Dimethyl ether production via methanol dehydration using Fe3O4 and CuO over γ–χ–Al2O3 nanocatalysts

[Display omitted] •DME production by methanol dehydration using Fe3O4 and CuO.•Fe3O4/γ–χ–Al2O3 reached selectivity to DME of 100%.•The Ea of the Fe3O4/γ–χ–Al2O3 was lower than the value of CuO/γ–χ–Al2O3. Selective Fe3O4 and CuO catalysts supported on γ–χ–Al2O3 were successfully prepared using the fa...

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Veröffentlicht in:Fuel (Guildford) 2020-11, Vol.280, p.118545, Article 118545
Hauptverfasser: Armenta, M.A., Maytorena, V.M., Flores–Sánchez, L.A., Quintana, J.M., Valdez, R., Olivas, A.
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Sprache:eng
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Zusammenfassung:[Display omitted] •DME production by methanol dehydration using Fe3O4 and CuO.•Fe3O4/γ–χ–Al2O3 reached selectivity to DME of 100%.•The Ea of the Fe3O4/γ–χ–Al2O3 was lower than the value of CuO/γ–χ–Al2O3. Selective Fe3O4 and CuO catalysts supported on γ–χ–Al2O3 were successfully prepared using the facile controlled precipitation method. The catalysts Fe3O4/γ–χ–Al2O3 and CuO/γ–χ–Al2O3 showed excellent catalytic activity at low temperatures between 250 and 290 °C and 1 atm pressure. According to the experimental works, Fe3O4/γ–χ–Al2O3 showed better activity and selectivity at 250 °C, related to better dispersion of its active phase within the pores of γ–χ–Al2O3 and its lower activation energy, Ea = 46.4 kJ/mol. At 250 °C, Fe3O4/γ–χ–Al2O3 presented a higher theorical partial pressure of DME related to its better catalytic performance in the methanol dehydration reaction.
ISSN:0016-2361
1873-7153
DOI:10.1016/j.fuel.2020.118545