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Abstract
The increasing need to mitigate CO₂ emissions and develop sustainable routes for fuel and chemical production has intensified research on the catalytic hydrogenation of CO₂ to value-added products. This thesis investigates Cu–Al–Mg-based catalysts for the direct (single-step) hydrogenation of CO₂ to dimethyl ether (DME). The catalysts were synthesised by co-precipitation and evaluated with and without the incorporation of HZSM-5 zeolite, aiming to combine hydrogenation and dehydration functionalities within a single catalytic system. The studied formulations include a CuMgAl catalyst with a Cu:Al:Mg molar ratio of 1:1:1, tested both in its sole form and after physical mixing with HZSM-5, and a CuMg/HZSM-5 catalyst (Cu:Mg = 1:1) obtained by co-precipitating the metallic phase onto the zeolite support. The catalysts were characterised by X-ray diffraction (XRD), nitrogen adsorption-desorption (BET/BJH), and temperature-programmed desorption (TPD), in order to investigate their structural, textural, and surface acid-base properties. Catalytic tests were carried out in a fixed-bed reactor at 240 °C and 20 bar, using a CO₂/H₂ feed molar ratio of 1:3 and a gas hourly space velocity (GHSV) of 1560 h⁻¹. Catalyst performance was evaluated in terms of CO₂ conversion, selectivity toward DME, methanol, CO, and CH₄, and the corresponding space-time yields. Although the synthesized catalysts underperformed the commercial benchmark in terms of CO₂ conversion, the integration of HZSM-5 successfully enabled direct DME synthesis and provided valuable insights into the interplay between metallic and acidic functions.
Abstract
The increasing need to mitigate CO₂ emissions and develop sustainable routes for fuel and chemical production has intensified research on the catalytic hydrogenation of CO₂ to value-added products. This thesis investigates Cu–Al–Mg-based catalysts for the direct (single-step) hydrogenation of CO₂ to dimethyl ether (DME). The catalysts were synthesised by co-precipitation and evaluated with and without the incorporation of HZSM-5 zeolite, aiming to combine hydrogenation and dehydration functionalities within a single catalytic system. The studied formulations include a CuMgAl catalyst with a Cu:Al:Mg molar ratio of 1:1:1, tested both in its sole form and after physical mixing with HZSM-5, and a CuMg/HZSM-5 catalyst (Cu:Mg = 1:1) obtained by co-precipitating the metallic phase onto the zeolite support. The catalysts were characterised by X-ray diffraction (XRD), nitrogen adsorption-desorption (BET/BJH), and temperature-programmed desorption (TPD), in order to investigate their structural, textural, and surface acid-base properties. Catalytic tests were carried out in a fixed-bed reactor at 240 °C and 20 bar, using a CO₂/H₂ feed molar ratio of 1:3 and a gas hourly space velocity (GHSV) of 1560 h⁻¹. Catalyst performance was evaluated in terms of CO₂ conversion, selectivity toward DME, methanol, CO, and CH₄, and the corresponding space-time yields. Although the synthesized catalysts underperformed the commercial benchmark in terms of CO₂ conversion, the integration of HZSM-5 successfully enabled direct DME synthesis and provided valuable insights into the interplay between metallic and acidic functions.
Tipologia del documento
Tesi di laurea
(Laurea magistrale)
Autore della tesi
Madrigali, Elisa
Relatore della tesi
Correlatore della tesi
Scuola
Corso di studio
Ordinamento Cds
DM270
Parole chiave
CO₂ hydrogenation DME synthesis CuAlMg catalysts hybrid HZSM5 catalysts
Data di discussione della Tesi
26 Gennaio 2026
URI
Altri metadati
Tipologia del documento
Tesi di laurea
(NON SPECIFICATO)
Autore della tesi
Madrigali, Elisa
Relatore della tesi
Correlatore della tesi
Scuola
Corso di studio
Ordinamento Cds
DM270
Parole chiave
CO₂ hydrogenation DME synthesis CuAlMg catalysts hybrid HZSM5 catalysts
Data di discussione della Tesi
26 Gennaio 2026
URI
Gestione del documento: