TY - JOUR
T1 - Hydrogenation of CO2 to methanol over Cu/AlCeO catalyst
AU - Li, Shaozhong
AU - Guo, Limin
AU - Ishihara, Tatsumi
N1 - Funding Information:
The work was financially supported by the Huazhong University of Science and Technology, China Postdoctoral Science Foundation (No. 2016M602302) and the Opening Project of State Key Laboratory of High Performance Ceramics and Superfine Microstructure (No. SKL201707SIC). The authors thank the Analysis and Testing Center of Huazhong University of Science and Technology for analytical support.
Funding Information:
The work was financially supported by the Huazhong University of Science and Technology, China Postdoctoral Science Foundation (No. 2016M602302 ) and the Opening Project of State Key Laboratory of High Performance Ceramics and Superfine Microstructure (No. SKL201707SIC ). The authors thank the Analysis and Testing Center of Huazhong University of Science and Technology for analytical support.
Publisher Copyright:
© 2019 Elsevier B.V.
PY - 2020/1/1
Y1 - 2020/1/1
N2 - The hydrogenation of CO2 to methanol is one of the most promising ways to reduce the CO2 emission and mitigate the energy shortage, but it still confronts low CO2 conversion and methanol selectivity. In this work, the Cu/Al2O3, Cu/AlCeO and Cu/CeO2 catalysts with 60 wt.% Cu were prepared by co-precipitation method for the CO2 hydrogenation to methanol, and the Cu particles were well dispersed on the supports. It was found that the composite of Al2O3 and CeO2 can inhibit the growth of Cu crystallite, and the Cu/AlCeO had the smaller Cu particles, which was beneficial for catalytic activity improvement. Besides, CeO2 introduced in the catalysts increased the surface basicity and the atom ratio of Cu+ species, which promoted the methanol selectivity. Kinetic experiments indicated that the Cu/AlCeO catalyst had the lowest apparent activation barriers for CO2 activation and methanol synthesis. In the process of reaction, CeO2 in the catalysts can inhibit the agglomerate of Cu, which improved the stability of catalysts. Hence, the Cu/AlCeO catalyst showed the highest space time yield (STYmethanol) for CO2 hydrogenation into methanol. And the STYmethanol was 11.9 mmol h−1 g−1 at 533 K, V(H2)/V(CO2) = 3/1, gas hourly space velocity (GHSV) = 14,400 mL h−1 g−1 and P = 3 MPa.
AB - The hydrogenation of CO2 to methanol is one of the most promising ways to reduce the CO2 emission and mitigate the energy shortage, but it still confronts low CO2 conversion and methanol selectivity. In this work, the Cu/Al2O3, Cu/AlCeO and Cu/CeO2 catalysts with 60 wt.% Cu were prepared by co-precipitation method for the CO2 hydrogenation to methanol, and the Cu particles were well dispersed on the supports. It was found that the composite of Al2O3 and CeO2 can inhibit the growth of Cu crystallite, and the Cu/AlCeO had the smaller Cu particles, which was beneficial for catalytic activity improvement. Besides, CeO2 introduced in the catalysts increased the surface basicity and the atom ratio of Cu+ species, which promoted the methanol selectivity. Kinetic experiments indicated that the Cu/AlCeO catalyst had the lowest apparent activation barriers for CO2 activation and methanol synthesis. In the process of reaction, CeO2 in the catalysts can inhibit the agglomerate of Cu, which improved the stability of catalysts. Hence, the Cu/AlCeO catalyst showed the highest space time yield (STYmethanol) for CO2 hydrogenation into methanol. And the STYmethanol was 11.9 mmol h−1 g−1 at 533 K, V(H2)/V(CO2) = 3/1, gas hourly space velocity (GHSV) = 14,400 mL h−1 g−1 and P = 3 MPa.
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U2 - 10.1016/j.cattod.2019.01.015
DO - 10.1016/j.cattod.2019.01.015
M3 - Article
AN - SCOPUS:85059520167
SN - 0920-5861
VL - 339
SP - 352
EP - 361
JO - Catalysis Today
JF - Catalysis Today
ER -