The CO hydrogenation reaction catalyzed by the ZnCr 2 O 4 catalyst is studied using quasi-in situ XPS, temperatureprogrammed reaction spectroscopy, and temporal in situ diffuse reflectance Fourier transform infrared spectroscopy. At 573 K, the ZnCr 2 O 4 catalyst selectively catalyzes the CH 3 OH formation reaction, in which the hydrogenation reaction of monodentate formate species is the rate-limiting step with an activation energy of approximately 60.5 kJ/mol. As the temperature increases to 673 K, CO 2 and CH 4 are produced at the expense of CH 3 OH, which can be attributed to in situ partial reduction of the ZnCr 2 O 4 catalyst into metallic Zn. On one hand, the CO disproportionation reaction into CO 2 and atomic carbon species occurs on the resulting metallic Zn, and the atomic carbon species is subsequently hydrogenated predominantly into CH 4 ; on the other hand, the rate-limiting step of methanol synthesis on the resulting partially reduced ZnCr 2 O 4 catalyst becomes the hydrogenation of the methoxy group with an activation energy of approximately 120.3 kJ/mol, considerably reducing the CH 3 OH formation rate. These results unveil that the changes in the elementary surface reaction network and the kinetics induced by in situ restructuring of the ZnCr 2 O 4 catalyst in the CO hydrogenation reaction lead to the changes in catalytic selectivity.