Thermodynamics of Fuels with a Biosynthetic Component: Vapor-Liquid Equilibrium Data for Binary and Ternary Mixtures Containing Ethyl 1,1-Dimethylethyl Ether, n-Heptane, and Toluene at T = 313.15 K Villamañán, R.M.; Martín, C.M.; Chamorro, C.R.; Villamañán, M.A.; Segovia, J.J.; Journal of Chemical & Engineering Data 2006, 51, 2091-2095
Data
T = 313.15 K
x (mol mol-1) x (mol mol-1) P (kPa)
0 0 7.875
0.0515 0.2831 11.442
0.1005 0.6296 13.991
0.1011 0.2683 12.557
0.1504 0.5947 15.067
0.1506 0.2535 13.656
0.1579 0.4964 14.885
0.1612 0.3319 14.282
0.1730 0.4482 15.053
0.1777 0.3659 14.814
0.1893 0.3963 15.209
0 0.2984 10.271
0.1939 0.3993 15.34
0.1996 0.5602 16.102
0.2003 0.2387 14.747
0.2050 0.3459 15.358
0.2103 0.4331 15.856
0.2203 0.2972 15.49
0.2271 0.4676 16.388
0.2361 0.2465 15.615
0.2435 0.5016 16.909
0.2493 0.2240 15.818
0 0.6999 11.783
0.2496 0.5253 17.144
0.2516 0.1970 15.729
0.2599 0.5354 17.424
0.2670 0.1480 15.831
0.2764 0.5694 17.947
0.2826 0.0980 15.919
0.2931 0.6037 18.471
0.2980 0.0488 15.996
0.2991 0.2092 16.892
0.2997 0.4901 18.167
0 1 12.318
0.3051 0.0263 16.024
0.3101 0.6389 19.021
0.3133 0 16.054
0.3180 0.6551 19.269
0.3268 0.6732 19.556
0.3485 0.5012 19.326
0.3489 0.1943 17.95
0.3489 0.4557 19.159
0.3684 0.1375 18.101
0.3833 0.4513 19.911
0.0001 0 7.88
0.3988 0.1794 19.017
0.3994 0.4204 20.165
0.4047 0.1511 18.996
0.4179 0.4018 20.484
0.4409 0.1646 19.875
0.4488 0.1645 20.074
0.4496 0.3853 21.155
0.4551 0.3486 21.081
0.4773 0.1782 20.773
0.4985 0.1497 21.122
0.0001 1 12.315
0.4990 0.3507 22.12
0.5138 0.1918 21.661
0.5157 0.2618 22.037
0.5222 0.2524 22.141
0.5500 0.2054 22.54
0.5572 0.2023 22.686
0.5851 0.2185 23.402
0.5916 0.1530 23.222
0.6204 0.2317 24.267
0.6267 0.1027 23.764
0.0278 0.2902 10.896
0.6579 0.2457 25.187
0.6612 0.0534 24.291
0.6786 0.0284 24.556
0.6932 0.2589 26.064
0.6985 0 24.85
0.7101 0.2652 26.487
0.7281 0.2719 26.935
1 0 31.64
1 0 31.628
0.0291 0.6795 12.426
0.0507 0.6644 12.907
4970; toluene + heptane + tert-butyl ethyl ether; 00005:00023:00265