C. Gabaldon et al., ISOBARIC VAPOR-LIQUID-EQUILIBRIA FOR BINARY AND TERNARY-SYSTEMS COMPOSED OF WATER, 1-PROPANOL, AND 2-PROPANOL AT 100 KPA, Journal of chemical and engineering data, 41(6), 1996, pp. 1379-1382
Isobaric vapor-liquid equilibria data were obtained for the 2-propanol
+1-propanol binary system and the water+1-propanol+2-propanol ternary
system at 100 kPa. The data were found to be thermodynamically consist
ent according to the Van Ness-Byer-Gibbs method for the binary system
and according to the McDermott-Ellis method for the ternary one. The b
inary system is well represented by assuming ideal behavior. The binar
y interaction parameters obtained from this and our previous work are
used to predict the vapor-liquid equilibrium for the ternary system us
ing the UNIQUAC, NRTL, and Wilson models. The ternary system is well p
redicted from binary data.