Isobaric Vapor-Liquid-Liquid Equilibria for the Ternary Systems Ethanol + Water + Propyl Acetate and 1-Propanol + Water + Propyl acetate Pla-Franco, J.; Lladosa, E.; Loras, S.; Montón, J.B.; Journal of Chemical & Engineering Data 2014, 59, 2054-2064
Data
P = 101.3 kPa
T (K) x (mol mol-1) x (mol mol-1) x (mol mol-1) x (mol mol-1) x (mol mol-1) x (mol mol-1)
355.37 0.013 0.984 0.2698 0.139 0.09 0.521
356.14 0.035 0.961 0.5091 0.262 0.183 0.533
356.74 0.042 0.952 0.5924 0.255 0.207 0.539
355.39 0.01 0.987 0.2526 0.122 0.081 0.525
355.44 0.007 0.99 0.2084 0.064 0.051 0.528
355.50 0.016 0.981 0.2994 0.17 0.108 0.524
355.53 0.021 0.975 0.3665 0.215 0.132 0.524
355.63 0.002 0.994 0.1906 0.032 0.024 0.534
355.69 0.027 0.97 0.4042 0.236 0.147 0.526
355.83 0.03 0.967 0.4305 0.243 0.161 0.525
356.08 0.032 0.964 0.4589 0.253 0.174 0.529
23645; propan-1-ol + propyl ethanoate + water; 00004:00101:00378