Datasets
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Activity coefficient (2)
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Mole fraction (6)
Activity coefficient of 1,2-Ethanediol (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Temperature, K - Liquid |
Activity coefficient of 1,2-Ethanediol (2) - Liquid |
323.15 |
30.23 |
343.15 |
26.44 |
363.15 |
23.34 |
383.15 |
21.14 |
Activity coefficient of 1,2-Ethanediol (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Temperature, K - Liquid |
Activity coefficient of 1,2-Ethanediol (2) - Liquid |
323.15 |
30.23 |
343.15 |
26.44 |
363.15 |
23.34 |
383.15 |
21.14 |
Mole fraction of Benzene (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Benzene (1) - Liquid mixture 1 |
298.20 |
101.00 |
0.0340 |
Mole fraction of Benzene (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Benzene (1) - Liquid mixture 1 |
279.20 |
0.0466 |
288.50 |
0.0488 |
303.30 |
0.0500 |
318.10 |
0.0510 |
332.60 |
0.0553 |
342.10 |
0.0557 |
Mole fraction of 1,2-Ethanediol (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 2 |
Mole fraction of 1,2-Ethanediol (2) - Liquid mixture 2 |
279.20 |
0.0011 |
288.50 |
0.0015 |
303.30 |
0.0030 |
318.10 |
0.0046 |
332.60 |
0.0075 |
342.10 |
0.0098 |
Mole fraction of Benzene (1)
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of Benzene (1) - Liquid mixture 1 |
298.20 |
101.00 |
0.0340 |
Mole fraction of Benzene (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Benzene (1) - Liquid mixture 1 |
279.20 |
0.0466 |
288.50 |
0.0488 |
303.30 |
0.0500 |
318.10 |
0.0510 |
332.60 |
0.0553 |
342.10 |
0.0557 |
Mole fraction of 1,2-Ethanediol (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 2 |
Mole fraction of 1,2-Ethanediol (2) - Liquid mixture 2 |
279.20 |
0.0011 |
288.50 |
0.0015 |
303.30 |
0.0030 |
318.10 |
0.0046 |
332.60 |
0.0075 |
342.10 |
0.0098 |
Sources