The promotional effect of gallium loading on the bifunctional Cu–Ga/γ-Al2O3catalyst for CO2hydrogenation to methanol and dimethyl ether at atmospheric pressure

2026-01-01
Hydrogenation of CO2 to methanol and dimethyl ether (DME) was investigated over gallium-promoted copper catalysts supported on γ-Al2O3 (Cu–Ga/γ-Al2O3) at atmospheric pressure—conditions under which Ga-promoted Cu/γ-Al2O3 catalysts have not been investigated before. Reaction parameters—including temperature, H2 : CO2 feed ratio, and gas hourly space velocity (GHSV)—were optimized prior to evaluating the effect of Ga loading. Catalysts with varying Ga loadings (5, 10, 12, and 15 wt%) were tested, with the 5 wt% Ga catalyst achieving the highest combined formation rate of methanol and DME at 246 μmolcarbon gcat−1 h−1 and a combined selectivity of 20.6% under optimal conditions (220 °C, 9 : 1 H2 : CO2, GHSV = 30 000 mL gcat−1 h−1), where the DME production rate was twofold that of the Ga-free catalyst. For comparison, a commercial Cu/ZnO/Al2O3 catalyst was synthesized and showed a significantly lower methanol selectivity (7.2%) and formation rate (60 μmol gcat−1 h−1) under identical operating conditions, with no DME production observed. The promotional effect of Ga was further explored using periodic density functional theory (DFT) calculations on a Cu4/β-Ga2O3(001) model. Theoretical results suggest that CO2 hydrogenation proceeds primarily via a carboxyl intermediate, rather than through formate or CO pathways.
Reaction Chemistry and Engineering
Citation Formats
S. Osmanağa, Y. Kaya, I. Önal, and B. İpek Torun, “The promotional effect of gallium loading on the bifunctional Cu–Ga/γ-Al2O3catalyst for CO2hydrogenation to methanol and dimethyl ether at atmospheric pressure,” Reaction Chemistry and Engineering, pp. 0–0, 2026, Accessed: 00, 2026. [Online]. Available: https://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=105028123763&origin=inward.