Tri-Reforming, comprises of steam and CO2 reforming as well as partial oxidation of methane, has became attractive by many researchers for production of suitable H2/CO ratios, which can be employed in chemical industries for utilization of abounded natural gas. In this research, thermodynamic equilibrium modeling of involved chemical reactions in Tri-reforming of methane has been conducted using CHEMKIN software via Gibbs free energy minimization method. For this work, various mixtures of initial feed (methane, CO2, H2O and O2) at different temperatures of 500-1000 K and pressures ranging from 1-50 atm. It is shown that, CH4:CO2:H2O:O2 ratios of 1:0.4:0.2:0.1, 1:0.475:0.475:0.1 and 1:0.2:0.5:0.1 are suitable feed composition at 1000 K in terms of methane/CO2/H2O conversion. In thermodynamic viewpoint, high pressure is not desirable and production of syngas is decreased.