Datasets
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Temperature, K x Pressure, kPa x Mole fraction (6)
Temperature, K x Pressure, kPa x Mole fraction
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Octane (2) - Liquid |
Mole fraction of Aniline (1) - Liquid |
Mole fraction of Aniline (1) - Gas |
Mole fraction of Octane (2) - Gas |
333.15 |
6.92 |
0.0813 |
0.8726 |
0.0885 |
0.8813 |
333.15 |
7.43 |
0.1273 |
0.3603 |
0.0891 |
0.5836 |
333.15 |
8.94 |
0.1486 |
0.0169 |
0.0025 |
0.2650 |
333.15 |
8.95 |
0.2678 |
0.2124 |
0.0223 |
0.5788 |
333.15 |
9.32 |
0.2480 |
0.0097 |
0.0015 |
0.4576 |
333.15 |
9.39 |
0.3754 |
0.0358 |
0.0014 |
0.6055 |
333.15 |
9.79 |
0.2807 |
0.0269 |
0.0038 |
0.4210 |
333.15 |
10.02 |
0.5528 |
0.0222 |
0.0053 |
0.7645 |
333.15 |
10.07 |
0.6099 |
0.1407 |
0.0512 |
0.7258 |
333.15 |
10.42 |
0.6881 |
0.1107 |
0.0290 |
0.8018 |
363.15 |
23.32 |
0.1563 |
0.5506 |
0.0537 |
0.6566 |
363.15 |
23.88 |
0.1096 |
0.1814 |
0.0372 |
0.3247 |
363.15 |
26.18 |
0.1786 |
0.5154 |
0.0572 |
0.6540 |
363.15 |
27.92 |
0.3180 |
0.2561 |
0.0568 |
0.6827 |
363.15 |
28.32 |
0.1391 |
0.0083 |
0.0024 |
0.2504 |
363.15 |
28.88 |
0.1593 |
0.0081 |
0.0008 |
0.3131 |
363.15 |
29.22 |
0.2009 |
0.0072 |
0.0009 |
0.3601 |
363.15 |
30.64 |
0.2767 |
0.0105 |
0.0039 |
0.4566 |
363.15 |
31.39 |
0.4743 |
0.0459 |
0.0045 |
0.6580 |
363.15 |
32.04 |
0.6918 |
0.1590 |
0.1111 |
0.7606 |
363.15 |
32.71 |
0.7566 |
0.1137 |
0.0396 |
0.8363 |
Mole fraction of Cyclohexylamine (3)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mole fraction of Aniline (1) - Liquid mixture 1 |
Mole fraction of Cyclohexylamine (3) - Liquid mixture 1 |
298.15 |
0.0860 |
0.0000 |
298.15 |
0.0960 |
0.0080 |
298.15 |
0.1060 |
0.0180 |
298.15 |
0.1210 |
0.0330 |
298.15 |
0.1380 |
0.0470 |
298.15 |
0.1580 |
0.0650 |
298.15 |
0.2000 |
0.0900 |
298.15 |
0.2410 |
0.1080 |
298.15 |
0.2980 |
0.1260 |
298.15 |
0.3840 |
0.1430 |
298.15 |
0.4520 |
0.1530 |
298.15 |
0.5640 |
0.1600 |
298.15 |
0.6610 |
0.1520 |
298.15 |
0.7420 |
0.1280 |
298.15 |
0.8370 |
0.0820 |
298.15 |
0.9220 |
0.0260 |
298.15 |
0.9550 |
0.0000 |
333.15 |
0.2750 |
0.0000 |
333.15 |
0.3030 |
0.0100 |
333.15 |
0.3300 |
0.0190 |
333.15 |
0.3670 |
0.0260 |
333.15 |
0.4190 |
0.0350 |
333.15 |
0.4770 |
0.0400 |
333.15 |
0.5000 |
0.0420 |
333.15 |
0.5370 |
0.0420 |
333.15 |
0.5850 |
0.0450 |
333.15 |
0.6020 |
0.0440 |
333.15 |
0.6130 |
0.0450 |
333.15 |
0.6230 |
0.0430 |
333.15 |
0.6470 |
0.0430 |
333.15 |
0.6760 |
0.0420 |
333.15 |
0.7380 |
0.0350 |
333.15 |
0.8090 |
0.0210 |
333.15 |
0.8650 |
0.0000 |
Temperature, K x Mole fraction
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mole fraction of Aniline (1) - Liquid mixture 2 |
Mole fraction of Cyclohexylamine (3) - Liquid mixture 2 |
Mole fraction of Cyclohexylamine (3) - Liquid mixture 1 |
Mole fraction of Aniline (1) - Liquid mixture 1 |
298.15 |
0.8150 |
0.0800 |
0.0510 |
0.1670 |
298.15 |
0.8940 |
0.0300 |
0.0140 |
0.1060 |
298.15 |
0.6610 |
0.1520 |
0.0880 |
0.2290 |
333.15 |
0.7460 |
0.0310 |
0.0190 |
0.3300 |
333.15 |
0.8670 |
0.0070 |
0.0070 |
0.3020 |
Temperature, K x Pressure, kPa x Mole fraction
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Octane (2) - Liquid |
Mole fraction of Aniline (1) - Liquid |
Mole fraction of Aniline (1) - Gas |
Mole fraction of Octane (2) - Gas |
333.15 |
6.92 |
0.0813 |
0.8726 |
0.0885 |
0.8813 |
333.15 |
7.43 |
0.1273 |
0.3603 |
0.0891 |
0.5836 |
333.15 |
8.94 |
0.1486 |
0.0169 |
0.0025 |
0.2650 |
333.15 |
8.95 |
0.2678 |
0.2124 |
0.0223 |
0.5788 |
333.15 |
9.32 |
0.2480 |
0.0097 |
0.0015 |
0.4576 |
333.15 |
9.39 |
0.3754 |
0.0358 |
0.0014 |
0.6055 |
333.15 |
9.79 |
0.2807 |
0.0269 |
0.0038 |
0.4210 |
333.15 |
10.02 |
0.5528 |
0.0222 |
0.0053 |
0.7645 |
333.15 |
10.07 |
0.6099 |
0.1407 |
0.0512 |
0.7258 |
333.15 |
10.42 |
0.6881 |
0.1107 |
0.0290 |
0.8018 |
363.15 |
23.32 |
0.1563 |
0.5506 |
0.0537 |
0.6566 |
363.15 |
23.88 |
0.1096 |
0.1814 |
0.0372 |
0.3247 |
363.15 |
26.18 |
0.1786 |
0.5154 |
0.0572 |
0.6540 |
363.15 |
27.92 |
0.3180 |
0.2561 |
0.0568 |
0.6827 |
363.15 |
28.32 |
0.1391 |
0.0083 |
0.0024 |
0.2504 |
363.15 |
28.88 |
0.1593 |
0.0081 |
0.0008 |
0.3131 |
363.15 |
29.22 |
0.2009 |
0.0072 |
0.0009 |
0.3601 |
363.15 |
30.64 |
0.2767 |
0.0105 |
0.0039 |
0.4566 |
363.15 |
31.39 |
0.4743 |
0.0459 |
0.0045 |
0.6580 |
363.15 |
32.04 |
0.6918 |
0.1590 |
0.1111 |
0.7606 |
363.15 |
32.71 |
0.7566 |
0.1137 |
0.0396 |
0.8363 |
Mole fraction of Cyclohexylamine (3)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mole fraction of Aniline (1) - Liquid mixture 1 |
Mole fraction of Cyclohexylamine (3) - Liquid mixture 1 |
298.15 |
0.0860 |
0.0000 |
298.15 |
0.0960 |
0.0080 |
298.15 |
0.1060 |
0.0180 |
298.15 |
0.1210 |
0.0330 |
298.15 |
0.1380 |
0.0470 |
298.15 |
0.1580 |
0.0650 |
298.15 |
0.2000 |
0.0900 |
298.15 |
0.2410 |
0.1080 |
298.15 |
0.2980 |
0.1260 |
298.15 |
0.3840 |
0.1430 |
298.15 |
0.4520 |
0.1530 |
298.15 |
0.5640 |
0.1600 |
298.15 |
0.6610 |
0.1520 |
298.15 |
0.7420 |
0.1280 |
298.15 |
0.8370 |
0.0820 |
298.15 |
0.9220 |
0.0260 |
298.15 |
0.9550 |
0.0000 |
333.15 |
0.2750 |
0.0000 |
333.15 |
0.3030 |
0.0100 |
333.15 |
0.3300 |
0.0190 |
333.15 |
0.3670 |
0.0260 |
333.15 |
0.4190 |
0.0350 |
333.15 |
0.4770 |
0.0400 |
333.15 |
0.5000 |
0.0420 |
333.15 |
0.5370 |
0.0420 |
333.15 |
0.5850 |
0.0450 |
333.15 |
0.6020 |
0.0440 |
333.15 |
0.6130 |
0.0450 |
333.15 |
0.6230 |
0.0430 |
333.15 |
0.6470 |
0.0430 |
333.15 |
0.6760 |
0.0420 |
333.15 |
0.7380 |
0.0350 |
333.15 |
0.8090 |
0.0210 |
333.15 |
0.8650 |
0.0000 |
Temperature, K x Mole fraction
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mole fraction of Aniline (1) - Liquid mixture 2 |
Mole fraction of Cyclohexylamine (3) - Liquid mixture 2 |
Mole fraction of Cyclohexylamine (3) - Liquid mixture 1 |
Mole fraction of Aniline (1) - Liquid mixture 1 |
298.15 |
0.8150 |
0.0800 |
0.0510 |
0.1670 |
298.15 |
0.8940 |
0.0300 |
0.0140 |
0.1060 |
298.15 |
0.6610 |
0.1520 |
0.0880 |
0.2290 |
333.15 |
0.7460 |
0.0310 |
0.0190 |
0.3300 |
333.15 |
0.8670 |
0.0070 |
0.0070 |
0.3020 |
Sources