Identifying the active sites and reaction kinetics for a catalytic reaction can provide significant insight to the catalytic systems. By conducting DFT calculations, the catalytic activity of FeO/Pt(111) interfacial sites, which is an important class of catalyst with excellent activity, for methanol partial oxidation is carefully examined and compared. The O-H cleavage barrier of methanol is significantly diminished to below 0.1 eV with the aid of interfacial oxygen, which is much lower than that on the Pt(111) surface (> 0.8 eV). The CH3O* intermediate can further undergo a C-H bond breaking process to produce formaldehyde via a low barrier (~ 0.2 eV) at the interfacial Pt sites. Assisted by interfacial Pt-O ensemble, the O-H and C-H bond cleavage are greatly facilitated, suggesting that the FeO/Pt bi-phase system could effectively combine the advantages of two individual phases. To investigate the rate determining steps, a multi-site 2 / 32 micro-kinetic model is applied at FeO/Pt interface. The results show that the overall rate can be significantly improved by lower the activation energy of interfacial oxygen removal steps. Interestingly, the turnover frequency (TOF) can also be enlarged when increasing the barriers of O2 dissociative adsorption on the Pt flat surface, which is a special feature in multi-phase systems comparing with the mono-phase one. The active site and micro-kinetic studies in our work can provide insights into the development of metal/oxide catalysts for the partial oxidation of methanol or other primary alcohols.