Both noble metals and transition metal oxides are recognized as active centers for alkyne hydrogenation. However, it is still a "black box" how the catalytic behavior of oxides evolves upon the catalytic intervention of noble metals. Herein, we report a modularized strategy to track the hydrogenation mechanism of oxides (e.g., TiO 2 , CeO 2 , and ZrO 2 ) using a core−shell micromesoporous zeolite as a structure model, in which the oxide and noble metal (Pt) are functionally separated within a mesopore shell and a micropore core (TS-1 zeolite), respectively. The Pt species are atomically distributed and stabilized by the oxygen atoms of fivemembered rings in TS-1 zeolite, which facilitates the heterolytic activation of dihydrogen over Pt δ+ •••O 2− units. The active hydrogen species, i.e., H + and H δ− , migrate to the oxide surface, where the adsorbed reactants are activated for hydrogenation. Mechanistic studies reveal that TiO 2 , CeO 2 , and ZrO 2 possess efficient hydrogenation properties at near-room temperature with the assistance of spillover hydrogen species, demonstrating dihydrogen dissociation as the main rate-limiting step for pure oxide. Impressively, the adsorbed H 2 O molecule on TiO 2 , ZrO 2 , and CeO 2 not only acts as a bridge of hydrogen spillover in reducing the proton diffusion barrier but also forms H 3 O + species on the TiO 2 (100) surface and endows TiO 2 with extraordinary hydrogenation properties. This work opens the "black box" for the hydrogenation behavior of transition metal oxides and develops a molecule-assisted strategy for the rational design of hydrogenation catalysts.