Vapor-liquid equilibria for systems of diethyl carbonate and ketones and determination of group interaction parameters for the UNIFAC and ASOG methods Pereiro, A.; Rodrí­guez, A.; Canosa, J.; Tojo, J.; Fluid Phase Equilibria 2005, 235, 83-91
Data
P = 101.325 kPa
x (mol mol-1) Tbp (K)
0.0232 398.42
0.2279 391.25
0.2587 390.69
0.2869 389.74
0.3075 389.29
0.3206 388.79
0.3716 387.65
0.3868 387.39
0.4375 386.21
0.4724 385.28
0.5083 384.62
0.0470 397.26
0.5367 383.93
0.5556 383.46
0.5914 382.81
0.6074 382.56
0.6311 382.15
0.6645 381.25
0.6932 380.79
0.7156 380.23
0.7435 379.77
0.7742 379.31
0.0604 396.79
0.7988 378.66
0.8288 378.26
0.8600 377.63
0.8916 377.15
0.9282 376.39
0.9629 375.83
0.0764 395.99
0.1142 394.81
0.1276 394.39
0.1447 393.9
0.1688 393.16
0.2042 391.98
30032; diethyl carbonate + pentan-2-one; 00072:01417