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)
0.0209 395.28
0.1496 377.54
0.1629 375.65
0.1796 373.95
0.2003 371.97
0.2324 369.47
0.2473 367.71
0.2823 365.0
0.3113 362.89
0.3543 359.61
0.3713 358.13
0.0287 393.62
0.4031 355.9
0.4393 354.02
0.4756 351.6
0.5165 349.34
0.5392 348.0
0.5803 345.73
0.6065 344.5
0.6410 343.15
0.6658 342.1
0.6912 340.6
0.0372 392.57
0.7237 339.22
0.7619 337.53
0.7999 335.77
0.8253 334.61
0.8647 333.77
0.8827 332.85
0.9163 331.76
0.9502 330.97
0.9744 330.14
0.0511 390.39
0.0727 387.5
0.0875 385.54
0.0974 383.71
0.1227 381.33
0.1376 379.01
30030; acetone + diethyl carbonate; 00024:00072