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Data publikacji: 2025-12-19

Ce-impregnated acid functionalized mesoporous silica as catalyst for ethanol dehydration to ethylene

O. Dudarko, V. Tomina, N. Kobylinska, D. Duraczynska, K. Pamin, E. Serwicka, G. Seisenbaeva

Microporous and Mesoporous Materials 403 (2025-12-19) 114006

Abstrakt

The catalytic performance of Ce-containing mesoporous silica, functionalized with phenylsulfonic and phenylsulfonic/phosphonic acid groups, was studied for the ethanol dehydration to ethylene reaction in the temperaturerange of 250 ◦C–500 ◦C. The SBA-15-type materials were prepared using a ‘one-pot’ hydrothermal method, and for comparison, the performance of a silica gel with grafted alkylsulfonic groups was also studied. The initial silica supports and Ce-containing catalysts were characterized by XRD, XPS, TEM, SEM/EDX, TGA, zeta potential measurements, etc. The characterization results showed that the morphology, structure, thermal and textural parameters of the catalysts remained largely unchanged following the impregnation of 0.1 M Ce3+ ions. The nature, amount, and availability of acid groups in the mesoporous framework were identified as key factors influencing the metal-impregnation process. According to DRIFT-IR spectroscopy, the functionalization with sulfonic groups binding Ce3+ ions led to the generation of Brønsted (B) and Lewis (L) acid sites, respectively. Importantly, the thermal stability analysis revealed that the number of strong B-sites rapidly diminished during desorption up to 500 ◦C, resulting in a notable decrease in the B/L ratio after treatment at high temperatures. At the same time, ethanol conversion and selectivity towards ethylene were found to augment with increased reaction temperature to 500 ◦C. The SBA/PhSO3H/Ce catalyst demonstrated superior overall performance, characterized by high ethanol conversion (95 %) and the most favourable kinetic profile, including the lowest activation energy (48.2 kJ/mol) among all materials. In contrast, the Ce-containing SiO2SO3H/Ce catalyst exhibited the highest TON (5223.6 per hour), indicating superior intrinsic efficiency per active site. The reusability of the obtained catalysts in terms of stability and conversion was explained using a range of instrumental methods.

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