Mixture of Aniline + Toluene + Cyclohexylamine
Datasets
-
Temperature, K x Pressure, kPa x Mole fraction (2)
Temperature, K x Pressure, kPa x Mole fraction
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Toluene (2) - Liquid |
Mole fraction of Aniline (1) - Liquid |
Mole fraction of Aniline (1) - Gas |
Mole fraction of Toluene (2) - Gas |
333.15 |
5.01 |
0.0691 |
0.5591 |
0.0850 |
0.4176 |
333.15 |
6.13 |
0.1248 |
0.5534 |
0.0635 |
0.5981 |
333.15 |
6.38 |
0.1549 |
0.7383 |
0.0821 |
0.8147 |
333.15 |
7.01 |
0.1147 |
0.3591 |
0.0354 |
0.4380 |
333.15 |
8.31 |
0.2045 |
0.3481 |
0.0295 |
0.6041 |
333.15 |
8.57 |
0.2548 |
0.6128 |
0.0509 |
0.8585 |
333.15 |
8.73 |
0.2609 |
0.7137 |
0.0564 |
0.9273 |
333.15 |
9.65 |
0.1855 |
0.0789 |
0.0049 |
0.4165 |
333.15 |
10.16 |
0.3334 |
0.5135 |
0.0352 |
0.8777 |
333.15 |
10.70 |
0.2914 |
0.1407 |
0.0093 |
0.6047 |
333.15 |
10.74 |
0.3807 |
0.5853 |
0.0416 |
0.9415 |
333.15 |
11.98 |
0.3827 |
0.1675 |
0.0138 |
0.6774 |
333.15 |
12.40 |
0.4863 |
0.3234 |
0.0439 |
0.8729 |
333.15 |
12.59 |
0.5224 |
0.4357 |
0.0268 |
0.9554 |
333.15 |
12.80 |
0.4990 |
0.2214 |
0.0155 |
0.8356 |
333.15 |
13.95 |
0.6329 |
0.3167 |
0.0202 |
0.9597 |
333.15 |
14.84 |
0.7093 |
0.2372 |
0.0153 |
0.9633 |
333.15 |
16.08 |
0.8066 |
0.1343 |
0.0095 |
0.9652 |
333.15 |
16.95 |
0.8658 |
0.0688 |
0.0050 |
0.9668 |
363.15 |
7.24 |
0.0079 |
0.8617 |
0.4118 |
0.1166 |
363.15 |
10.15 |
0.0247 |
0.7718 |
0.2554 |
0.2432 |
363.15 |
13.55 |
0.0483 |
0.6761 |
0.1630 |
0.3296 |
363.15 |
16.50 |
0.0666 |
0.5806 |
0.1031 |
0.3694 |
363.15 |
18.78 |
0.1486 |
0.7473 |
0.1222 |
0.7502 |
363.15 |
19.27 |
0.1183 |
0.5708 |
0.0853 |
0.5396 |
363.15 |
22.00 |
0.1098 |
0.3847 |
0.0521 |
0.3866 |
363.15 |
24.65 |
0.2476 |
0.7283 |
0.0843 |
0.8949 |
363.15 |
25.06 |
0.1861 |
0.3869 |
0.0395 |
0.5596 |
363.15 |
26.36 |
0.2674 |
0.6037 |
0.0665 |
0.8293 |
363.15 |
29.22 |
0.1695 |
0.1305 |
0.0126 |
0.3819 |
363.15 |
30.34 |
0.3611 |
0.6063 |
0.0568 |
0.9221 |
363.15 |
31.06 |
0.3635 |
0.4866 |
0.0485 |
0.8502 |
363.15 |
32.60 |
0.2756 |
0.1472 |
0.0107 |
0.5414 |
363.15 |
35.43 |
0.3827 |
0.1675 |
0.0138 |
0.6774 |
363.15 |
35.80 |
0.4881 |
0.4710 |
0.0419 |
0.9353 |
363.15 |
36.49 |
0.4698 |
0.3155 |
0.0291 |
0.8413 |
363.15 |
39.06 |
0.5192 |
0.2159 |
0.0186 |
0.8254 |
363.15 |
40.27 |
0.6218 |
0.3303 |
0.0295 |
0.9465 |
363.15 |
42.80 |
0.6843 |
0.2633 |
0.0231 |
0.9514 |
363.15 |
45.89 |
0.7674 |
0.1755 |
0.0156 |
0.9570 |
363.15 |
50.04 |
0.8683 |
0.0677 |
0.0059 |
0.9631 |
Temperature, K x Pressure, kPa x Mole fraction
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Toluene (2) - Liquid |
Mole fraction of Aniline (1) - Liquid |
Mole fraction of Aniline (1) - Gas |
Mole fraction of Toluene (2) - Gas |
333.15 |
5.01 |
0.0691 |
0.5591 |
0.0850 |
0.4176 |
333.15 |
6.13 |
0.1248 |
0.5534 |
0.0635 |
0.5981 |
333.15 |
6.38 |
0.1549 |
0.7383 |
0.0821 |
0.8147 |
333.15 |
7.01 |
0.1147 |
0.3591 |
0.0354 |
0.4380 |
333.15 |
8.31 |
0.2045 |
0.3481 |
0.0295 |
0.6041 |
333.15 |
8.57 |
0.2548 |
0.6128 |
0.0509 |
0.8585 |
333.15 |
8.73 |
0.2609 |
0.7137 |
0.0564 |
0.9273 |
333.15 |
9.65 |
0.1855 |
0.0789 |
0.0049 |
0.4165 |
333.15 |
10.16 |
0.3334 |
0.5135 |
0.0352 |
0.8777 |
333.15 |
10.70 |
0.2914 |
0.1407 |
0.0093 |
0.6047 |
333.15 |
10.74 |
0.3807 |
0.5853 |
0.0416 |
0.9415 |
333.15 |
11.98 |
0.3827 |
0.1675 |
0.0138 |
0.6774 |
333.15 |
12.40 |
0.4863 |
0.3234 |
0.0439 |
0.8729 |
333.15 |
12.59 |
0.5224 |
0.4357 |
0.0268 |
0.9554 |
333.15 |
12.80 |
0.4990 |
0.2214 |
0.0155 |
0.8356 |
333.15 |
13.95 |
0.6329 |
0.3167 |
0.0202 |
0.9597 |
333.15 |
14.84 |
0.7093 |
0.2372 |
0.0153 |
0.9633 |
333.15 |
16.08 |
0.8066 |
0.1343 |
0.0095 |
0.9652 |
333.15 |
16.95 |
0.8658 |
0.0688 |
0.0050 |
0.9668 |
363.15 |
7.24 |
0.0079 |
0.8617 |
0.4118 |
0.1166 |
363.15 |
10.15 |
0.0247 |
0.7718 |
0.2554 |
0.2432 |
363.15 |
13.55 |
0.0483 |
0.6761 |
0.1630 |
0.3296 |
363.15 |
16.50 |
0.0666 |
0.5806 |
0.1031 |
0.3694 |
363.15 |
18.78 |
0.1486 |
0.7473 |
0.1222 |
0.7502 |
363.15 |
19.27 |
0.1183 |
0.5708 |
0.0853 |
0.5396 |
363.15 |
22.00 |
0.1098 |
0.3847 |
0.0521 |
0.3866 |
363.15 |
24.65 |
0.2476 |
0.7283 |
0.0843 |
0.8949 |
363.15 |
25.06 |
0.1861 |
0.3869 |
0.0395 |
0.5596 |
363.15 |
26.36 |
0.2674 |
0.6037 |
0.0665 |
0.8293 |
363.15 |
29.22 |
0.1695 |
0.1305 |
0.0126 |
0.3819 |
363.15 |
30.34 |
0.3611 |
0.6063 |
0.0568 |
0.9221 |
363.15 |
31.06 |
0.3635 |
0.4866 |
0.0485 |
0.8502 |
363.15 |
32.60 |
0.2756 |
0.1472 |
0.0107 |
0.5414 |
363.15 |
35.43 |
0.3827 |
0.1675 |
0.0138 |
0.6774 |
363.15 |
35.80 |
0.4881 |
0.4710 |
0.0419 |
0.9353 |
363.15 |
36.49 |
0.4698 |
0.3155 |
0.0291 |
0.8413 |
363.15 |
39.06 |
0.5192 |
0.2159 |
0.0186 |
0.8254 |
363.15 |
40.27 |
0.6218 |
0.3303 |
0.0295 |
0.9465 |
363.15 |
42.80 |
0.6843 |
0.2633 |
0.0231 |
0.9514 |
363.15 |
45.89 |
0.7674 |
0.1755 |
0.0156 |
0.9570 |
363.15 |
50.04 |
0.8683 |
0.0677 |
0.0059 |
0.9631 |
Sources