Mixture of Butane, 1,4-dichloro- + Cyclopentanone

Datasets

1. P_vap - Vapor or sublimation pressure, kPa (2)
2. ρ_l - Mass density, kg/m3 (2)

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 1,4-dichloro- (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
298.15	0.0000	1.71
298.15	0.0588	1.64
298.15	0.1300	1.62
298.15	0.2039	1.57
298.15	0.2858	1.48
298.15	0.3353	1.41
298.15	0.4072	1.33
298.15	0.4825	1.26
298.15	0.5472	1.20
298.15	0.6130	1.22
298.15	0.6877	1.17
298.15	0.7794	1.11
298.15	0.8338	1.07
298.15	0.8789	1.06
298.15	0.9078	1.03
298.15	0.9429	1.01
298.15	1.0000	0.99
308.15	0.0000	2.80
308.15	0.0588	2.76
308.15	0.1300	2.61
308.15	0.2039	2.56
308.15	0.2858	2.42
308.15	0.3353	2.32
308.15	0.4072	2.21
308.15	0.4825	2.11
308.15	0.5472	2.00
308.15	0.6130	1.93
308.15	0.6877	1.83
308.15	0.7794	1.73
308.15	0.8338	1.63
308.15	0.8789	1.62
308.15	0.9078	1.54
308.15	0.9429	1.51
308.15	1.0000	1.39
318.15	0.0000	4.40
318.15	0.0588	4.34
318.15	0.1300	4.13
318.15	0.2039	3.90
318.15	0.2858	3.78
318.15	0.3353	3.71
318.15	0.4072	3.52
318.15	0.4825	3.32
318.15	0.5472	3.17
318.15	0.6130	3.04
318.15	0.6877	2.87
318.15	0.7794	2.61
318.15	0.8338	2.54
318.15	0.8789	2.48
318.15	0.9078	2.37
318.15	0.9429	2.34
318.15	1.0000	2.13

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 1,4-dichloro- (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
298.15	0.0000	1.71
298.15	0.0588	1.64
298.15	0.1300	1.62
298.15	0.2039	1.57
298.15	0.2858	1.48
298.15	0.3353	1.41
298.15	0.4072	1.33
298.15	0.4825	1.26
298.15	0.5472	1.20
298.15	0.6130	1.22
298.15	0.6877	1.17
298.15	0.7794	1.11
298.15	0.8338	1.07
298.15	0.8789	1.06
298.15	0.9078	1.03
298.15	0.9429	1.01
298.15	1.0000	0.99
308.15	0.0000	2.80
308.15	0.0588	2.76
308.15	0.1300	2.61
308.15	0.2039	2.56
308.15	0.2858	2.42
308.15	0.3353	2.32
308.15	0.4072	2.21
308.15	0.4825	2.11
308.15	0.5472	2.00
308.15	0.6130	1.93
308.15	0.6877	1.83
308.15	0.7794	1.73
308.15	0.8338	1.63
308.15	0.8789	1.62
308.15	0.9078	1.54
308.15	0.9429	1.51
308.15	1.0000	1.39
318.15	0.0000	4.40
318.15	0.0588	4.34
318.15	0.1300	4.13
318.15	0.2039	3.90
318.15	0.2858	3.78
318.15	0.3353	3.71
318.15	0.4072	3.52
318.15	0.4825	3.32
318.15	0.5472	3.17
318.15	0.6130	3.04
318.15	0.6877	2.87
318.15	0.7794	2.61
318.15	0.8338	2.54
318.15	0.8789	2.48
318.15	0.9078	2.37
318.15	0.9429	2.34
318.15	1.0000	2.13

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 1,4-dichloro- (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	953.99
288.15	0.1103	979.25
288.15	0.2151	1002.02
288.15	0.3024	1020.17
288.15	0.3909	1037.87
288.15	0.4900	1056.87
288.15	0.5868	1074.68
288.15	0.6976	1094.22
288.15	0.8036	1112.13
288.15	0.9190	1130.8
288.15	1.0000	1143.43
298.15	0.0000	944.35
298.15	0.1103	969.45
298.15	0.2151	992.09
298.15	0.3024	1010.12
298.15	0.3909	1027.7
298.15	0.4900	1046.56
298.15	0.5868	1064.25
298.15	0.6976	1083.64
298.15	0.8036	1101.43
298.15	0.9190	1119.97
298.15	1.0000	1132.5
308.15	0.0000	934.69
308.15	0.1103	959.63
308.15	0.2151	982.11
308.15	0.3024	1000.02
308.15	0.3909	1017.48
308.15	0.4900	1036.22
308.15	0.5868	1053.78
308.15	0.6976	1073.04
308.15	0.8036	1090.7
308.15	0.9190	1109.1
308.15	1.0000	1121.54
318.15	0.0000	924.99
318.15	0.1103	949.76
318.15	0.2151	972.09
318.15	0.3024	989.87
318.15	0.3909	1007.21
318.15	0.4900	1025.82
318.15	0.5868	1043.26
318.15	0.6976	1062.39
318.15	0.8036	1079.93
318.15	0.9190	1098.19
318.15	1.0000	1110.54

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 1,4-dichloro- (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	953.99
288.15	0.1103	979.25
288.15	0.2151	1002.02
288.15	0.3024	1020.17
288.15	0.3909	1037.87
288.15	0.4900	1056.87
288.15	0.5868	1074.68
288.15	0.6976	1094.22
288.15	0.8036	1112.13
288.15	0.9190	1130.8
288.15	1.0000	1143.43
298.15	0.0000	944.35
298.15	0.1103	969.45
298.15	0.2151	992.09
298.15	0.3024	1010.12
298.15	0.3909	1027.7
298.15	0.4900	1046.56
298.15	0.5868	1064.25
298.15	0.6976	1083.64
298.15	0.8036	1101.43
298.15	0.9190	1119.97
298.15	1.0000	1132.5
308.15	0.0000	934.69
308.15	0.1103	959.63
308.15	0.2151	982.11
308.15	0.3024	1000.02
308.15	0.3909	1017.48
308.15	0.4900	1036.22
308.15	0.5868	1053.78
308.15	0.6976	1073.04
308.15	0.8036	1090.7
308.15	0.9190	1109.1
308.15	1.0000	1121.54
318.15	0.0000	924.99
318.15	0.1103	949.76
318.15	0.2151	972.09
318.15	0.3024	989.87
318.15	0.3909	1007.21
318.15	0.4900	1025.82
318.15	0.5868	1043.26
318.15	0.6976	1062.39
318.15	0.8036	1079.93
318.15	0.9190	1098.19
318.15	1.0000	1110.54

Sources

• Isothermal (vapour + liquid) equilibria and excess Gibbs free energies in some binary (cyclopentanone + chloroalkane) mixtures at temperatures from 298.15 K to 318.15 K
• Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K