Datasets
-
Mole fraction (20)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
ρl - Mass density, kg/m3 (2)
Mole fraction of Phenol, 2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1 |
289.15 |
0.0593 |
323.15 |
0.1562 |
Mole fraction of Phenol, 2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 |
Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 2 |
289.15 |
0.5170 |
323.15 |
0.5187 |
Mole fraction of Octane (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Octane (2) - Liquid mixture 1 |
289.15 |
0.9110 |
323.15 |
0.7566 |
Mole fraction of Octane (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 |
Mole fraction of Octane (2) - Liquid mixture 2 |
289.15 |
0.0707 |
323.15 |
0.1109 |
Mole fraction of Phenol, 2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mole fraction of Octane (2) - Liquid mixture 1 |
Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1 |
298.15 |
0.0000 |
0.5093 |
298.15 |
0.0142 |
0.5290 |
298.15 |
0.0334 |
0.5400 |
298.15 |
0.0409 |
0.5530 |
298.15 |
0.0593 |
0.5410 |
298.15 |
0.0634 |
0.5420 |
298.15 |
0.0907 |
0.5390 |
298.15 |
0.1020 |
0.5550 |
298.15 |
0.1080 |
0.5570 |
298.15 |
0.1230 |
0.5700 |
298.15 |
0.1260 |
0.5730 |
298.15 |
0.1360 |
0.5780 |
298.15 |
0.1370 |
0.5820 |
298.15 |
0.1490 |
0.5820 |
298.15 |
0.1530 |
0.5840 |
298.15 |
0.2220 |
0.5900 |
298.15 |
0.2680 |
0.5560 |
298.15 |
0.3260 |
0.5230 |
298.15 |
0.3790 |
0.4860 |
298.15 |
0.3820 |
0.4930 |
298.15 |
0.4350 |
0.4490 |
298.15 |
0.4650 |
0.4390 |
298.15 |
0.6200 |
0.3090 |
298.15 |
0.7290 |
0.2250 |
323.15 |
0.0000 |
0.4917 |
323.15 |
0.0119 |
0.5092 |
323.15 |
0.1128 |
0.5279 |
323.15 |
0.1299 |
0.5179 |
323.15 |
0.1709 |
0.5126 |
323.15 |
0.2428 |
0.4928 |
323.15 |
0.2514 |
0.4878 |
323.15 |
0.2987 |
0.4666 |
323.15 |
0.4283 |
0.4011 |
323.15 |
0.5282 |
0.3400 |
Mole fraction of Phenol, 2-methyl- (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1 |
333.15 |
22.50 |
0.4903 |
333.15 |
24.87 |
0.5202 |
333.15 |
27.18 |
0.4212 |
333.15 |
27.90 |
0.4372 |
333.15 |
28.56 |
0.4308 |
333.15 |
28.98 |
0.4977 |
353.15 |
60.24 |
0.4636 |
353.15 |
63.25 |
0.3275 |
353.15 |
65.29 |
0.3617 |
353.15 |
66.21 |
0.3956 |
353.15 |
66.75 |
0.4834 |
353.15 |
67.53 |
0.4834 |
Mole fraction of Phenol, 2-methyl- (1)
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Pressure, kPa - Gas |
Mole fraction of Phenol, 2-methyl- (1) - Gas |
333.15 |
22.50 |
0.0155 |
333.15 |
24.87 |
0.0161 |
333.15 |
27.18 |
0.0175 |
333.15 |
27.90 |
0.0169 |
333.15 |
28.56 |
0.0175 |
333.15 |
28.98 |
0.0159 |
353.15 |
60.24 |
0.0205 |
353.15 |
63.25 |
0.0199 |
353.15 |
65.29 |
0.0115 |
353.15 |
66.21 |
0.0187 |
353.15 |
66.75 |
0.0186 |
353.15 |
67.53 |
0.0180 |
Mole fraction of Octane (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Octane (2) - Liquid mixture 1 |
333.15 |
22.50 |
0.0291 |
333.15 |
24.87 |
0.0357 |
333.15 |
27.18 |
0.0394 |
333.15 |
27.90 |
0.0545 |
333.15 |
28.56 |
0.0671 |
333.15 |
28.98 |
0.0929 |
353.15 |
60.24 |
0.0337 |
353.15 |
63.25 |
0.0385 |
353.15 |
65.29 |
0.0524 |
353.15 |
66.21 |
0.0661 |
353.15 |
66.75 |
0.0822 |
353.15 |
67.53 |
0.1000 |
Mole fraction of Octane (2)
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Pressure, kPa - Gas |
Mole fraction of Octane (2) - Gas |
333.15 |
22.50 |
0.2338 |
333.15 |
24.87 |
0.2332 |
333.15 |
27.18 |
0.2613 |
333.15 |
27.90 |
0.2746 |
333.15 |
28.56 |
0.3065 |
333.15 |
28.98 |
0.2885 |
353.15 |
60.24 |
0.1992 |
353.15 |
63.25 |
0.2336 |
353.15 |
65.29 |
0.2560 |
353.15 |
66.21 |
0.2617 |
353.15 |
66.75 |
0.2635 |
353.15 |
67.53 |
0.2780 |
Temperature, K x Pressure, kPa x Mole fraction
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Octane (2) - Gas |
Mole fraction of Phenol, 2-methyl- (1) - Gas |
Mole fraction of Octane (2) - Liquid |
Mole fraction of Phenol, 2-methyl- (1) - Liquid |
333.15 |
13.78 |
0.3763 |
0.0222 |
0.0671 |
0.7806 |
333.15 |
14.97 |
0.2171 |
0.0320 |
0.0393 |
0.7460 |
333.15 |
15.05 |
0.1958 |
0.0426 |
0.0341 |
0.7382 |
333.15 |
18.88 |
0.1572 |
0.0286 |
0.0324 |
0.7354 |
333.15 |
20.09 |
0.1546 |
0.0235 |
0.0225 |
0.6342 |
333.15 |
21.31 |
0.2305 |
0.0255 |
0.0330 |
0.6210 |
333.15 |
23.80 |
0.2078 |
0.0153 |
0.0344 |
0.5581 |
353.15 |
48.05 |
0.1591 |
0.0197 |
0.0291 |
0.6170 |
353.15 |
52.66 |
0.1805 |
0.0163 |
0.0330 |
0.5720 |
353.15 |
56.61 |
0.1874 |
0.0131 |
0.0338 |
0.5232 |
Mole fraction of Phenol, 2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1 |
289.15 |
0.0593 |
323.15 |
0.1562 |
Mole fraction of Phenol, 2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 |
Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 2 |
289.15 |
0.5170 |
323.15 |
0.5187 |
Mole fraction of Octane (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Octane (2) - Liquid mixture 1 |
289.15 |
0.9110 |
323.15 |
0.7566 |
Mole fraction of Octane (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 |
Mole fraction of Octane (2) - Liquid mixture 2 |
289.15 |
0.0707 |
323.15 |
0.1109 |
Mole fraction of Phenol, 2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mole fraction of Octane (2) - Liquid mixture 1 |
Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1 |
298.15 |
0.0000 |
0.5093 |
298.15 |
0.0142 |
0.5290 |
298.15 |
0.0334 |
0.5400 |
298.15 |
0.0409 |
0.5530 |
298.15 |
0.0593 |
0.5410 |
298.15 |
0.0634 |
0.5420 |
298.15 |
0.0907 |
0.5390 |
298.15 |
0.1020 |
0.5550 |
298.15 |
0.1080 |
0.5570 |
298.15 |
0.1230 |
0.5700 |
298.15 |
0.1260 |
0.5730 |
298.15 |
0.1360 |
0.5780 |
298.15 |
0.1370 |
0.5820 |
298.15 |
0.1490 |
0.5820 |
298.15 |
0.1530 |
0.5840 |
298.15 |
0.2220 |
0.5900 |
298.15 |
0.2680 |
0.5560 |
298.15 |
0.3260 |
0.5230 |
298.15 |
0.3790 |
0.4860 |
298.15 |
0.3820 |
0.4930 |
298.15 |
0.4350 |
0.4490 |
298.15 |
0.4650 |
0.4390 |
298.15 |
0.6200 |
0.3090 |
298.15 |
0.7290 |
0.2250 |
323.15 |
0.0000 |
0.4917 |
323.15 |
0.0119 |
0.5092 |
323.15 |
0.1128 |
0.5279 |
323.15 |
0.1299 |
0.5179 |
323.15 |
0.1709 |
0.5126 |
323.15 |
0.2428 |
0.4928 |
323.15 |
0.2514 |
0.4878 |
323.15 |
0.2987 |
0.4666 |
323.15 |
0.4283 |
0.4011 |
323.15 |
0.5282 |
0.3400 |
Mole fraction of Phenol, 2-methyl- (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1 |
333.15 |
22.50 |
0.4903 |
333.15 |
24.87 |
0.5202 |
333.15 |
27.18 |
0.4212 |
333.15 |
27.90 |
0.4372 |
333.15 |
28.56 |
0.4308 |
333.15 |
28.98 |
0.4977 |
353.15 |
60.24 |
0.4636 |
353.15 |
63.25 |
0.3275 |
353.15 |
65.29 |
0.3617 |
353.15 |
66.21 |
0.3956 |
353.15 |
66.75 |
0.4834 |
353.15 |
67.53 |
0.4834 |
Mole fraction of Phenol, 2-methyl- (1)
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Pressure, kPa - Gas |
Mole fraction of Phenol, 2-methyl- (1) - Gas |
333.15 |
22.50 |
0.0155 |
333.15 |
24.87 |
0.0161 |
333.15 |
27.18 |
0.0175 |
333.15 |
27.90 |
0.0169 |
333.15 |
28.56 |
0.0175 |
333.15 |
28.98 |
0.0159 |
353.15 |
60.24 |
0.0205 |
353.15 |
63.25 |
0.0199 |
353.15 |
65.29 |
0.0115 |
353.15 |
66.21 |
0.0187 |
353.15 |
66.75 |
0.0186 |
353.15 |
67.53 |
0.0180 |
Mole fraction of Octane (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Octane (2) - Liquid mixture 1 |
333.15 |
22.50 |
0.0291 |
333.15 |
24.87 |
0.0357 |
333.15 |
27.18 |
0.0394 |
333.15 |
27.90 |
0.0545 |
333.15 |
28.56 |
0.0671 |
333.15 |
28.98 |
0.0929 |
353.15 |
60.24 |
0.0337 |
353.15 |
63.25 |
0.0385 |
353.15 |
65.29 |
0.0524 |
353.15 |
66.21 |
0.0661 |
353.15 |
66.75 |
0.0822 |
353.15 |
67.53 |
0.1000 |
Mole fraction of Octane (2)
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Pressure, kPa - Gas |
Mole fraction of Octane (2) - Gas |
333.15 |
22.50 |
0.2338 |
333.15 |
24.87 |
0.2332 |
333.15 |
27.18 |
0.2613 |
333.15 |
27.90 |
0.2746 |
333.15 |
28.56 |
0.3065 |
333.15 |
28.98 |
0.2885 |
353.15 |
60.24 |
0.1992 |
353.15 |
63.25 |
0.2336 |
353.15 |
65.29 |
0.2560 |
353.15 |
66.21 |
0.2617 |
353.15 |
66.75 |
0.2635 |
353.15 |
67.53 |
0.2780 |
Temperature, K x Pressure, kPa x Mole fraction
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Octane (2) - Gas |
Mole fraction of Phenol, 2-methyl- (1) - Gas |
Mole fraction of Octane (2) - Liquid |
Mole fraction of Phenol, 2-methyl- (1) - Liquid |
333.15 |
13.78 |
0.3763 |
0.0222 |
0.0671 |
0.7806 |
333.15 |
14.97 |
0.2171 |
0.0320 |
0.0393 |
0.7460 |
333.15 |
15.05 |
0.1958 |
0.0426 |
0.0341 |
0.7382 |
333.15 |
18.88 |
0.1572 |
0.0286 |
0.0324 |
0.7354 |
333.15 |
20.09 |
0.1546 |
0.0235 |
0.0225 |
0.6342 |
333.15 |
21.31 |
0.2305 |
0.0255 |
0.0330 |
0.6210 |
333.15 |
23.80 |
0.2078 |
0.0153 |
0.0344 |
0.5581 |
353.15 |
48.05 |
0.1591 |
0.0197 |
0.0291 |
0.6170 |
353.15 |
52.66 |
0.1805 |
0.0163 |
0.0330 |
0.5720 |
353.15 |
56.61 |
0.1874 |
0.0131 |
0.0338 |
0.5232 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
353.15 (Liquid)
Fixed |
Measured |
Mole fraction of Octane (2) - Liquid |
Mole fraction of Phenol, 2-methyl- (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0161 |
0.7187 |
38.91 |
0.0170 |
0.6699 |
42.74 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Temperature, K =
353.15 (Liquid)
Fixed |
Measured |
Mole fraction of Octane (2) - Liquid |
Mole fraction of Phenol, 2-methyl- (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0161 |
0.7187 |
38.91 |
0.0170 |
0.6699 |
42.74 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Fixed |
Measured |
Mole fraction of Octane (2) - Liquid |
Mole fraction of Phenol, 2-methyl- (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
0.8184 |
1035.9 |
0.0000 |
0.8443 |
1036.16 |
0.0000 |
0.8903 |
1036.47 |
0.0000 |
0.9409 |
1036.95 |
0.0000 |
1.0000 |
1036.94 |
0.0424 |
0.8084 |
1011.69 |
0.0500 |
0.8939 |
1010.32 |
0.0518 |
0.8442 |
1007.87 |
0.0621 |
0.7675 |
999.87 |
0.0741 |
0.8712 |
998.07 |
0.0779 |
0.9221 |
998.31 |
0.0788 |
0.7778 |
991.93 |
0.1358 |
0.7693 |
964.99 |
0.1372 |
0.7061 |
959.96 |
0.1580 |
0.7108 |
951.38 |
0.1603 |
0.7901 |
956.44 |
0.1634 |
0.8366 |
958.43 |
0.1819 |
0.6695 |
938.15 |
0.1955 |
0.7162 |
936.96 |
0.2128 |
0.6646 |
925.62 |
0.2270 |
0.7273 |
926.72 |
0.2381 |
0.6783 |
917.98 |
0.2569 |
0.7431 |
918.23 |
0.2618 |
0.6041 |
902.27 |
0.2758 |
0.6447 |
902.28 |
0.2898 |
0.6682 |
900.46 |
0.2990 |
0.7010 |
901.26 |
0.3165 |
0.5593 |
879.7 |
0.3212 |
0.5731 |
880.01 |
0.3399 |
0.6211 |
880.83 |
0.3533 |
0.5758 |
871.64 |
0.3600 |
0.6400 |
877.71 |
0.3779 |
0.5091 |
856.4 |
0.3924 |
0.5130 |
853.33 |
0.4206 |
0.4741 |
841.23 |
0.4226 |
0.5433 |
850.56 |
0.4277 |
0.5723 |
853.18 |
0.4328 |
0.5050 |
843.04 |
0.4565 |
0.4588 |
831.2 |
0.4642 |
0.5041 |
836.2 |
0.4784 |
0.4269 |
821.81 |
0.4797 |
0.5203 |
835.08 |
0.4986 |
0.4233 |
817.45 |
0.5188 |
0.4284 |
814.49 |
0.5668 |
0.3657 |
796.64 |
0.5694 |
0.3524 |
794.07 |
0.5787 |
0.4213 |
803.61 |
0.5821 |
0.3720 |
795.24 |
0.5968 |
0.3404 |
787.93 |
0.5996 |
0.3768 |
793.48 |
0.6279 |
0.3045 |
777.63 |
0.6512 |
0.3106 |
775.12 |
0.6607 |
0.3393 |
779.19 |
0.6913 |
0.2607 |
762.39 |
0.6933 |
0.2886 |
767.12 |
0.7003 |
0.2453 |
758.56 |
0.7217 |
0.2477 |
756.84 |
0.7559 |
0.2297 |
750.39 |
0.7569 |
0.2052 |
745.94 |
0.7664 |
0.2336 |
750.13 |
0.8006 |
0.1776 |
737.32 |
0.8032 |
0.1968 |
740.51 |
0.8410 |
0.1301 |
725.73 |
0.8670 |
0.1252 |
723.22 |
0.9112 |
0.0750 |
711.44 |
0.9143 |
0.0857 |
713.35 |
0.9159 |
0.0791 |
712.02 |
0.9384 |
0.0504 |
705.5 |
0.9693 |
0.0273 |
700.33 |
1.0000 |
0.0000 |
694.52 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Fixed |
Measured |
Mole fraction of Octane (2) - Liquid |
Mole fraction of Phenol, 2-methyl- (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
0.8184 |
1035.9 |
0.0000 |
0.8443 |
1036.16 |
0.0000 |
0.8903 |
1036.47 |
0.0000 |
0.9409 |
1036.95 |
0.0000 |
1.0000 |
1036.94 |
0.0424 |
0.8084 |
1011.69 |
0.0500 |
0.8939 |
1010.32 |
0.0518 |
0.8442 |
1007.87 |
0.0621 |
0.7675 |
999.87 |
0.0741 |
0.8712 |
998.07 |
0.0779 |
0.9221 |
998.31 |
0.0788 |
0.7778 |
991.93 |
0.1358 |
0.7693 |
964.99 |
0.1372 |
0.7061 |
959.96 |
0.1580 |
0.7108 |
951.38 |
0.1603 |
0.7901 |
956.44 |
0.1634 |
0.8366 |
958.43 |
0.1819 |
0.6695 |
938.15 |
0.1955 |
0.7162 |
936.96 |
0.2128 |
0.6646 |
925.62 |
0.2270 |
0.7273 |
926.72 |
0.2381 |
0.6783 |
917.98 |
0.2569 |
0.7431 |
918.23 |
0.2618 |
0.6041 |
902.27 |
0.2758 |
0.6447 |
902.28 |
0.2898 |
0.6682 |
900.46 |
0.2990 |
0.7010 |
901.26 |
0.3165 |
0.5593 |
879.7 |
0.3212 |
0.5731 |
880.01 |
0.3399 |
0.6211 |
880.83 |
0.3533 |
0.5758 |
871.64 |
0.3600 |
0.6400 |
877.71 |
0.3779 |
0.5091 |
856.4 |
0.3924 |
0.5130 |
853.33 |
0.4206 |
0.4741 |
841.23 |
0.4226 |
0.5433 |
850.56 |
0.4277 |
0.5723 |
853.18 |
0.4328 |
0.5050 |
843.04 |
0.4565 |
0.4588 |
831.2 |
0.4642 |
0.5041 |
836.2 |
0.4784 |
0.4269 |
821.81 |
0.4797 |
0.5203 |
835.08 |
0.4986 |
0.4233 |
817.45 |
0.5188 |
0.4284 |
814.49 |
0.5668 |
0.3657 |
796.64 |
0.5694 |
0.3524 |
794.07 |
0.5787 |
0.4213 |
803.61 |
0.5821 |
0.3720 |
795.24 |
0.5968 |
0.3404 |
787.93 |
0.5996 |
0.3768 |
793.48 |
0.6279 |
0.3045 |
777.63 |
0.6512 |
0.3106 |
775.12 |
0.6607 |
0.3393 |
779.19 |
0.6913 |
0.2607 |
762.39 |
0.6933 |
0.2886 |
767.12 |
0.7003 |
0.2453 |
758.56 |
0.7217 |
0.2477 |
756.84 |
0.7559 |
0.2297 |
750.39 |
0.7569 |
0.2052 |
745.94 |
0.7664 |
0.2336 |
750.13 |
0.8006 |
0.1776 |
737.32 |
0.8032 |
0.1968 |
740.51 |
0.8410 |
0.1301 |
725.73 |
0.8670 |
0.1252 |
723.22 |
0.9112 |
0.0750 |
711.44 |
0.9143 |
0.0857 |
713.35 |
0.9159 |
0.0791 |
712.02 |
0.9384 |
0.0504 |
705.5 |
0.9693 |
0.0273 |
700.33 |
1.0000 |
0.0000 |
694.52 |
Sources