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)
0.0259 397.18
0.3237 376.81
0.3597 374.84
0.3913 373.54
0.4218 372.06
0.4613 370.71
0.4899 369.56
0.5259 368.07
0.5790 365.86
0.6130 364.44
0.6581 363.0
0.0489 394.57
0.6876 361.95
0.7104 361.2
0.7457 360.3
0.7683 359.33
0.8058 358.4
0.8348 357.45
0.8663 356.45
0.8949 355.58
0.9291 354.67
0.9688 353.75
0.1027 390.39
0.1323 387.96
0.1611 386.12
0.1891 384.45
0.2333 381.7
0.2680 379.55
0.3034 377.68
30031; butanone + diethyl carbonate; 00072:00272