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Highly Active Ir/In<sub>2</sub>O<sub>3</sub> Catalysts for Selective Hydrogenation of CO<sub>2</sub> to Methanol: Experimental and Theoretical Studies

2021/03/17 by Chenyang Shen, Kaihang Sun, Zhitao Zhang +4
Chemical Engineering · Energy · Materials Science · #CO2 Reduction Techniques and Catalysts #Catalysts for Methane Reforming #Catalytic Processes in Materials Science

paper · doi:10.1021/acscatal.0c05628

openalex publication_date 2021/03/17 · openalex created_date 2025/10/10 · openalex updated_date 2026/07/30

Abstract

Iridium (Ir) catalysts have been extensively applied in homogeneous and photocatalytic CO 2 conversion. However, CO 2 hydrogenation to methanol over the supported Ir catalyst in a heterogeneous flowing reactor has not been reported yet. Here, we report that indium oxide supported Ir catalyst (Ir/In 2 O 3 ) of high dispersion is very active for CO 2 hydrogenation to methanol. Compared to In 2 O 3, Ir/In 2 O 3 shows a significantly higher activity with even higher methanol selectivity. For example, CO 2 conversion of 17.7% is achieved on Ir/In 2 O 3 of 10 wt % Ir loading with methanol selectivity over 70% and high methanol space time yield of 0.765 g MeOH h –1 g cat –1 at 4/1 of the CO 2 /H 2 feed ratio, 21 000 h –1, 300 °C, and 5 MPa. With the catalysts tested, the higher Ir loading causes the higher activity. The catalyst characterization confirms an intense interaction between iridium and In 2 O 3, which causes the high dispersion of the Ir catalyst with the Ir–In 2 O 3 interface as the active site for selective hydrogenation of CO 2 into methanol. The Ir loading not only enhances the formation of oxygen vacancies but also stabilizes the vacancies for improved CO 2 activation. Further density functional theory studies reveal that the reverse water–gas shift route is more favorable over the formate route for CO 2 hydrogenation to methanol over Ir/In 2 O 3 catalyst.

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