Isothermal vapor-liquid equilibrium at 333.15 K, excess molar volumes and refractive indices at 298.15 K for mixtures of tert-amyl methyl ether + ethanol + 2,2,4-trimethylpentane Hwang, I.C.; Lee, J.Y.; Park, S.J.; Fluid Phase Equilibria 2009, 281, 5-11
Data
T = 333.15 K
x (mol mol-1) x (mol mol-1) P (kPa)
0.0272 0.6702 63.4
0.0721 0.5770 65.67
0.1010 0.6040 65.57
0.1030 0.7927 56.88
0.1076 0.4799 63.6
0.1164 0.6770 62.99
0.1211 0.5693 66.31
0.1275 0.4933 64.87
0.1350 0.3962 59.04
0.1355 0.2737 48.43
0.1431 0.5354 66.46
0.0293 0.5146 62.05
0.1510 0.5988 65.11
0.1633 0.5101 66.26
0.1692 0.4180 61.75
0.1778 0.5529 66.02
0.1948 0.4217 63.25
0.1949 0.7511 58.43
0.1977 0.6179 63.42
0.2018 0.5190 66.22
0.2168 0.4331 64.28
0.2241 0.4789 65.79
0.0383 0.5439 63.67
0.2289 0.5591 64.42
0.2360 0.3337 57.79
0.2523 0.6733 60.1
0.2577 0.5091 64.65
0.2666 0.3401 59.48
0.2859 0.4687 64.17
0.2882 0.4169 64.09
0.2919 0.3452 60.5
0.2938 0.1459 47.62
0.2966 0.6078 60.85
0.0389 0.6295 64.83
0.3110 0.3486 61.31
0.3293 0.5530 60.93
0.3419 0.1681 50.46
0.3436 0.4399 62.59
0.3439 0.3747 62.1
0.3662 0.2358 54.13
0.3676 0.3021 59.32
0.3693 0.4995 60.31
0.3773 0.1798 52.14
0.4060 0.3342 59.49
0.0470 0.7520 59.14
0.4097 0.3958 60.12
0.4197 0.1900 52.88
0.4252 0.4849 58.66
0.4301 0.2550 56.97
0.4761 0.3516 56.88
0.4812 0.4384 56.2
0.4815 0.2834 56.18
0.4863 0.1325 51.75
0.5109 0.2002 54.21
0.5499 0.0971 50.49
0.0491 0.5544 64.6
0.5758 0.3647 52.86
0.5770 0.2246 52.33
0.0507 0.4222 55.8
0.0508 0.5975 65.3
0.0595 0.5681 65.2
31114; ethanol + 2,2,4-trimethylpentane + 2-methoxy-2-methylbutane; 00026:00071:00465