Catalytic
conversion of CO2 to CO via reverse water
gas shift (RWGS) and CH4 via methanation are competing
reactions that simultaneously happen on Ni-based catalysts, and selective
control of the reactions is of great importance to subsequent applications.
Herein, conversion of CO2 on Mo3O5/Ni(111) with varying MoO
x
coverages
was investigated using a combination of density functional theory
(DFT) calculation and microkinetic modeling. The overall reaction
proceeds through sequential RWGS to CO and CO methanation. The coordinatively
unsaturated Mo (Moov) site at the interface of Mo3O5/Ni(111) enhances CO2 adsorption and facilitates
C–O cleavage over the bare Ni(111), leading to more favorable
CO2 direct dissociation to CO formation than the carboxyl
and formate pathways. The oxophilic Moov also facilitates
hydrogenation of CO to HCO and decomposition of CHO to CH and O. On
Mo3O5/4 × 4 Ni(111), the enhanced hydrogenation
and C–O breakage activity resulted in CH4 as the
selective product. On Mo3O5/3 × 3 Ni(111),
in contrast, the reduced size of the surface Ni ensembles caused the
d-band center of surface Ni sites to shift downward, weakened CO adsorption,
and reduced the hydrogenation activity, resulting in CO as the dominant
product. Microkinetics analysis revealed that direct CO2 dissociation was the dominant path on Mo3O5/4 × 4 Ni(111) and the interfacial sites of Mo3O5/4 × 4 Ni(111) were primarily covered by O and OH. The
rate-limiting step on Mo3O5/Ni(111) was the
regeneration of Mo3O5. Consistent with the experimental
results, the microkinetics also predicts that CH4 is selectively
produced on Mo3O5/4 × 4 Ni(111) whereas
CO is the primary product on Mo3O5/3 ×
3 Ni(111).