Iridium (Ir) catalysts have been
extensively applied in homogeneous
and photocatalytic CO2 conversion. However, CO2 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/In2O3) of high
dispersion is very active for CO2 hydrogenation to methanol.
Compared to In2O3, Ir/In2O3 shows a significantly higher activity with even higher methanol
selectivity. For example, CO2 conversion of 17.7% is achieved
on Ir/In2O3 of 10 wt % Ir loading with methanol
selectivity over 70% and high methanol space time yield of 0.765 gMeOH h–1 gcat
–1 at 4/1 of the CO2/H2 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
In2O3, which causes the high dispersion of the
Ir catalyst with the Ir–In2O3 interface
as the active site for selective hydrogenation of CO2 into
methanol. The Ir loading not only enhances the formation of oxygen
vacancies but also stabilizes the vacancies for improved CO2 activation. Further density functional theory studies reveal that
the reverse water–gas shift route is more favorable over the
formate route for CO2 hydrogenation to methanol over Ir/In2O3 catalyst.