The reasonable introduction of oxygen to the in situ conversion process of oil shale can effectively reduce energy consumption, and during this process, temperature is a crucial factor. In this work, we study the isothermal oxidative pyrolysis behavior of two oil shales differing in total organic carbon (TOC) at constant temperatures (225, 285, 340, 400, and 445 ℃). Quantitative analysis of pyrolysis reactants and products was performed through multiple approaches, including gas chromatography (GC), gas chromatography-mass spectrometry (GC-MS), Rock-Eval analysis, and elemental organic analysis. The results indicated that with the increase in reaction temperature, two reaction regimes can be distinguished, low-temperature oxidative pyrolysis (LTOP) and high-temperature oxidative pyrolysis (HTOP), where the transition temperature is approximately 340 ℃. In the LTOP process, low-temperature oxygen addition, isomerization, and decomposition reactions mainly occurred, while in the HTOP process, high-temperature oxidation, pyrolysis, and coke oxidation reactions dominated. Accordingly, a temperature-dependent reaction model of oxidative pyrolysis of oil shale in isothermal conditions was validated and the real-time change in the reaction rates was obtained. The oxidative pyrolysis of oil shale is found to be significantly enhanced with the increase in temperature. Also, oil shale with a higher TOC has a more intense reaction and a higher transition temperature of HTOP and LTOP. This work provides a theoretical basis for the further application of oxidative pyrolysis in oil shale exploitation.