Partially Ordered Mesoporous Zeolite Beta Frameworks as Naphtha-Selective Catalysts in Vacuum Gas Oil Hydrocracking

Designing hierarchical zeolites with ordered mesoporosity remains a major synthetic challenge despite their well-established importance in catalysis and separations. In this study, we examine the spatiotemporal dynamics of zeolite dissolution and reorganization to retrace how transient structural changes during zeolite nucleation influence supramolecular self-assembly. For the first time, we demonstrate that subtle differences in the aluminum (Al) spatial proximity and distribution within various zeolite frameworks critically affect their mesostructuring behavior. Notably, beta zeolite comprising distinct polymorphs with marginally different Al environments has shown an anisotropic dissolution pattern, where polymorph B was selectively fragmented, leaving polymorph A unaffected. Through a postsynthetic mesostructuring approach, polymorph B was preferentially reorganized into a gyroidal cubic ordered mesophase, resulting in partially ordered mesoporous beta zeolite. The prepared zeolites exhibit improved catalytic performance in vacuum gas oil hydrocracking, affording high isoparaffin yields and superior naphtha selectivity. These findings provide a direct link between atomic-scale heterogeneity and mesoscale structural evolution in crystals, offering a new strategy for designing advanced catalytic materials.

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Publication Details

Journal
Journal of the American Chemical Society
Published
2025-10-23
DOI
https://doi.org/10.1021/jacs.5c15691
Citations
1
Primary Topic
Zeolite Catalysis and Synthesis
Type
article
Field-Weighted Citation Impact
0.54
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article

Partially Ordered Mesoporous Zeolite Beta Frameworks as Naphtha-Selective Catalysts in Vacuum Gas Oil Hydrocracking

Robert P. Hodgkins, Omer Refa Koseoglu, Zhiping Lai, Mohammad F. Aljishi et al.
1 citations
Journal of the American Chemical Society
Zeolite Catalysis and Synthesis
0.54
article

Partially Ordered Mesoporous Zeolite Beta Frameworks as Naphtha-Selective Catalysts in Vacuum Gas Oil Hydrocracking

Robert P. Hodgkins, Omer Refa Koseoglu, Zhiping Lai, Mohammad F. Aljishi, Anissa Bendjeriou‐Sedjerari, Vasilios G. Samaras, Edy Abou‐Hamad, Rajesh Kumar Parsapur, Georgian Melinte, Magnus Rueping, Kuo‐Wei Huang, Youssef Saih
article en
1 citations

Abstract

Designing hierarchical zeolites with ordered mesoporosity remains a major synthetic challenge despite their well-established importance in catalysis and separations. In this study, we examine the spatiotemporal dynamics of zeolite dissolution and reorganization to retrace how transient structural changes during zeolite nucleation influence supramolecular self-assembly. For the first time, we demonstrate that subtle differences in the aluminum (Al) spatial proximity and distribution within various zeolite frameworks critically affect their mesostructuring behavior. Notably, beta zeolite comprising distinct polymorphs with marginally different Al environments has shown an anisotropic dissolution pattern, where polymorph B was selectively fragmented, leaving polymorph A unaffected. Through a postsynthetic mesostructuring approach, polymorph B was preferentially reorganized into a gyroidal cubic ordered mesophase, resulting in partially ordered mesoporous beta zeolite. The prepared zeolites exhibit improved catalytic performance in vacuum gas oil hydrocracking, affording high isoparaffin yields and superior naphtha selectivity. These findings provide a direct link between atomic-scale heterogeneity and mesoscale structural evolution in crystals, offering a new strategy for designing advanced catalytic materials.

Journal of the American Chemical SocietyVol. 147(44)
Institute of Catalysis and Petrochemistry (RU), Community Catalyst (US), Renewable Energy Systems (United States) (US), Saudi Aramco (Saudi Arabia) (SA), Cory Laboratories (US), Saudi Aramco (United States) (US), King Abdullah University of Science and Technology (SA), Core Laboratories (United States) (US)
Openalex Percentile: Top 29%
Zeolite Catalysis and Synthesis
0.54
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