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In relation to this article, we declare that there is no conflict of interest.
Publication history
Received April 15, 2026
Accepted April 28, 2026
Available online August 25, 2026
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Hierarchical MFI-Type Zeolites for Light Olefin Production in CO2-Fischer-Tropsch Tandem Catalysis

CO2 & Energy Research Center, Korea Research Institute of Chemical Technology (KRICT) 1Department of Chemical and Biomolecular Engineering (BK21 Four), Korea Advanced Institute of Science and Technology (KAIST) 2Hydrogen Process Research Center, Korea Research Institute of Chemical Technology (KRICT) 3Department of Energy and Chemical Engineering, Incheon National University (INU) 4Department of Chemical Engineering, Ajou University 5Department of Energy System Research, Ajou University
hgpark@krict.re.kr, seokki@ajou.ac.kr
Korean Journal of Chemical Engineering, August 2026, 43(10), 2647-2661(15)
https://doi.org/10.1007/s11814-026-00739-7

Abstract

A two-stage tandem process combining CO2 Fischer-Tropsch synthesis (CO2-FTS) with downstream zeolite upgrading 

provides a practical route for converting broad Anderson-Schulz-Flory (ASF)-type hydrocarbons into light olefins. In 

this study, hierarchical MFI zeolites with systematically tuned mesoporosity were synthesized using the amphiphilic 

organosilane [3-(trimethoxysilyl)propyl]hexadecyldimethylammonium chloride (TPHAC) and compared with commercial 

microporous ZSM-5 (Si/Al=15). TPHAC preserved the MFI framework while increasing the external surface area and 

mesopore volume. The upstream K/Fe-Cu-Al catalyst produced a stable ASF-type hydrocarbon stream at 300 °C and 

2.5 MPa. In the temperature-screening tandem reaction, TPHAC-4% showed the best performance, affording the highest

C2-C4 olefin selectivity of 52.34% on a hydrocarbon basis at 500 °C while suppressing BTEX formation. Under the 

150 h long-term operation at the same temperature, it maintained an average C2-C4 olefin selectivity of 56.77% over 

TOS 40–150 h. A 1-octene model reaction reproduced the same trend, indicating that the hierarchical pore structure promoted

light-olefin formation while suppressing competing aromatic pathways. Post-reaction coke analysis further showed 

reduced coke accumulation in the micropores. Overall, the hierarchical pore architecture created a more favorable environment

for light-olefin production

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