Mixture of Thiophene + Heptane + Ethanol, 2,2'-oxybis-

Datasets

1. Mole fraction (2)

Mole fraction [ref]

Operational conditions:

• Temperature, K = 308.15 (Liquid mixture 2)
• Pressure, kPa = 101 (Liquid mixture 2)

Fixed	Measured
Mole fraction of Thiophene (1) - Liquid mixture 2	Mole fraction of Heptane (2) - Liquid mixture 2	Mole fraction of Heptane (2) - Liquid mixture 1	Mole fraction of Thiophene (1) - Liquid mixture 1
0.0000	0.0080	1.0000	0.0000
0.0540	0.0090	0.8880	0.1100
0.1000	0.0090	0.7710	0.2280
0.1650	0.0120	0.6630	0.3360
0.2100	0.0130	0.5810	0.4180
0.2540	0.0140	0.4960	0.5020
0.2860	0.0160	0.3810	0.6130
0.3380	0.0190	0.3380	0.6550
0.3490	0.0180	0.2890	0.6990
0.3780	0.0200	0.2530	0.7330
0.4040	0.0220	0.2180	0.7660
0.6530	0.0350	0.0600	0.7690
0.6290	0.0370	0.0720	0.7940
0.4150	0.0220	0.1720	0.7980
0.4660	0.0240	0.1430	0.8170
0.6150	0.0350	0.0790	0.8180
0.5940	0.0320	0.0820	0.8220
0.5700	0.0310	0.0930	0.8250
0.5040	0.0260	0.1200	0.8310

Mole fraction [ref]

Operational conditions:

• Temperature, K = 308.15 (Liquid mixture 2)
• Pressure, kPa = 101 (Liquid mixture 2)

Fixed	Measured
Mole fraction of Thiophene (1) - Liquid mixture 2	Mole fraction of Heptane (2) - Liquid mixture 2	Mole fraction of Heptane (2) - Liquid mixture 1	Mole fraction of Thiophene (1) - Liquid mixture 1
0.0000	0.0080	1.0000	0.0000
0.0540	0.0090	0.8880	0.1100
0.1000	0.0090	0.7710	0.2280
0.1650	0.0120	0.6630	0.3360
0.2100	0.0130	0.5810	0.4180
0.2540	0.0140	0.4960	0.5020
0.2860	0.0160	0.3810	0.6130
0.3380	0.0190	0.3380	0.6550
0.3490	0.0180	0.2890	0.6990
0.3780	0.0200	0.2530	0.7330
0.4040	0.0220	0.2180	0.7660
0.6530	0.0350	0.0600	0.7690
0.6290	0.0370	0.0720	0.7940
0.4150	0.0220	0.1720	0.7980
0.4660	0.0240	0.1430	0.8170
0.6150	0.0350	0.0790	0.8180
0.5940	0.0320	0.0820	0.8220
0.5700	0.0310	0.0930	0.8250
0.5040	0.0260	0.1200	0.8310

Sources

• Separation of thiophene, or benzothiophene from model fuel using glycols. Liquid-liquid phase equilibria and oxidative desulfurization study