Isothermal Vapor-Liquid Equilibrium at 333.15 K and Excess Molar Volumes, Refractive Indices, and Excess Molar Enthalpies at 303.15 K for the Binary and Ternary Mixtures of Di-isopropyl Ether, Ethanol, and 2,2,4-Trimethylpentane Kim, H.D.; Hwang, I.C.; Park, S.J.; Journal of Chemical & Engineering Data 2009, 54, 3051-3058
Data
P = 101 kPa, T = 303.15 K
x (mol mol-1) x (mol mol-1) n (1)
0.0162 0.1508 1.3859
0.0546 0.4923 1.37502
0.0578 0.0255 1.38477
0.0694 0.8938 1.3604
0.0766 0.1809 1.38157
0.0840 0.0835 1.38398
0.0859 0.6663 1.36891
0.0978 0.7811 1.3644
0.1047 0.2463 1.37966
0.1125 0.5627 1.37159
0.1283 0.1292 1.38133
0.0189 0.7669 1.36669
0.1337 0.3125 1.3854
0.1383 0.4616 1.37375
0.1448 0.6755 1.36717
0.1505 0.0173 1.38277
0.1641 0.3829 1.3762
0.1750 0.1757 1.3794
0.1789 0.7961 1.36195
0.1794 0.0768 1.38098
0.1908 0.5731 1.36928
0.2059 0.6848 1.36533
0.0247 0.0567 1.38539
0.2232 0.2231 1.37713
0.2310 0.0258 1.38083
0.2357 0.4715 1.3712
0.2447 0.1044 1.37889
0.2678 0.6949 1.36347
0.2722 0.5835 1.36692
0.2752 0.2727 1.37482
0.2797 0.3732 1.37267
0.3126 0.1331 1.37724
0.3145 0.0357 1.37789
0.0253 0.2313 1.38587
0.3379 0.4823 1.36813
0.3540 0.0541 1.37709
0.3566 0.5941 1.36456
0.3635 0.1630 1.37488
0.3734 0.2793 1.37214
0.4028 0.3832 1.36916
0.4448 0.4939 1.36521
0.4506 0.0447 1.3748
0.4620 0.1375 1.37354
0.4725 0.2350 1.37114
0.0284 0.6571 1.37066
0.4826 0.3379 1.368
0.5331 0.3939 1.36561
0.5526 0.0365 1.37228
0.5636 0.1107 1.37071
0.5719 0.1911 1.3691
0.5832 0.2724 1.36717
0.5949 0.3564 1.36501
0.6578 0.0276 1.37043
0.6662 0.0849 1.36891
0.6752 0.1448 1.36754
0.0298 0.8852 1.36141
0.6852 0.2050 1.36634
0.6944 0.2688 1.36456
0.7672 0.0180 1.36734
0.7793 0.0999 1.36583
0.7955 0.1797 1.36396
0.8861 0.0277 1.3646
0.8945 0.0686 1.36356
0.0345 0.3153 1.3797
0.0370 0.5526 1.37373
0.0454 0.4009 1.37785
18779; ethanol + diisopropyl ether + 2,2,4-trimethylpentane; 00026:00071:00250