Datasets
-
Mole fraction (6)
-
Pvap - Vapor or sublimation pressure, kPa (4)
Mole fraction of Ethane (2)
[ref]
Operational condition: Solvent: Amount concentration (molarity), mol/dm3 =
3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethane (2) - Liquid |
298.15 |
92.00 |
0.0001 |
298.15 |
507.00 |
0.0002 |
298.15 |
1510.00 |
0.0007 |
298.15 |
2530.00 |
0.0011 |
298.15 |
4218.00 |
0.0014 |
323.15 |
244.00 |
0.0001 |
323.15 |
783.00 |
0.0003 |
323.15 |
2560.00 |
0.0007 |
323.15 |
4070.00 |
0.0010 |
323.15 |
6210.00 |
0.0013 |
323.15 |
8420.00 |
0.0013 |
323.15 |
10610.00 |
0.0014 |
323.15 |
12140.00 |
0.0014 |
348.15 |
248.00 |
0.0001 |
348.15 |
812.00 |
0.0002 |
348.15 |
2530.00 |
0.0007 |
348.15 |
4190.00 |
0.0009 |
348.15 |
6170.00 |
0.0013 |
348.15 |
8610.00 |
0.0014 |
348.15 |
10120.00 |
0.0015 |
348.15 |
13200.00 |
0.0016 |
373.15 |
200.00 |
0.0001 |
373.15 |
896.00 |
0.0003 |
373.15 |
2440.00 |
0.0006 |
373.15 |
4060.00 |
0.0010 |
373.15 |
6790.00 |
0.0014 |
373.15 |
10510.00 |
0.0018 |
373.15 |
12780.00 |
0.0019 |
398.15 |
279.00 |
0.0001 |
398.15 |
1010.00 |
0.0003 |
398.15 |
2980.00 |
0.0008 |
398.15 |
4240.00 |
0.0011 |
398.15 |
7460.00 |
0.0017 |
398.15 |
9570.00 |
0.0020 |
398.15 |
12110.00 |
0.0023 |
Mole fraction of Ethane (2)
[ref]
Operational conditions:
- Solvent: Mass fraction = 0.35 (Liquid)
- Temperature, K = 283.15 (Liquid)
Pressure, kPa - Liquid |
Mole fraction of Ethane (2) - Liquid |
1.24 |
0.0004 |
1.32 |
0.0007 |
1.54 |
0.0011 |
1.99 |
0.0013 |
2.50 |
0.0015 |
2.94 |
0.0016 |
Mole fraction of Ethane (2)
[ref]
Operational condition: Solvent: Mass fraction =
0.35 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Ethane (2) - Liquid mixture 1 |
283.15 |
0.0016 |
288.15 |
0.0016 |
293.15 |
0.0015 |
298.15 |
0.0015 |
303.15 |
0.0015 |
305.15 |
0.0014 |
Mole fraction of Ethane (2)
[ref]
Operational condition: Solvent: Amount concentration (molarity), mol/dm3 =
3 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethane (2) - Liquid |
298.15 |
92.00 |
0.0001 |
298.15 |
507.00 |
0.0002 |
298.15 |
1510.00 |
0.0007 |
298.15 |
2530.00 |
0.0011 |
298.15 |
4218.00 |
0.0014 |
323.15 |
244.00 |
0.0001 |
323.15 |
783.00 |
0.0003 |
323.15 |
2560.00 |
0.0007 |
323.15 |
4070.00 |
0.0010 |
323.15 |
6210.00 |
0.0013 |
323.15 |
8420.00 |
0.0013 |
323.15 |
10610.00 |
0.0014 |
323.15 |
12140.00 |
0.0014 |
348.15 |
248.00 |
0.0001 |
348.15 |
812.00 |
0.0002 |
348.15 |
2530.00 |
0.0007 |
348.15 |
4190.00 |
0.0009 |
348.15 |
6170.00 |
0.0013 |
348.15 |
8610.00 |
0.0014 |
348.15 |
10120.00 |
0.0015 |
348.15 |
13200.00 |
0.0016 |
373.15 |
200.00 |
0.0001 |
373.15 |
896.00 |
0.0003 |
373.15 |
2440.00 |
0.0006 |
373.15 |
4060.00 |
0.0010 |
373.15 |
6790.00 |
0.0014 |
373.15 |
10510.00 |
0.0018 |
373.15 |
12780.00 |
0.0019 |
398.15 |
279.00 |
0.0001 |
398.15 |
1010.00 |
0.0003 |
398.15 |
2980.00 |
0.0008 |
398.15 |
4240.00 |
0.0011 |
398.15 |
7460.00 |
0.0017 |
398.15 |
9570.00 |
0.0020 |
398.15 |
12110.00 |
0.0023 |
Mole fraction of Ethane (2)
[ref]
Operational conditions:
- Solvent: Mass fraction = 0.35 (Liquid)
- Temperature, K = 283.15 (Liquid)
Pressure, kPa - Liquid |
Mole fraction of Ethane (2) - Liquid |
1.24 |
0.0004 |
1.32 |
0.0007 |
1.54 |
0.0011 |
1.99 |
0.0013 |
2.50 |
0.0015 |
2.94 |
0.0016 |
Mole fraction of Ethane (2)
[ref]
Operational condition: Solvent: Mass fraction =
0.35 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Ethane (2) - Liquid mixture 1 |
283.15 |
0.0016 |
288.15 |
0.0016 |
293.15 |
0.0015 |
298.15 |
0.0015 |
303.15 |
0.0015 |
305.15 |
0.0014 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Solvent: Mass fraction =
0.35 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
283.15 |
3023.00 |
288.15 |
3381.00 |
293.15 |
3770.00 |
298.15 |
4195.00 |
303.15 |
4662.00 |
305.15 |
4891.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Solvent: Mass fraction of Diethanolamine (1) - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
283.15 |
0.2500 |
3021.00 |
288.15 |
0.2500 |
3377.00 |
293.15 |
0.2500 |
3767.00 |
298.15 |
0.2500 |
4191.00 |
303.15 |
0.2500 |
4712.00 |
305.15 |
0.2500 |
5036.00 |
283.15 |
0.5000 |
3017.00 |
288.15 |
0.5000 |
3377.00 |
293.15 |
0.5000 |
3766.00 |
298.15 |
0.5000 |
4191.00 |
283.15 |
0.3500 |
3023.00 |
288.15 |
0.3500 |
3381.00 |
293.15 |
0.3500 |
3770.00 |
298.15 |
0.3500 |
4195.00 |
303.15 |
0.3500 |
4662.00 |
305.15 |
0.3500 |
4891.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Solvent: Mass fraction =
0.35 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
283.15 |
3023.00 |
288.15 |
3381.00 |
293.15 |
3770.00 |
298.15 |
4195.00 |
303.15 |
4662.00 |
305.15 |
4891.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Solvent: Mass fraction of Diethanolamine (1) - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Liquid mixture 1 |
283.15 |
0.2500 |
3021.00 |
288.15 |
0.2500 |
3377.00 |
293.15 |
0.2500 |
3767.00 |
298.15 |
0.2500 |
4191.00 |
303.15 |
0.2500 |
4712.00 |
305.15 |
0.2500 |
5036.00 |
283.15 |
0.5000 |
3017.00 |
288.15 |
0.5000 |
3377.00 |
293.15 |
0.5000 |
3766.00 |
298.15 |
0.5000 |
4191.00 |
283.15 |
0.3500 |
3023.00 |
288.15 |
0.3500 |
3381.00 |
293.15 |
0.3500 |
3770.00 |
298.15 |
0.3500 |
4195.00 |
303.15 |
0.3500 |
4662.00 |
305.15 |
0.3500 |
4891.00 |
Sources