Mixture of Thiophene + Propane, 2-ethoxy-2-methyl-

Datasets

1. Mole fraction (2)
2. P_vap - Vapor or sublimation pressure, kPa (2)

Mole fraction of Thiophene (1) [ref]

Fixed		Measured
Mole fraction of Thiophene (1) - Liquid	Temperature, K - Gas	Mole fraction of Thiophene (1) - Gas
0.0000	333.15	0.0000
0.0000	343.15	0.0000
0.0480	343.15	0.0400
0.0530	333.15	0.0440
0.1140	343.15	0.0960
0.1180	333.15	0.0980
0.1930	343.15	0.1620
0.1970	333.15	0.1630
0.2740	343.15	0.2290
0.2830	333.15	0.2340
0.3450	343.15	0.2890
0.3610	333.15	0.3000
0.4210	343.15	0.3530
0.4420	333.15	0.3680
0.4960	343.15	0.4170
0.5210	333.15	0.4360
0.5630	343.15	0.4770
0.5860	333.15	0.4930
0.5970	343.15	0.5060
0.6440	333.15	0.5450
0.6720	343.15	0.5770
0.6960	333.15	0.5930
0.7440	343.15	0.6480
0.7690	333.15	0.6690
0.8100	343.15	0.7200
0.8340	333.15	0.7440
0.8670	343.15	0.7900
0.8910	333.15	0.8180
0.9120	343.15	0.8530
0.9370	333.15	0.8870
0.9510	343.15	0.9110
0.9740	333.15	0.9500
0.9810	343.15	0.9640
1.0000	333.15	1.0000
1.0000	343.15	1.0000

Mole fraction of Thiophene (1) [ref]

Fixed		Measured
Mole fraction of Thiophene (1) - Liquid	Temperature, K - Gas	Mole fraction of Thiophene (1) - Gas
0.0000	333.15	0.0000
0.0000	343.15	0.0000
0.0480	343.15	0.0400
0.0530	333.15	0.0440
0.1140	343.15	0.0960
0.1180	333.15	0.0980
0.1930	343.15	0.1620
0.1970	333.15	0.1630
0.2740	343.15	0.2290
0.2830	333.15	0.2340
0.3450	343.15	0.2890
0.3610	333.15	0.3000
0.4210	343.15	0.3530
0.4420	333.15	0.3680
0.4960	343.15	0.4170
0.5210	333.15	0.4360
0.5630	343.15	0.4770
0.5860	333.15	0.4930
0.5970	343.15	0.5060
0.6440	333.15	0.5450
0.6720	343.15	0.5770
0.6960	333.15	0.5930
0.7440	343.15	0.6480
0.7690	333.15	0.6690
0.8100	343.15	0.7200
0.8340	333.15	0.7440
0.8670	343.15	0.7900
0.8910	333.15	0.8180
0.9120	343.15	0.8530
0.9370	333.15	0.8870
0.9510	343.15	0.9110
0.9740	333.15	0.9500
0.9810	343.15	0.9640
1.0000	333.15	1.0000
1.0000	343.15	1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Thiophene (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	333.15	66.52
0.0000	343.15	92.96
0.0480	343.15	92.08
0.0530	333.15	65.82
0.1140	343.15	90.97
0.1180	333.15	65.01
0.1930	343.15	89.58
0.1970	333.15	63.95
0.2740	343.15	88.08
0.2830	333.15	62.74
0.3450	343.15	86.58
0.3610	333.15	61.52
0.4210	343.15	84.92
0.4420	333.15	60.21
0.4960	343.15	83.13
0.5210	333.15	58.77
0.5630	343.15	81.42
0.5860	333.15	57.51
0.5970	343.15	80.64
0.6440	333.15	56.29
0.6720	343.15	78.46
0.6960	333.15	55.26
0.7440	343.15	76.07
0.7690	333.15	53.41
0.8100	343.15	73.61
0.8340	333.15	51.59
0.8670	343.15	71.27
0.8910	333.15	49.76
0.9120	343.15	69.22
0.9370	333.15	48.05
0.9510	343.15	67.23
0.9740	333.15	46.53
0.9810	343.15	65.54
1.0000	333.15	45.41
1.0000	343.15	64.45

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Thiophene (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	333.15	66.52
0.0000	343.15	92.96
0.0480	343.15	92.08
0.0530	333.15	65.82
0.1140	343.15	90.97
0.1180	333.15	65.01
0.1930	343.15	89.58
0.1970	333.15	63.95
0.2740	343.15	88.08
0.2830	333.15	62.74
0.3450	343.15	86.58
0.3610	333.15	61.52
0.4210	343.15	84.92
0.4420	333.15	60.21
0.4960	343.15	83.13
0.5210	333.15	58.77
0.5630	343.15	81.42
0.5860	333.15	57.51
0.5970	343.15	80.64
0.6440	333.15	56.29
0.6720	343.15	78.46
0.6960	333.15	55.26
0.7440	343.15	76.07
0.7690	333.15	53.41
0.8100	343.15	73.61
0.8340	333.15	51.59
0.8670	343.15	71.27
0.8910	333.15	49.76
0.9120	343.15	69.22
0.9370	333.15	48.05
0.9510	343.15	67.23
0.9740	333.15	46.53
0.9810	343.15	65.54
1.0000	333.15	45.41
1.0000	343.15	64.45

Sources

• Vapor liquid equilibrium for binary system of thiophene + 2,2,4-trimethylpentane at 343.15 and 353.15K and thiophene + 2-ethoxy-2-methylpropane at 333.15 and 343.15K