Synthesis and characterization of Cu-Mg-Al catalysts for the hydrogenation of CO₂ to methanol and dimethyl ether

Percopo, Federica (2026) Synthesis and characterization of Cu-Mg-Al catalysts for the hydrogenation of CO₂ to methanol and dimethyl ether. [Laurea magistrale], Università di Bologna, Corso di Studio in Chimica industriale [LM-DM270], Documento ad accesso riservato.
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Abstract

The anthropogenic emission of carbon dioxide (CO₂) is a primary driver of global climate change, prompting the urgent need for efficient Carbon Capture, Utilization, and Storage (CCUS) technologies. The catalytic hydrogenation of CO₂ to methanol and dimethyl ether (DME) represents a promising route to valorize this greenhouse gas into sustainable, carbon-neutral fuels. This thesis investigates the synthesis and performance of Cu/Mg/Al-based catalysts for the hydrogenation of CO₂ to methanol and DME. Specifically, the study evaluates the influence of the co-precipitation method (comparing constant pH 9 and variable pH up to 11) and the Cu/Mg molar ratio (2 vs. 1) on the physicochemical and catalytic properties of the materials. The catalysts were characterized by N₂ physisorption (BET/BJH), XRD, and Temperature-Programmed Desorption (TPD) of NH₃ and CO₂. Catalytic tests were conducted in a fixed-bed reactor (240 °C, 20 bar, H₂/CO₂ = 3) for both bulk catalysts and bifunctional systems, the latter obtained by physically mixing the precursors with HZSM-5 zeolite. Characterization revealed that a higher copper content (Cu/Mg = 2) promotes the dispersion of the active CuO phase and increases the specific surface area, leading to superior catalytic activity. The co-precipitation pH was found to profoundly affect the porous structure and the acid-base surface properties in synergy with the metal composition. The bulk CMA-2-11 catalyst (Cu/Mg=2, pH 11) exhibited the highest CO₂ conversion (8.3%) and methanol space-time yield (3.1 gCH₃OH/gCAT·min). Upon the addition of HZSM-5, the product distribution successfully shifted toward DME, with the CMA-2-11/HZSM-5 bifunctional system reaching a maximum DME productivity of 4.9 gDME/gCAT·min. The results demonstrate that precisely controlling the synthetic parameters is crucial for tuning the structural and acid-base properties of Cu-based catalysts, thereby optimizing their performance in the direct synthesis of DME from CO₂.

Abstract
Tipologia del documento
Tesi di laurea (Laurea magistrale)
Autore della tesi
Percopo, Federica
Relatore della tesi
Correlatore della tesi
Scuola
Corso di studio
Indirizzo
CHIMICA INDUSTRIALE
Ordinamento Cds
DM270
Parole chiave
CO₂ hydrogenation dimethyl ether (DME) Cu/Mg/Al catalysts co-precipitation bifunctional catalysts methanol Cu-based catalysts
Data di discussione della Tesi
18 Marzo 2026
URI

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