Dimethyl ether (DME) is a clean and efficient alternative fuel and chemical intermediate, typically produced by methanol dehydration over solid acid catalysts. In this study, the catalytic performance of a γ-Al2O3 membrane operated in a through-flow configuration was evaluated for DME production. The membrane exhibited high methanol conversion and complete DME selectivity (100 %) over the 260–300 °C temperature range, showing optimal performance at 280°C and low WHSV (0.4 h−1), where equilibrium conditions are approached. Comparative tests with γ-Al2O3 pellets demonstrated the membrane superior selectivity and enhanced stability with the time-on-stream. A 30-hour time-on-stream experiment showed a good resistance of membrane to deactivation, with catalytic activity fully restored through a thermal regeneration step. The γ-Al2O3 membrane was further benchmarked against literature-reported ZSM-5 and BEA zeolite membranes, showing better performance in the explored operating conditions.

Selective methanol-to-dimethyl ether conversion in a through-flow γ-Al2O3catalytic membrane contactor: Performance and comparative analysis

Avruscio E.;Catizzone E.
;
Migliori M.;
2026-01-01

Abstract

Dimethyl ether (DME) is a clean and efficient alternative fuel and chemical intermediate, typically produced by methanol dehydration over solid acid catalysts. In this study, the catalytic performance of a γ-Al2O3 membrane operated in a through-flow configuration was evaluated for DME production. The membrane exhibited high methanol conversion and complete DME selectivity (100 %) over the 260–300 °C temperature range, showing optimal performance at 280°C and low WHSV (0.4 h−1), where equilibrium conditions are approached. Comparative tests with γ-Al2O3 pellets demonstrated the membrane superior selectivity and enhanced stability with the time-on-stream. A 30-hour time-on-stream experiment showed a good resistance of membrane to deactivation, with catalytic activity fully restored through a thermal regeneration step. The γ-Al2O3 membrane was further benchmarked against literature-reported ZSM-5 and BEA zeolite membranes, showing better performance in the explored operating conditions.
2026
Catalytic membrane contactor
DME
E-fuel
Hydrogen carrier
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/20.500.11770/404364
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