“…Therefore, the three-phase (H–L W –V) equilibria of the CHF 3 + N 2 + water systems with various CHF 3 concentrations (10%, 20%, 40%, 60%, and 80%) in the temperature range of 275–289 K and pressure range of 0.7–11.5 MPa were measured, and the results are presented in Figure and Table . Also, the H–L W –V equilibrium data of pure CHF 3 hydrate, which were measured in our previous study, and those of pure N 2 hydrate are also presented in Figure to examine the effect of CHF 3 concentrations on the thermodynamic stability of the CHF 3 + N 2 gas hydrates. , As shown in Figure , the H–L W –V equilibrium curves of the CHF 3 + N 2 + water systems were located generally nearer to that of the CHF 3 + water system than that of the N 2 + water system. This is because N 2 forms the sII hydrate at very high pressure conditions, occupying both small (5 12 ) and large (5 12 6 4 ) cages, due to its small molecular size, whereas CHF 3 forms the sI hydrate, primarily occupying large (5 12 6 2 ) cages and partly occupying small (5 12 ) cages. ,− , Therefore, as the CHF 3 concentration in the vapor phase increased, the H–L W –V equilibria of the CHF 3 + N 2 + water systems became thermodynamically more stable as a result of the increased enclathration of a large-sized molecular guest (CHF 3 ).…”