Mixture of Butane, 1,4-dichloro- + Ethane, nitro-

Datasets

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

Mole fraction of Ethane, nitro- (2) [ref]

Fixed		Measured
Mole fraction of Ethane, nitro- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethane, nitro- (2) - Gas
0.0000	343.15	0.0000
0.0000	353.15	0.0000
0.0000	363.15	0.0000
0.0499	343.15	0.2474
0.0499	363.15	0.2235
0.0521	353.15	0.2315
0.1113	343.15	0.4219
0.1113	363.15	0.3865
0.1135	353.15	0.3937
0.1746	353.15	0.5260
0.1767	343.15	0.5421
0.1767	363.15	0.5179
0.2572	353.15	0.6241
0.2592	343.15	0.6300
0.2631	363.15	0.6165
0.3410	363.15	0.6983
0.3429	353.15	0.7040
0.3466	343.15	0.7110
0.4184	353.15	0.7577
0.4237	343.15	0.7658
0.4237	363.15	0.7496
0.4950	343.15	0.8119
0.4950	363.15	0.7897
0.4966	353.15	0.8015
0.5783	343.15	0.8451
0.5783	353.15	0.8400
0.5783	363.15	0.8324
0.6595	363.15	0.8650
0.6624	343.15	0.8823
0.6624	353.15	0.8700
0.7414	363.15	0.9017
0.7442	353.15	0.9017
0.7455	343.15	0.9065
0.8170	363.15	0.9291
0.8196	353.15	0.9326
0.8222	343.15	0.9373
0.8859	363.15	0.9582
0.8884	343.15	0.9605
0.8896	353.15	0.9593
0.9361	343.15	0.9798
0.9373	353.15	0.9776
0.9373	363.15	0.9764
1.0000	343.15	1.0000
1.0000	353.15	1.0000
1.0000	363.15	1.0000

Mole fraction of Ethane, nitro- (2) [ref]

Fixed		Measured
Mole fraction of Ethane, nitro- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethane, nitro- (2) - Gas
0.0000	343.15	0.0000
0.0000	353.15	0.0000
0.0000	363.15	0.0000
0.0499	343.15	0.2474
0.0499	363.15	0.2235
0.0521	353.15	0.2315
0.1113	343.15	0.4219
0.1113	363.15	0.3865
0.1135	353.15	0.3937
0.1746	353.15	0.5260
0.1767	343.15	0.5421
0.1767	363.15	0.5179
0.2572	353.15	0.6241
0.2592	343.15	0.6300
0.2631	363.15	0.6165
0.3410	363.15	0.6983
0.3429	353.15	0.7040
0.3466	343.15	0.7110
0.4184	353.15	0.7577
0.4237	343.15	0.7658
0.4237	363.15	0.7496
0.4950	343.15	0.8119
0.4950	363.15	0.7897
0.4966	353.15	0.8015
0.5783	343.15	0.8451
0.5783	353.15	0.8400
0.5783	363.15	0.8324
0.6595	363.15	0.8650
0.6624	343.15	0.8823
0.6624	353.15	0.8700
0.7414	363.15	0.9017
0.7442	353.15	0.9017
0.7455	343.15	0.9065
0.8170	363.15	0.9291
0.8196	353.15	0.9326
0.8222	343.15	0.9373
0.8859	363.15	0.9582
0.8884	343.15	0.9605
0.8896	353.15	0.9593
0.9361	343.15	0.9798
0.9373	353.15	0.9776
0.9373	363.15	0.9764
1.0000	343.15	1.0000
1.0000	353.15	1.0000
1.0000	363.15	1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethane, nitro- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	343.15	5.25
0.0000	353.15	8.20
0.0000	363.15	12.52
0.0499	343.15	6.79
0.0499	363.15	15.15
0.0521	353.15	10.21
0.1113	343.15	8.29
0.1113	363.15	18.16
0.1135	353.15	12.37
0.1746	353.15	14.44
0.1767	343.15	9.71
0.1767	363.15	21.05
0.2572	353.15	16.79
0.2592	343.15	11.31
0.2631	363.15	24.28
0.3410	363.15	27.64
0.3429	353.15	19.00
0.3466	343.15	12.96
0.4184	353.15	20.84
0.4237	343.15	14.25
0.4237	363.15	30.14
0.4950	343.15	15.37
0.4950	363.15	32.52
0.4966	353.15	22.46
0.5783	343.15	16.45
0.5783	353.15	24.32
0.5783	363.15	35.06
0.6595	363.15	37.40
0.6624	343.15	17.76
0.6624	353.15	25.96
0.7414	363.15	39.81
0.7442	353.15	27.62
0.7455	343.15	18.87
0.8170	363.15	42.01
0.8196	353.15	29.14
0.8222	343.15	19.97
0.8859	363.15	43.98
0.8884	343.15	20.85
0.8896	353.15	30.53
0.9361	343.15	21.37
0.9373	353.15	31.49
0.9373	363.15	45.34
1.0000	343.15	22.46
1.0000	353.15	32.84
1.0000	363.15	47.13

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethane, nitro- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	343.15	5.25
0.0000	353.15	8.20
0.0000	363.15	12.52
0.0499	343.15	6.79
0.0499	363.15	15.15
0.0521	353.15	10.21
0.1113	343.15	8.29
0.1113	363.15	18.16
0.1135	353.15	12.37
0.1746	353.15	14.44
0.1767	343.15	9.71
0.1767	363.15	21.05
0.2572	353.15	16.79
0.2592	343.15	11.31
0.2631	363.15	24.28
0.3410	363.15	27.64
0.3429	353.15	19.00
0.3466	343.15	12.96
0.4184	353.15	20.84
0.4237	343.15	14.25
0.4237	363.15	30.14
0.4950	343.15	15.37
0.4950	363.15	32.52
0.4966	353.15	22.46
0.5783	343.15	16.45
0.5783	353.15	24.32
0.5783	363.15	35.06
0.6595	363.15	37.40
0.6624	343.15	17.76
0.6624	353.15	25.96
0.7414	363.15	39.81
0.7442	353.15	27.62
0.7455	343.15	18.87
0.8170	363.15	42.01
0.8196	353.15	29.14
0.8222	343.15	19.97
0.8859	363.15	43.98
0.8884	343.15	20.85
0.8896	353.15	30.53
0.9361	343.15	21.37
0.9373	353.15	31.49
0.9373	363.15	45.34
1.0000	343.15	22.46
1.0000	353.15	32.84
1.0000	363.15	47.13

Sources

• Isothermal (vapour + liquid) equilibria for (nitromethane or nitroethane + 1,4-dichlorobutane) binary systems at temperatures between (343.15 and 363.15) K