally measured rates are proportional to both effective kinetic (<i>k</i><sub>eff</sub>) and diffusion (<i>D</i><sub>e</sub>) constants. DFT was therefore used to investigate the kinetic influences of void environment in isolation of transport effects. Adsorption free energies for C<sub>3</sub> and C<sub>6</sub> alkenes and dimerization free energy barriers were calculated at all 12 T-sites present in the MFI framework and all accessible O-sites around each T-site. C<sub>3</sub> preferentially adsorbs as H-bonded propene with similar energies in all void environments, while C<sub>6</sub> alkenes are destabilized by 10–56 kJ mol<sup>–1</sup> and dimerization transition states are destabilized by 29–102 kJ mol<sup>–1</sup>, on average, in the channels relative to intersections. The stability of C<sub>3</sub> and C<sub>6</sub> alkenes and dimerization transition states is largely governed by steric penalties arising from distortion of the MFI framework that outweigh stronger dispersive interactions with decreasing void size, even for species as small as C<sub>3</sub>. 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Assessing the Influence of Void Environment in MFI Zeolites on Propene Oligomerization Kinetics Using a Combined Computational and Experimental Approach
The consequences of Brønsted acid site location in MFI zeolites were investigated for propene oligomerization. Adsorbates in MFI may reside in smaller channels (∼5.5 Å diam.) or larger channel intersections (∼7 Å diam.), with tighter confinement expected to enhance both stabilizing dispersive interactions and destabilizing steric constraints. MFI samples synthesized using tetrapropylammonium (TPA+) as the structure directing agent have higher fractions of acid sites near intersections, while samples synthesized with 1,4-diazabicyclo[2.2.2]octane (DABCO) or ethylenediamine (EDA) have higher fractions of acid sites within channels. Measured propene dimerization rates (per H+, 315 kPa C3H6, 503 K, 1.6 H+/u.c.) are ∼9 times higher on MFI-DABCO/MFI-EDA than MFI-TPA. Because propene oligomerization is transport-limited in MFI at these conditions, experimentally measured rates are proportional to both effective kinetic (keff) and diffusion (De) constants. DFT was therefore used to investigate the kinetic influences of void environment in isolation of transport effects. Adsorption free energies for C3 and C6 alkenes and dimerization free energy barriers were calculated at all 12 T-sites present in the MFI framework and all accessible O-sites around each T-site. C3 preferentially adsorbs as H-bonded propene with similar energies in all void environments, while C6 alkenes are destabilized by 10–56 kJ mol–1 and dimerization transition states are destabilized by 29–102 kJ mol–1, on average, in the channels relative to intersections. The stability of C3 and C6 alkenes and dimerization transition states is largely governed by steric penalties arising from distortion of the MFI framework that outweigh stronger dispersive interactions with decreasing void size, even for species as small as C3. Given that DFT predicts keff values are lower at acid sites in smaller channel voids of MFI, higher measured rates on MFI samples synthesized using DABCO or EDA must reflect less severe diffusion restrictions and, in turn, higher De values.
期刊介绍:
ACS Catalysis is an esteemed journal that publishes original research in the fields of heterogeneous catalysis, molecular catalysis, and biocatalysis. It offers broad coverage across diverse areas such as life sciences, organometallics and synthesis, photochemistry and electrochemistry, drug discovery and synthesis, materials science, environmental protection, polymer discovery and synthesis, and energy and fuels.
The scope of the journal is to showcase innovative work in various aspects of catalysis. This includes new reactions and novel synthetic approaches utilizing known catalysts, the discovery or modification of new catalysts, elucidation of catalytic mechanisms through cutting-edge investigations, practical enhancements of existing processes, as well as conceptual advances in the field. Contributions to ACS Catalysis can encompass both experimental and theoretical research focused on catalytic molecules, macromolecules, and materials that exhibit catalytic turnover.