Datasets
-
Mole fraction (30)
-
Tboil - Boiling temperature at pressure P, K (2)
-
Vapor Liquid Equilibrium at Constant Temperature (3)
Mole fraction of p-Xylene (1)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of p-Xylene (1) - Liquid mixture 2 |
| 303.20 |
0.0000 |
| 323.20 |
0.0000 |
| 343.20 |
0.0001 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 303.20 |
0.0030 |
| 323.20 |
0.0047 |
| 343.20 |
0.0073 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 573.00 |
11200.00 |
0.9890 |
| 573.00 |
13900.00 |
0.9850 |
| 573.00 |
15600.00 |
0.9870 |
| 573.00 |
18000.00 |
0.9860 |
| 573.00 |
20700.00 |
0.9910 |
| 583.00 |
12000.00 |
0.9870 |
| 583.00 |
15200.00 |
0.9760 |
| 583.00 |
15600.00 |
0.9830 |
| 583.00 |
19400.00 |
0.9820 |
| 583.00 |
22600.00 |
0.9830 |
| 593.00 |
13600.00 |
0.9810 |
| 593.00 |
15600.00 |
0.9680 |
| 593.00 |
17500.00 |
0.9660 |
| 593.00 |
19400.00 |
0.9710 |
| 593.00 |
23000.00 |
0.9780 |
| 603.00 |
13300.00 |
0.9970 |
| 603.00 |
14100.00 |
0.9930 |
| 603.00 |
15100.00 |
0.9790 |
| 603.00 |
16200.00 |
0.9730 |
| 603.00 |
18200.00 |
0.9800 |
| 603.00 |
20200.00 |
0.9780 |
| 603.00 |
21100.00 |
0.9840 |
| 613.00 |
16200.00 |
0.9960 |
| 613.00 |
17300.00 |
0.9790 |
| 623.00 |
17200.00 |
0.9940 |
| 623.00 |
19700.00 |
0.9810 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 2 |
| 573.00 |
11200.00 |
0.6840 |
| 573.00 |
13900.00 |
0.6370 |
| 573.00 |
15600.00 |
0.6450 |
| 573.00 |
18000.00 |
0.6460 |
| 573.00 |
20700.00 |
0.5670 |
| 583.00 |
12000.00 |
0.8550 |
| 583.00 |
15200.00 |
0.7530 |
| 583.00 |
15600.00 |
0.7480 |
| 583.00 |
19400.00 |
0.7080 |
| 583.00 |
22600.00 |
0.6840 |
| 593.00 |
13600.00 |
0.8800 |
| 593.00 |
15600.00 |
0.8140 |
| 593.00 |
17500.00 |
0.8040 |
| 593.00 |
19400.00 |
0.7830 |
| 593.00 |
23000.00 |
0.7480 |
| 603.00 |
13300.00 |
0.9700 |
| 603.00 |
14100.00 |
0.9460 |
| 603.00 |
15100.00 |
0.9060 |
| 603.00 |
16200.00 |
0.8700 |
| 603.00 |
18200.00 |
0.8670 |
| 603.00 |
20200.00 |
0.8400 |
| 603.00 |
21100.00 |
0.8380 |
| 613.00 |
16200.00 |
0.9770 |
| 613.00 |
17300.00 |
0.9270 |
| 623.00 |
17200.00 |
0.9800 |
| 623.00 |
19700.00 |
0.9440 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Pressure, kPa - Gas |
Mole fraction of Water (2) - Gas |
| 573.00 |
6100.00 |
0.6080 |
| 573.00 |
7800.00 |
0.6370 |
| 573.00 |
9600.00 |
0.6950 |
| 573.00 |
10300.00 |
0.6570 |
| 583.00 |
4300.00 |
0.3710 |
| 583.00 |
5000.00 |
0.4410 |
| 583.00 |
6000.00 |
0.5070 |
| 583.00 |
6900.00 |
0.5180 |
| 583.00 |
7700.00 |
0.5380 |
| 583.00 |
8400.00 |
0.5630 |
| 583.00 |
9000.00 |
0.5530 |
| 583.00 |
9400.00 |
0.5580 |
| 593.00 |
4900.00 |
0.3590 |
| 593.00 |
5500.00 |
0.4200 |
| 593.00 |
6400.00 |
0.4330 |
| 593.00 |
6900.00 |
0.4550 |
| 593.00 |
7400.00 |
0.4630 |
| 603.00 |
4700.00 |
0.3030 |
| 603.00 |
5800.00 |
0.3490 |
| 603.00 |
6100.00 |
0.3700 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Water (2) - Liquid |
| 573.00 |
6100.00 |
0.2060 |
| 573.00 |
7800.00 |
0.3310 |
| 573.00 |
9600.00 |
0.4660 |
| 573.00 |
10300.00 |
0.6400 |
| 583.00 |
4300.00 |
0.0740 |
| 583.00 |
5000.00 |
0.1510 |
| 583.00 |
6000.00 |
0.1830 |
| 583.00 |
6900.00 |
0.2910 |
| 583.00 |
7700.00 |
0.3070 |
| 583.00 |
8400.00 |
0.3630 |
| 583.00 |
9000.00 |
0.3590 |
| 583.00 |
9400.00 |
0.4280 |
| 593.00 |
4900.00 |
0.1420 |
| 593.00 |
5500.00 |
0.2050 |
| 593.00 |
6400.00 |
0.2650 |
| 593.00 |
6900.00 |
0.2960 |
| 593.00 |
7400.00 |
0.3060 |
| 603.00 |
4700.00 |
0.1240 |
| 603.00 |
5800.00 |
0.2070 |
| 603.00 |
6100.00 |
0.2060 |
Mass fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 1 |
| 298.15 |
100.00 |
0.9756 |
Mass fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 2 |
| 298.15 |
100.00 |
0.0267 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 313.15 |
0.0030 |
| 365.40 |
0.0100 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid |
Mole fraction of Water (2) - Liquid |
Mole fraction of Water (2) - Gas |
| 101.30 |
0.0100 |
0.7590 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid mixture 1 |
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 101.30 |
303.15 |
0.0032 |
Mole fraction of p-Xylene (1)
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid mixture 2 |
Temperature, K - Liquid mixture 2 |
Mole fraction of p-Xylene (1) - Liquid mixture 2 |
| 101.30 |
303.15 |
0.0000 |
Mole fraction of p-Xylene (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of p-Xylene (1) - Liquid mixture 2 |
| 288.15 |
2.40 |
0.0000 |
| 298.15 |
4.40 |
0.0000 |
| 313.15 |
10.30 |
0.0000 |
| 333.15 |
27.00 |
0.0001 |
| 348.15 |
52.00 |
0.0001 |
| 373.15 |
136.00 |
0.0001 |
| 398.15 |
310.00 |
0.0002 |
| 423.15 |
630.00 |
0.0003 |
| 448.15 |
1170.00 |
0.0006 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 288.15 |
2.40 |
0.0024 |
| 298.15 |
4.40 |
0.0033 |
| 313.15 |
10.30 |
0.0046 |
| 333.15 |
27.00 |
0.0082 |
| 348.15 |
52.00 |
0.0124 |
| 373.15 |
136.00 |
0.0216 |
| 398.15 |
310.00 |
0.0398 |
| 423.15 |
630.00 |
0.0656 |
| 448.15 |
1170.00 |
0.1020 |
Henry's Law constant (molality scale), kPa*kg/mol of p-Xylene (1)
[ref]
Operational condition: Molality, mol/kg =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (molality scale), kPa*kg/mol of p-Xylene (1) - Liquid |
| 274.15 |
146.96 |
| 294.65 |
381.29 |
| 294.65 |
438.72 |
| 296.15 |
456.99 |
| 310.15 |
409.23 |
| 313.15 |
1171.2 |
| 326.15 |
2092.4 |
| 331.15 |
1813.2 |
Mole fraction of p-Xylene (1)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of p-Xylene (1) - Liquid mixture 2 |
| 303.20 |
0.0000 |
| 323.20 |
0.0000 |
| 343.20 |
0.0001 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 303.20 |
0.0030 |
| 323.20 |
0.0047 |
| 343.20 |
0.0073 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 573.00 |
11200.00 |
0.9890 |
| 573.00 |
13900.00 |
0.9850 |
| 573.00 |
15600.00 |
0.9870 |
| 573.00 |
18000.00 |
0.9860 |
| 573.00 |
20700.00 |
0.9910 |
| 583.00 |
12000.00 |
0.9870 |
| 583.00 |
15200.00 |
0.9760 |
| 583.00 |
15600.00 |
0.9830 |
| 583.00 |
19400.00 |
0.9820 |
| 583.00 |
22600.00 |
0.9830 |
| 593.00 |
13600.00 |
0.9810 |
| 593.00 |
15600.00 |
0.9680 |
| 593.00 |
17500.00 |
0.9660 |
| 593.00 |
19400.00 |
0.9710 |
| 593.00 |
23000.00 |
0.9780 |
| 603.00 |
13300.00 |
0.9970 |
| 603.00 |
14100.00 |
0.9930 |
| 603.00 |
15100.00 |
0.9790 |
| 603.00 |
16200.00 |
0.9730 |
| 603.00 |
18200.00 |
0.9800 |
| 603.00 |
20200.00 |
0.9780 |
| 603.00 |
21100.00 |
0.9840 |
| 613.00 |
16200.00 |
0.9960 |
| 613.00 |
17300.00 |
0.9790 |
| 623.00 |
17200.00 |
0.9940 |
| 623.00 |
19700.00 |
0.9810 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 2 |
| 573.00 |
11200.00 |
0.6840 |
| 573.00 |
13900.00 |
0.6370 |
| 573.00 |
15600.00 |
0.6450 |
| 573.00 |
18000.00 |
0.6460 |
| 573.00 |
20700.00 |
0.5670 |
| 583.00 |
12000.00 |
0.8550 |
| 583.00 |
15200.00 |
0.7530 |
| 583.00 |
15600.00 |
0.7480 |
| 583.00 |
19400.00 |
0.7080 |
| 583.00 |
22600.00 |
0.6840 |
| 593.00 |
13600.00 |
0.8800 |
| 593.00 |
15600.00 |
0.8140 |
| 593.00 |
17500.00 |
0.8040 |
| 593.00 |
19400.00 |
0.7830 |
| 593.00 |
23000.00 |
0.7480 |
| 603.00 |
13300.00 |
0.9700 |
| 603.00 |
14100.00 |
0.9460 |
| 603.00 |
15100.00 |
0.9060 |
| 603.00 |
16200.00 |
0.8700 |
| 603.00 |
18200.00 |
0.8670 |
| 603.00 |
20200.00 |
0.8400 |
| 603.00 |
21100.00 |
0.8380 |
| 613.00 |
16200.00 |
0.9770 |
| 613.00 |
17300.00 |
0.9270 |
| 623.00 |
17200.00 |
0.9800 |
| 623.00 |
19700.00 |
0.9440 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Pressure, kPa - Gas |
Mole fraction of Water (2) - Gas |
| 573.00 |
6100.00 |
0.6080 |
| 573.00 |
7800.00 |
0.6370 |
| 573.00 |
9600.00 |
0.6950 |
| 573.00 |
10300.00 |
0.6570 |
| 583.00 |
4300.00 |
0.3710 |
| 583.00 |
5000.00 |
0.4410 |
| 583.00 |
6000.00 |
0.5070 |
| 583.00 |
6900.00 |
0.5180 |
| 583.00 |
7700.00 |
0.5380 |
| 583.00 |
8400.00 |
0.5630 |
| 583.00 |
9000.00 |
0.5530 |
| 583.00 |
9400.00 |
0.5580 |
| 593.00 |
4900.00 |
0.3590 |
| 593.00 |
5500.00 |
0.4200 |
| 593.00 |
6400.00 |
0.4330 |
| 593.00 |
6900.00 |
0.4550 |
| 593.00 |
7400.00 |
0.4630 |
| 603.00 |
4700.00 |
0.3030 |
| 603.00 |
5800.00 |
0.3490 |
| 603.00 |
6100.00 |
0.3700 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Water (2) - Liquid |
| 573.00 |
6100.00 |
0.2060 |
| 573.00 |
7800.00 |
0.3310 |
| 573.00 |
9600.00 |
0.4660 |
| 573.00 |
10300.00 |
0.6400 |
| 583.00 |
4300.00 |
0.0740 |
| 583.00 |
5000.00 |
0.1510 |
| 583.00 |
6000.00 |
0.1830 |
| 583.00 |
6900.00 |
0.2910 |
| 583.00 |
7700.00 |
0.3070 |
| 583.00 |
8400.00 |
0.3630 |
| 583.00 |
9000.00 |
0.3590 |
| 583.00 |
9400.00 |
0.4280 |
| 593.00 |
4900.00 |
0.1420 |
| 593.00 |
5500.00 |
0.2050 |
| 593.00 |
6400.00 |
0.2650 |
| 593.00 |
6900.00 |
0.2960 |
| 593.00 |
7400.00 |
0.3060 |
| 603.00 |
4700.00 |
0.1240 |
| 603.00 |
5800.00 |
0.2070 |
| 603.00 |
6100.00 |
0.2060 |
Mass fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 1 |
| 298.15 |
100.00 |
0.9756 |
Mass fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 2 |
Pressure, kPa - Liquid mixture 2 |
Mass fraction of Water (2) - Liquid mixture 2 |
| 298.15 |
100.00 |
0.0267 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 313.15 |
0.0030 |
| 365.40 |
0.0100 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid |
Mole fraction of Water (2) - Liquid |
Mole fraction of Water (2) - Gas |
| 101.30 |
0.0100 |
0.7590 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid mixture 1 |
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 101.30 |
303.15 |
0.0032 |
Mole fraction of p-Xylene (1)
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid mixture 2 |
Temperature, K - Liquid mixture 2 |
Mole fraction of p-Xylene (1) - Liquid mixture 2 |
| 101.30 |
303.15 |
0.0000 |
Mole fraction of p-Xylene (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of p-Xylene (1) - Liquid mixture 2 |
| 288.15 |
2.40 |
0.0000 |
| 298.15 |
4.40 |
0.0000 |
| 313.15 |
10.30 |
0.0000 |
| 333.15 |
27.00 |
0.0001 |
| 348.15 |
52.00 |
0.0001 |
| 373.15 |
136.00 |
0.0001 |
| 398.15 |
310.00 |
0.0002 |
| 423.15 |
630.00 |
0.0003 |
| 448.15 |
1170.00 |
0.0006 |
Mole fraction of Water (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 288.15 |
2.40 |
0.0024 |
| 298.15 |
4.40 |
0.0033 |
| 313.15 |
10.30 |
0.0046 |
| 333.15 |
27.00 |
0.0082 |
| 348.15 |
52.00 |
0.0124 |
| 373.15 |
136.00 |
0.0216 |
| 398.15 |
310.00 |
0.0398 |
| 423.15 |
630.00 |
0.0656 |
| 448.15 |
1170.00 |
0.1020 |
Henry's Law constant (molality scale), kPa*kg/mol of p-Xylene (1)
[ref]
Operational condition: Molality, mol/kg =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (molality scale), kPa*kg/mol of p-Xylene (1) - Liquid |
| 274.15 |
146.96 |
| 294.65 |
381.29 |
| 294.65 |
438.72 |
| 296.15 |
456.99 |
| 310.15 |
409.23 |
| 313.15 |
1171.2 |
| 326.15 |
2092.4 |
| 331.15 |
1813.2 |
Boiling temperature at pressure P, K
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid |
Mole fraction of Water (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 101.30 |
0.0100 |
365.40 |
Boiling temperature at pressure P, K
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid |
Mole fraction of Water (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 101.30 |
0.0100 |
365.40 |
Vapor Liquid Equilibrium at Constant Temperature
[ref]
Operational condition: Temperature, K =
573 (VLE)
| Fixed |
Measured |
| P [kPa] - VLE |
x1[mol/mol] of Water (2) - Liquid |
y1[mol/mol] of Water (2) - Vapour |
| 6100.005 |
0.2060 |
0.6080 |
| 7799.999 |
0.3310 |
0.6370 |
| 9599.997 |
0.4660 |
0.6950 |
| 10299.994 |
0.6400 |
0.6570 |
Vapor Liquid Equilibrium at Constant Temperature
[ref]
Operational condition: Temperature, K =
583 (VLE)
| Fixed |
Measured |
| P [kPa] - VLE |
x1[mol/mol] of Water (2) - Liquid |
y1[mol/mol] of Water (2) - Vapour |
| 4299.993 |
0.0740 |
0.3710 |
| 5000.002 |
0.1510 |
0.4410 |
| 6000.0 |
0.1830 |
0.5070 |
| 6899.992 |
0.2910 |
0.5180 |
| 7699.993 |
0.3070 |
0.5380 |
| 8400.002 |
0.3630 |
0.5630 |
| 8999.993 |
0.3590 |
0.5530 |
| 9400.001 |
0.4280 |
0.5580 |
Vapor Liquid Equilibrium at Constant Temperature
[ref]
Operational condition: Temperature, K =
593 (VLE)
| Fixed |
Measured |
| P [kPa] - VLE |
x1[mol/mol] of Water (2) - Liquid |
y1[mol/mol] of Water (2) - Vapour |
| 4899.997 |
0.1420 |
0.3590 |
| 5500.001 |
0.2050 |
0.4200 |
| 6399.994 |
0.2650 |
0.4330 |
| 6899.992 |
0.2960 |
0.4550 |
| 7400.005 |
0.3060 |
0.4630 |
Sources
-
Dortmund Data Bank Vapor-Liquid Equilibrium Data
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Tar removal from biosyngas in the biomass gasification process. (Liquid + liquid) equilibrium {water + solvent (paraxylene and methyl hexadecanoate) + model molecules of tar (benzene, toluene, phenol)}
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Measurement and correlation of phase equilibria for (water + aromatic hydrocarbon) binary mixtures at T = (573 to 623) K using microfluidic mixing
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Phase behaviour of aqueous mixtures of acetic acid with isomers of xylene
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Isothermal (liquid + liquid) equilibrium data at T = 313.15 K and isobaric (vapor + liquid + liquid) equilibrium data at 101.3 kPa for the ternary system (water + 1-butanol + p-xylene)
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Liquid Liquid Equilibria of Binary, Ternary, and Quaternary Systems Involving Monoethylene Glycol, Water, Toluene, p-Xylene, Hexane, and Octane
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Liquid-Liquid Equilibria for Binary Mixtures of Water + Benzene, + Toluene, and + p-Xylene from 273 K to 458 K
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Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
