The vapor-liquid equilibrium data of various refrigerant mixtures are correlated by the Soave, Patel-Teja, and Iwai-Margerum-Lu equations of state, respectively, with one adjustable binary interaction constant, ka12. The Patel-Teja equation is slightly better than others. A generalized equation for ka12 is, then, developed that enables the Patel-Teja equation to predict the equilibrium-phase properties for such mixtures within reasonable accuracy. With the aid of this model, the bubble and dew pressures are predicted for 55 binary non-chlorofluorocarbon (non-CFC) refrigerant mixtures containing HCFC-22, HFC-32, HCFC-123, HCFC-124, HFC-125, HFC-l34a, HCFC-l42b, HFC-l43a, HFC-l52a, HFC-1243, and dimethyl ether at temperatures from 233.15 to 363.15.K over the entire composition range. The prediction shows that the mixtures of HCFC-124/HCFC-l42b as well as HFC-l34a/dimethyl ether could work as near-azeotropic refrigerants.