Mixture of Ethane, iodo- + Ethanol + Water

Datasets

1. Mole fraction (4)

Mole fraction of Ethanol (2) [ref]

Operational conditions:

• Pressure, kPa = 101.2 (Liquid mixture 1)
• Temperature, K = 298.15 (Liquid mixture 1)

Mole fraction of Ethane, iodo- (1) - Liquid mixture 1	Mole fraction of Ethanol (2) - Liquid mixture 1
0.0120	0.2910
0.0190	0.3110
0.0230	0.3150
0.0310	0.3330
0.0430	0.3600
0.0560	0.3750
0.0740	0.3970
0.1000	0.4170
0.1280	0.4260
0.1660	0.4320
0.1750	0.4320
0.2210	0.4350
0.2680	0.4260
0.3180	0.4110
0.3690	0.3920
0.4820	0.3510
0.5290	0.3250
0.5990	0.2810
0.6890	0.2310
0.8330	0.1480

Mole fraction [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid mixture 1)
• Pressure, kPa = 101.2 (Liquid mixture 1)

Fixed	Measured
Mole fraction of Water (3) - Liquid mixture 1	Mole fraction of Ethanol (2) - Liquid mixture 1	Mole fraction of Water (3) - Liquid mixture 2	Mole fraction of Ethanol (2) - Liquid mixture 2
0.4430	0.4250	0.0690	0.2360
0.5280	0.3930	0.0640	0.1870
0.5820	0.3620	0.0470	0.1620
0.6610	0.3070	0.0230	0.1300
0.7260	0.2570	0.0100	0.0990
0.8170	0.1780	0.0080	0.0730
0.8430	0.1480	0.0070	0.0660
0.9010	0.0960	0.0050	0.0320

Mole fraction of Ethanol (2) [ref]

Operational conditions:

• Pressure, kPa = 101.2 (Liquid mixture 1)
• Temperature, K = 298.15 (Liquid mixture 1)

Mole fraction of Ethane, iodo- (1) - Liquid mixture 1	Mole fraction of Ethanol (2) - Liquid mixture 1
0.0120	0.2910
0.0190	0.3110
0.0230	0.3150
0.0310	0.3330
0.0430	0.3600
0.0560	0.3750
0.0740	0.3970
0.1000	0.4170
0.1280	0.4260
0.1660	0.4320
0.1750	0.4320
0.2210	0.4350
0.2680	0.4260
0.3180	0.4110
0.3690	0.3920
0.4820	0.3510
0.5290	0.3250
0.5990	0.2810
0.6890	0.2310
0.8330	0.1480

Mole fraction [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid mixture 1)
• Pressure, kPa = 101.2 (Liquid mixture 1)

Fixed	Measured
Mole fraction of Water (3) - Liquid mixture 1	Mole fraction of Ethanol (2) - Liquid mixture 1	Mole fraction of Water (3) - Liquid mixture 2	Mole fraction of Ethanol (2) - Liquid mixture 2
0.4430	0.4250	0.0690	0.2360
0.5280	0.3930	0.0640	0.1870
0.5820	0.3620	0.0470	0.1620
0.6610	0.3070	0.0230	0.1300
0.7260	0.2570	0.0100	0.0990
0.8170	0.1780	0.0080	0.0730
0.8430	0.1480	0.0070	0.0660
0.9010	0.0960	0.0050	0.0320

Sources

• Solubility and Liquid-Liquid Equilibrium of Aqueous Systems of Iodoethane with Methanol, Ethanol, or 1-Propanol at Temperature 298.15 K and Pressure 101.2 kPa