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Catalytic Aromatization of Propane-Butane Fractions over Polyfunctional Zeolite Catalysts: Effect of Process Parameters

1Shakarim University, Glinki, 20, Semey, Kazakhstan

2Al-Farabi Kazakh National University, Al-Farabi 71, 050040, Almaty, Kazakhstan

3Satbayev University, Satbayev Str. 22, Almaty, 050000, Kazakhstan

4 Chouaïb Doukkali University, Faculty of Sciences, 24000 El Jadida, Morocco

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Received: 10 Feb 2026; Revised: 29 May 2026; Accepted: 29 May 2026; Available online: 29 Jun 2026; Published: 29 Oct 2026.
Editor(s): Istadi Istadi
Open Access Copyright (c) 2026 by Authors, Published by BCREC Publishing Group
Creative Commons License This work is licensed under a Creative Commons Attribution-ShareAlike 4.0 International License.
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Abstract

The catalytic conversion of a propane–butane fraction into aromatic hydrocarbons was investigated over ZnLaFe/ZSM-5 and phosphorus-modified ZnLaFeP/ZSM-5 catalysts. The catalysts were characterized by N₂ adsorption–desorption, X-ray diffraction, SEM-EDX, TEM, and NH₃-TPD analyses. Textural and structural studies confirmed the preservation of the MFI framework after metal and phosphorus incorporation, while acidity measurements revealed that phosphorus modification significantly reduced the concentration of medium-strong and strong Brønsted acid sites, leading to a moderated acid strength distribution. Catalytic performance tests demonstrated that ZnLaFe/ZSM-5 exhibits high PBF conversion over a wide temperature range, whereas ZnLaFeP/ZSM-5 delivers substantially higher aromatic yields, reaching up to 59.7% at 550 °C and a gas hourly space velocity (GHSV) of 350 h⁻¹. The enhanced aromatization performance of the phosphorus-containing catalyst is attributed to the synergistic interaction between moderated Brønsted acidity and Zn–phosphate Lewis acid sites, which promote dehydrogenation, cyclization, and aromatization while suppressing excessive cracking and coke formation. Stability tests over 11 h confirmed the superior resistance of ZnLaFeP/ZSM-5 to deactivation, with only minor losses in conversion and aromatic yield and a stable product distribution dominated by benzene and toluene. Pilot-scale experiments using larger catalyst beds (100 and 500 mL) further demonstrated that the optimized acidity and catalytic functionality are retained upon scale-up.

Keywords: propane-butane fraction; liquefied petroleum gas; ZSM-5; aromatic compound.

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