Hydrate-based gas storage holds a huge potential to become a promising technology in the future, provided that the storage conditions are moderate enough. Tetrahydrofuran (THF), a widely known promoter, is used in this study to understand its effect on hydrate phase equilibrium conditions and cage occupancies thereafter. Here, we present a fugacity-based thermodynamic model to study the three-phase liquid-hydrate-vapor (L-H-V) equilibria of CH 4 hydrate in pure water (sI hydrate) and in 0.48−5.56 mol % THF solutions (sII hydrate). The model uses the vdW-P theory for the hydrate phase, Peng−Robinson−Stryjek−Vera (PRSV) EOS for the vapor phase, and a modified UNIFAC method for liquid phase calculations. We have introduced a guest−guest interaction parameter for the Langmuir constant estimation. The model also considers the occupancy of CH 4 in large cages of the CH 4 +THF sII hydrate. The AADs of the model predictions from the experimental values for CH 4 hydrate in pure water and THF solutions are 1.52 and 2.75%, respectively. Although THF reduced CH 4 hydrate phase equilibrium pressures drastically in the beginning at 0.48 mol %, no significant changes are observed beyond 3.0 mol % THF concentration. With the increase in THF concentration, the CH 4 occupancy in small and large cages decreased, and the THF occupancy in large cages increased. CH 4 occupancy in sII hydrate large cages is minimal but increases slowly with the temperature. Based on the findings, CH 4 hydrates can be stored at moderate conditions of 298.15 K and 4.71 MPa using an optimal 3.0 mol % THF concentration. The thermodynamic approach developed in this study also provides a significant basis for future hydrate-based gas storage technology.