Mixture of Butane, 1-chloro- + Ethane, nitro-

Datasets

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

Mole fraction of Butane, 1-chloro- (1) [ref]

Fixed		Measured
Mole fraction of Butane, 1-chloro- (1) - Liquid	Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (1) - Gas
0.0000	298.15	0.0000
0.0510	298.15	0.3516
0.1346	298.15	0.5685
0.2264	298.15	0.6796
0.2715	298.15	0.7164
0.3237	298.15	0.7510
0.4136	298.15	0.7979
0.5181	298.15	0.8390
0.6247	298.15	0.8715
0.6988	298.15	0.8908
0.7767	298.15	0.9101
0.8488	298.15	0.9297
0.9254	298.15	0.9570
1.0000	298.15	1.0000
0.0000	308.15	0.0000
0.0510	308.15	0.3663
0.1346	308.15	0.5766
0.2264	308.15	0.6802
0.2715	308.15	0.7141
0.3237	308.15	0.7460
0.4136	308.15	0.7896
0.5181	308.15	0.8285
0.6247	308.15	0.8601
0.6988	308.15	0.8794
0.7767	308.15	0.8994
0.8488	308.15	0.9203
0.9254	308.15	0.9506
1.0000	308.15	1.0000
0.0000	318.15	0.0000
0.0510	318.15	0.3614
0.1346	318.15	0.5748
0.2264	318.15	0.6774
0.2715	318.15	0.7099
0.3237	318.15	0.7399
0.4136	318.15	0.7803
0.5181	318.15	0.8172
0.6247	318.15	0.8498
0.6988	318.15	0.8718
0.7767	318.15	0.8961
0.8488	318.15	0.9216
0.9254	318.15	0.9552
1.0000	318.15	1.0000

Mole fraction of Butane, 1-chloro- (1) [ref]

Fixed		Measured
Mole fraction of Butane, 1-chloro- (1) - Liquid	Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (1) - Gas
0.0000	298.15	0.0000
0.0510	298.15	0.3516
0.1346	298.15	0.5685
0.2264	298.15	0.6796
0.2715	298.15	0.7164
0.3237	298.15	0.7510
0.4136	298.15	0.7979
0.5181	298.15	0.8390
0.6247	298.15	0.8715
0.6988	298.15	0.8908
0.7767	298.15	0.9101
0.8488	298.15	0.9297
0.9254	298.15	0.9570
1.0000	298.15	1.0000
0.0000	308.15	0.0000
0.0510	308.15	0.3663
0.1346	308.15	0.5766
0.2264	308.15	0.6802
0.2715	308.15	0.7141
0.3237	308.15	0.7460
0.4136	308.15	0.7896
0.5181	308.15	0.8285
0.6247	308.15	0.8601
0.6988	308.15	0.8794
0.7767	308.15	0.8994
0.8488	308.15	0.9203
0.9254	308.15	0.9506
1.0000	308.15	1.0000
0.0000	318.15	0.0000
0.0510	318.15	0.3614
0.1346	318.15	0.5748
0.2264	318.15	0.6774
0.2715	318.15	0.7099
0.3237	318.15	0.7399
0.4136	318.15	0.7803
0.5181	318.15	0.8172
0.6247	318.15	0.8498
0.6988	318.15	0.8718
0.7767	318.15	0.8961
0.8488	318.15	0.9216
0.9254	318.15	0.9552
1.0000	318.15	1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Butane, 1-chloro- (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	298.15	2.95
0.0510	298.15	4.52
0.1346	298.15	5.99
0.2264	298.15	7.33
0.2715	298.15	8.10
0.3237	298.15	9.09
0.4136	298.15	9.88
0.5181	298.15	10.83
0.6247	298.15	11.75
0.6988	298.15	12.17
0.7767	298.15	12.68
0.8488	298.15	13.06
0.9254	298.15	13.59
1.0000	298.15	13.72
0.0000	308.15	4.69
0.0510	308.15	6.99
0.1346	308.15	9.92
0.2264	308.15	12.08
0.2715	308.15	13.00
0.3237	308.15	14.33
0.4136	308.15	15.47
0.5181	308.15	16.79
0.6247	308.15	17.88
0.6988	308.15	19.00
0.7767	308.15	19.41
0.8488	308.15	20.02
0.9254	308.15	20.54
1.0000	308.15	20.66
0.0000	318.15	7.24
0.0510	318.15	11.00
0.1346	318.15	15.10
0.2264	318.15	18.79
0.2715	318.15	19.73
0.3237	318.15	21.50
0.4136	318.15	23.41
0.5181	318.15	25.25
0.6247	318.15	26.94
0.6988	318.15	27.91
0.7767	318.15	28.88
0.8488	318.15	29.83
0.9254	318.15	30.73
1.0000	318.15	31.46

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Butane, 1-chloro- (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	298.15	2.95
0.0510	298.15	4.52
0.1346	298.15	5.99
0.2264	298.15	7.33
0.2715	298.15	8.10
0.3237	298.15	9.09
0.4136	298.15	9.88
0.5181	298.15	10.83
0.6247	298.15	11.75
0.6988	298.15	12.17
0.7767	298.15	12.68
0.8488	298.15	13.06
0.9254	298.15	13.59
1.0000	298.15	13.72
0.0000	308.15	4.69
0.0510	308.15	6.99
0.1346	308.15	9.92
0.2264	308.15	12.08
0.2715	308.15	13.00
0.3237	308.15	14.33
0.4136	308.15	15.47
0.5181	308.15	16.79
0.6247	308.15	17.88
0.6988	308.15	19.00
0.7767	308.15	19.41
0.8488	308.15	20.02
0.9254	308.15	20.54
1.0000	308.15	20.66
0.0000	318.15	7.24
0.0510	318.15	11.00
0.1346	318.15	15.10
0.2264	318.15	18.79
0.2715	318.15	19.73
0.3237	318.15	21.50
0.4136	318.15	23.41
0.5181	318.15	25.25
0.6247	318.15	26.94
0.6988	318.15	27.91
0.7767	318.15	28.88
0.8488	318.15	29.83
0.9254	318.15	30.73
1.0000	318.15	31.46

Sources

• Isothermal vapor liquid equilibria and excess Gibbs free energies in some binary nitroalkane + chloroalkane mixtures at temperatures from 298.15 K to 318.15 K