The catalytic activities of In2O3 catalysts with different surface area for both cyclic unsteady-state (transient) and steady-state reverse water–gas shift (RWGS) reactions were systemically investigated. The initial CO formation rates during CO2-oxidation of the H2-reduced In2O3 catalysts were close to the CO formation rates in steady-state RWGS conditions at 325 °C, suggesting a redox mechanism for the steady-state RWGS reaction over the In2O3 catalysts. Transient kinetics for the In3+/In+ redox and products (H2O, CO) formation during the cyclic H2-reduction and CO2-oxidation of In2O3 under periodic feeding of H2 ↔ CO2 were studied by time-resolved operando UV–vis and In K-edge X-ray absorption experiments at 325 °C. During the H2-reduction, the surface In3+-O species was reduced to produce H2O and In+-□ (□: oxygen vacancy). Subsequent re-oxidation of the In+-□ by CO2 gave CO and the In3+-O species. The transient CO formation rates were close to the consumption rates of In+-□ under CO2, providing a quantitative evidence on the redox mechanism for unsteady-state RWGS reaction over In2O3. These results indicate that the unsteady-state and steady-state RWGS reactions are primary driven by the In3+/In+ redox mechanism. Kinetic results show that the reoxidation step is the rate-limiting step in the steady-state RWGS reaction.
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