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In relation to this article, we declare that there is no conflict of interest.
Publication history
Received December 4, 2025
Revised December 29, 2025
Accepted January 12, 2026
Available online May 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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Catalytic Cracking of 1-Dodecene to Light Olefins Over Steam-Treated Phosphorus-Modified ZSM-5 Zeolites

Center for Low-Carbon Chemical Process, Korea Research Institute of Chemical Technology 1Department of Chemical Engineering and Applied Chemistry, Chungnam National University
sunnykim@cnu.ac.kr, jhshin@krict.re.kr
Korean Journal of Chemical Engineering, May 2026, 43(6), 1555-1569(15)
https://doi.org/10.1007/s11814-026-00652-z

Abstract

Escalating global environmental concerns have heightened the need for effective chemical production methods employing waste plastics pyrolysis. This study focuses on developing a zeolite catalyst for light olefin production, using 1-dodecene to simulate pyrolysis oil derived from waste polyolefin plastics. Here, various H-ZSM-5 and phosphorus-modified ZSM-5 zeolites with different Si/Al and P/Al ratios were prepared with/without steam treatment, and their physicochemical and catalytic properties for 1-dodecene cracking were studied. Phosphorus introduction decreased the number and strength of acid sites, yet aided in maintaining or generating necessary acid sites for olefin cracking after steaming. Optimal preservation of acid sites and thus, the highest yield of C2–C4 olefins, was attained with a P/Al ratio of 0.7 and Si/Al ratio of 15 after steam treatment. Given its high light olefin yield, hydrothermal stability, and complete regeneration after deactivation, our phosphorus-modified ZSM-5 zeolite is a promising catalyst for waste plastic pyrolysis oil cracking.

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