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) x (mol mol-1)
0.0209 0.1206
0.1496 0.5637
0.1629 0.5982
0.1796 0.628
0.2003 0.6609
0.2324 0.6994
0.2473 0.7244
0.2823 0.7605
0.3113 0.7862
0.3543 0.8226
0.3713 0.8376
0.0287 0.1689
0.4031 0.8589
0.4393 0.8755
0.4756 0.8949
0.5165 0.9114
0.5392 0.9205
0.5803 0.9347
0.6065 0.9419
0.6410 0.9493
0.6658 0.9548
0.6912 0.9621
0.0372 0.2054
0.7237 0.9683
0.7619 0.9754
0.7999 0.982
0.8253 0.9859
0.8647 0.9889
0.8827 0.9916
0.9163 0.9948
0.9502 0.997
0.9744 0.9987
0.0511 0.2675
0.0727 0.3447
0.0875 0.3934
0.0974 0.435
0.1227 0.4876
0.1376 0.5349
30030; acetone + diethyl carbonate; 00024:00072