Mixture of Benzene + Pyrrole
Datasets
-
Excess molar enthalpy (molar enthalpy (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Pyrrole (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0150 |
0.0713 |
| 0.0300 |
0.1226 |
| 0.0448 |
0.1698 |
| 0.0597 |
0.2127 |
| 0.0747 |
0.2528 |
| 0.0896 |
0.2893 |
| 0.1045 |
0.3234 |
| 0.1193 |
0.3545 |
| 0.1343 |
0.3837 |
| 0.1493 |
0.4106 |
| 0.1642 |
0.4352 |
| 0.1792 |
0.4581 |
| 0.1942 |
0.4792 |
| 0.2092 |
0.4988 |
| 0.2242 |
0.5167 |
| 0.2392 |
0.5329 |
| 0.2542 |
0.5471 |
| 0.2691 |
0.5596 |
| 0.2840 |
0.5707 |
| 0.2990 |
0.5805 |
| 0.3140 |
0.5893 |
| 0.3290 |
0.5968 |
| 0.3440 |
0.6032 |
| 0.3590 |
0.6084 |
| 0.3740 |
0.6125 |
| 0.3890 |
0.6156 |
| 0.4040 |
0.6176 |
| 0.4190 |
0.6186 |
| 0.4340 |
0.6186 |
| 0.4490 |
0.6176 |
| 0.4640 |
0.6156 |
| 0.4790 |
0.6127 |
| 0.4940 |
0.6090 |
| 0.5091 |
0.6042 |
| 0.5241 |
0.5986 |
| 0.5391 |
0.5921 |
| 0.5541 |
0.5848 |
| 0.5613 |
0.5844 |
| 0.5683 |
0.5814 |
| 0.5692 |
0.5765 |
| 0.5830 |
0.5744 |
| 0.5842 |
0.5674 |
| 0.5977 |
0.5666 |
| 0.5993 |
0.5575 |
| 0.6122 |
0.5581 |
| 0.6143 |
0.5468 |
| 0.6267 |
0.5490 |
| 0.6411 |
0.5391 |
| 0.6554 |
0.5283 |
| 0.6696 |
0.5170 |
| 0.6838 |
0.5052 |
| 0.6978 |
0.4923 |
| 0.7118 |
0.4786 |
| 0.7257 |
0.4643 |
| 0.7395 |
0.4494 |
| 0.7533 |
0.4334 |
| 0.7669 |
0.4169 |
| 0.7805 |
0.3998 |
| 0.7940 |
0.3820 |
| 0.8074 |
0.3632 |
| 0.8208 |
0.3441 |
| 0.8341 |
0.3240 |
| 0.8473 |
0.3037 |
| 0.8604 |
0.2822 |
| 0.8735 |
0.2603 |
| 0.8865 |
0.2374 |
| 0.8993 |
0.2137 |
| 0.9121 |
0.1893 |
| 0.9249 |
0.1642 |
| 0.9377 |
0.1384 |
| 0.9502 |
0.1125 |
| 0.9628 |
0.0851 |
| 0.9753 |
0.0578 |
| 0.9877 |
0.0292 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Pyrrole (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0150 |
0.0713 |
| 0.0300 |
0.1226 |
| 0.0448 |
0.1698 |
| 0.0597 |
0.2127 |
| 0.0747 |
0.2528 |
| 0.0896 |
0.2893 |
| 0.1045 |
0.3234 |
| 0.1193 |
0.3545 |
| 0.1343 |
0.3837 |
| 0.1493 |
0.4106 |
| 0.1642 |
0.4352 |
| 0.1792 |
0.4581 |
| 0.1942 |
0.4792 |
| 0.2092 |
0.4988 |
| 0.2242 |
0.5167 |
| 0.2392 |
0.5329 |
| 0.2542 |
0.5471 |
| 0.2691 |
0.5596 |
| 0.2840 |
0.5707 |
| 0.2990 |
0.5805 |
| 0.3140 |
0.5893 |
| 0.3290 |
0.5968 |
| 0.3440 |
0.6032 |
| 0.3590 |
0.6084 |
| 0.3740 |
0.6125 |
| 0.3890 |
0.6156 |
| 0.4040 |
0.6176 |
| 0.4190 |
0.6186 |
| 0.4340 |
0.6186 |
| 0.4490 |
0.6176 |
| 0.4640 |
0.6156 |
| 0.4790 |
0.6127 |
| 0.4940 |
0.6090 |
| 0.5091 |
0.6042 |
| 0.5241 |
0.5986 |
| 0.5391 |
0.5921 |
| 0.5541 |
0.5848 |
| 0.5613 |
0.5844 |
| 0.5683 |
0.5814 |
| 0.5692 |
0.5765 |
| 0.5830 |
0.5744 |
| 0.5842 |
0.5674 |
| 0.5977 |
0.5666 |
| 0.5993 |
0.5575 |
| 0.6122 |
0.5581 |
| 0.6143 |
0.5468 |
| 0.6267 |
0.5490 |
| 0.6411 |
0.5391 |
| 0.6554 |
0.5283 |
| 0.6696 |
0.5170 |
| 0.6838 |
0.5052 |
| 0.6978 |
0.4923 |
| 0.7118 |
0.4786 |
| 0.7257 |
0.4643 |
| 0.7395 |
0.4494 |
| 0.7533 |
0.4334 |
| 0.7669 |
0.4169 |
| 0.7805 |
0.3998 |
| 0.7940 |
0.3820 |
| 0.8074 |
0.3632 |
| 0.8208 |
0.3441 |
| 0.8341 |
0.3240 |
| 0.8473 |
0.3037 |
| 0.8604 |
0.2822 |
| 0.8735 |
0.2603 |
| 0.8865 |
0.2374 |
| 0.8993 |
0.2137 |
| 0.9121 |
0.1893 |
| 0.9249 |
0.1642 |
| 0.9377 |
0.1384 |
| 0.9502 |
0.1125 |
| 0.9628 |
0.0851 |
| 0.9753 |
0.0578 |
| 0.9877 |
0.0292 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Pyrrole (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 1.0000 |
338.15 |
9.40 |
| 0.9237 |
338.15 |
15.10 |
| 0.9024 |
338.15 |
17.50 |
| 0.8386 |
338.15 |
22.20 |
| 0.7836 |
338.15 |
25.70 |
| 0.6780 |
338.15 |
32.00 |
| 0.6208 |
338.15 |
35.00 |
| 0.5489 |
338.15 |
38.40 |
| 0.4828 |
338.15 |
41.40 |
| 0.4267 |
338.15 |
43.80 |
| 0.3799 |
338.15 |
45.70 |
| 0.3319 |
338.15 |
47.50 |
| 0.2982 |
338.15 |
49.00 |
| 0.2356 |
338.15 |
51.50 |
| 0.1767 |
338.15 |
53.80 |
| 0.1353 |
338.15 |
55.60 |
| 0.0000 |
338.15 |
62.10 |
| 1.0000 |
348.15 |
14.60 |
| 0.9857 |
348.15 |
16.30 |
| 0.9685 |
348.15 |
17.90 |
| 0.9485 |
348.15 |
20.50 |
| 0.9296 |
348.15 |
22.50 |
| 0.8980 |
348.15 |
25.90 |
| 0.8778 |
348.15 |
26.60 |
| 0.8328 |
348.15 |
32.10 |
| 0.7821 |
348.15 |
36.80 |
| 0.7269 |
348.15 |
41.30 |
| 0.6735 |
348.15 |
45.40 |
| 0.6172 |
348.15 |
49.60 |
| 0.5438 |
348.15 |
54.10 |
| 0.4713 |
348.15 |
58.40 |
| 0.4203 |
348.15 |
61.40 |
| 0.3740 |
348.15 |
64.00 |
| 0.3298 |
348.15 |
66.40 |
| 0.2964 |
348.15 |
68.30 |
| 0.2275 |
348.15 |
71.70 |
| 0.1738 |
348.15 |
74.90 |
| 0.1314 |
348.15 |
77.30 |
| 0.0000 |
348.15 |
86.40 |
| 1.0000 |
358.15 |
21.90 |
| 0.9832 |
358.15 |
24.30 |
| 0.9667 |
358.15 |
26.60 |
| 0.9442 |
358.15 |
30.40 |
| 0.9328 |
358.15 |
32.50 |
| 0.8779 |
358.15 |
37.80 |
| 0.8285 |
358.15 |
45.60 |
| 0.7761 |
358.15 |
51.60 |
| 0.7206 |
358.15 |
57.30 |
| 0.6652 |
358.15 |
62.90 |
| 0.6062 |
358.15 |
68.60 |
| 0.5339 |
358.15 |
74.50 |
| 0.4659 |
358.15 |
79.70 |
| 0.4152 |
358.15 |
83.80 |
| 0.3709 |
358.15 |
87.30 |
| 0.3310 |
358.15 |
90.20 |
| 0.2832 |
358.15 |
93.10 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Pyrrole (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 1.0000 |
338.15 |
9.40 |
| 0.9237 |
338.15 |
15.10 |
| 0.9024 |
338.15 |
17.50 |
| 0.8386 |
338.15 |
22.20 |
| 0.7836 |
338.15 |
25.70 |
| 0.6780 |
338.15 |
32.00 |
| 0.6208 |
338.15 |
35.00 |
| 0.5489 |
338.15 |
38.40 |
| 0.4828 |
338.15 |
41.40 |
| 0.4267 |
338.15 |
43.80 |
| 0.3799 |
338.15 |
45.70 |
| 0.3319 |
338.15 |
47.50 |
| 0.2982 |
338.15 |
49.00 |
| 0.2356 |
338.15 |
51.50 |
| 0.1767 |
338.15 |
53.80 |
| 0.1353 |
338.15 |
55.60 |
| 0.0000 |
338.15 |
62.10 |
| 1.0000 |
348.15 |
14.60 |
| 0.9857 |
348.15 |
16.30 |
| 0.9685 |
348.15 |
17.90 |
| 0.9485 |
348.15 |
20.50 |
| 0.9296 |
348.15 |
22.50 |
| 0.8980 |
348.15 |
25.90 |
| 0.8778 |
348.15 |
26.60 |
| 0.8328 |
348.15 |
32.10 |
| 0.7821 |
348.15 |
36.80 |
| 0.7269 |
348.15 |
41.30 |
| 0.6735 |
348.15 |
45.40 |
| 0.6172 |
348.15 |
49.60 |
| 0.5438 |
348.15 |
54.10 |
| 0.4713 |
348.15 |
58.40 |
| 0.4203 |
348.15 |
61.40 |
| 0.3740 |
348.15 |
64.00 |
| 0.3298 |
348.15 |
66.40 |
| 0.2964 |
348.15 |
68.30 |
| 0.2275 |
348.15 |
71.70 |
| 0.1738 |
348.15 |
74.90 |
| 0.1314 |
348.15 |
77.30 |
| 0.0000 |
348.15 |
86.40 |
| 1.0000 |
358.15 |
21.90 |
| 0.9832 |
358.15 |
24.30 |
| 0.9667 |
358.15 |
26.60 |
| 0.9442 |
358.15 |
30.40 |
| 0.9328 |
358.15 |
32.50 |
| 0.8779 |
358.15 |
37.80 |
| 0.8285 |
358.15 |
45.60 |
| 0.7761 |
358.15 |
51.60 |
| 0.7206 |
358.15 |
57.30 |
| 0.6652 |
358.15 |
62.90 |
| 0.6062 |
358.15 |
68.60 |
| 0.5339 |
358.15 |
74.50 |
| 0.4659 |
358.15 |
79.70 |
| 0.4152 |
358.15 |
83.80 |
| 0.3709 |
358.15 |
87.30 |
| 0.3310 |
358.15 |
90.20 |
| 0.2832 |
358.15 |
93.10 |
Sources