The role of the oxide support on the structure of the MoS2 active phase (size, morphology, orientation, sulfidation ratio, etc.) remains an open question in hydrotreating catalysis and biomass processing with important industrial implications for the design of improved catalytic formulations. The present work builds on an aqueous-phase surface-science approach using four well-defined alpha-alumina single crystal surfaces (C (0001), A (11 (2) over bar0), M (10 (1) over bar0), and R (1 (1) over bar 02) planes) as surrogates for gamma-alumina (the industrial support) in order to discriminate the specific role of individual support facets. The reactivity of the various surface orientations toward molybdenum adsorption is controlled by the speciation of surface hydroxyls that determines the surface charge at the oxide/water interface. The C (0001) plane is inert, and the R (1 (1) over bar 02) plane has a limited Mo adsorption capacity while the A (11 (2) over bar0) and M (10 (1) over bar0) surfaces are highly reactive. Sulfidation of model catalysts reveals the highest sulfidation degree for the A (11 (2) over bar0) and M (10 (1) over bar0) planes suggesting weak metal/support interactions. Conversely, a low sulfidation rate and shorter MoS2 slabs are found for the R (1 (1) over bar 02) plane implying stronger Mo-O-Al bonds. These limiting cases are reminiscent of type I/type II MoS2 nanostructures. Structural analogies between alpha- and gamma-alumina surfaces allow us to bridge the material gap with real.Al2O3-supported catalysts. Hence, it can be proposed that Mo distribution and sulfidation rate are heterogeneous and surface-dependent on industrial gamma-Al2O3-supported high-surface-area catalysts. These results demonstrate that a proper control of the gamma-alumina morphology is a. strategic lever for a molecular-scale design of hydrotreating catalysts.