Thermochemical conversion of surplus agro-residue for energy generation has gained renewed attention, due to its abundant availability throughout the world. Although, it still needs the thermodynamic and pyrolysis kinetic background, that play important role for the effectual design of thermo-chemical conversion reactors such as pyrolyzers, gasifiers, etc. In the present study, thermal profile (mass loss vs. temp) for soybean straw was examined at 20, 30, 40 oC/min heating rates under a non-isothermal condition in an oxygen limiting environment through a thermogravimetric analyzer (TGA). The pyrolysis kinetic parameters (activation energy and pre-exponential factor) were evaluated by applying iso-conversional model-free methods such as Flynn–Wall-Ozawa (FWO), Kissinger-Akahira-Sunose (KAS), and Starink. The average values of activation energy for KAS, FWO and Starink models were recorded to be around 150, 155 and 147 kJ/mol, respectively. Thermodynamic variables (change of enthalpy, entropy, and Gibbs free energy) for soybean straw were also computed. The average value of enthalpy for FWO, KAS, Starink were recorded to be 151, 147, and 142 kJ/mol, respectively. The obtained simulation findings of pyrolysis kinetic and thermodynamic variables are in good agreement.