Mesostructured zeolite ZSM-5 directed by polyethylene glycol (PEG) at low temperature for producing high aromatic green gasoline from palm oil

ZSM-5 has become the primary catalyst for converting palm oil into green gasoline. However, the small intrinsic micropore of ZSM-5 creates a diffusion issue, especially for the bulky molecule of palm oil, which decreases the conversion. Introducing additional mesopores to ZSM-5, forming a hierarchic...

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Vydané v:Journal of porous materials Ročník 32; číslo 5; s. 2015 - 2025
Hlavní autori: Nanda, Arxhel S. F., Maghfirah, Ainul, Khalil, Munawar, Rasrendra, Carolus B., Fahma, Farah, Kadja, Grandprix T. M.
Médium: Journal Article
Jazyk:English
Vydavateľské údaje: New York Springer US 01.10.2025
Springer Nature B.V
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ISSN:1380-2224, 1573-4854
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Shrnutí:ZSM-5 has become the primary catalyst for converting palm oil into green gasoline. However, the small intrinsic micropore of ZSM-5 creates a diffusion issue, especially for the bulky molecule of palm oil, which decreases the conversion. Introducing additional mesopores to ZSM-5, forming a hierarchical zeolite, could resolve this issue. This work presents the formation of a hierarchical ZSM-5 assisted by polyethylene glycol (PEG) at low temperatures. The TEM images and N 2 adsorption isotherms confirmed the formation of interconnected mesopores in the ZSM-5 framework. We found that the molecular weight of PEG (PEG-400, PEG-4000, and PEG-5800) firmly controlled the textural properties and catalytic performance of palm oil conversion into green gasoline. Among the PEG types, PEG-4000 significantly increased the S BET and S ext to 400 and 198 m 2 /g, respectively. PEG-4000 also increased the hierarchy factor index by about two times that of commercial ZSM-5 and ZSM-5 prepared without PEG. Despite the lower acidity, the prepared hierarchical ZSM-5 exhibited higher gasoline yields than the commercial one, with a remarkable selectivity toward aromatic gasoline. Accordingly, the prepared hierarchical ZSM-5 improved the quality of the gasoline by increasing the RON values to 110–119, higher than the commercial zeolite (RON: 102).
Bibliografia:ObjectType-Article-1
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content type line 14
ISSN:1380-2224
1573-4854
DOI:10.1007/s10934-025-01826-6