Mixture of Ethane, 1,2-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
Mole fraction of Ethane, 1,2-dichloro- (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	298.15	1.61
0.0000	303.15	2.03
0.0000	308.15	2.68
0.0000	313.15	3.41
0.0421	298.15	1.71
0.0421	303.15	2.39
0.0421	308.15	2.99
0.0421	313.15	3.87
0.1259	298.15	2.14
0.1259	303.15	2.84
0.1259	308.15	3.76
0.1259	313.15	4.71
0.2243	298.15	2.93
0.2243	303.15	3.58
0.2243	308.15	4.49
0.2243	313.15	6.14
0.3021	298.15	3.61
0.3021	303.15	4.51
0.3021	308.15	5.61
0.3021	313.15	7.15
0.4378	298.15	4.53
0.4378	303.15	6.00
0.4378	308.15	7.47
0.4378	313.15	9.33
0.5220	298.15	5.47
0.5220	303.15	7.02
0.5220	308.15	8.89
0.5220	313.15	11.04
0.6141	298.15	6.52
0.6141	303.15	8.27
0.6141	308.15	10.35
0.6141	313.15	12.89
0.7075	298.15	7.41
0.7075	303.15	9.48
0.7075	308.15	11.88
0.7075	313.15	14.93
0.8318	298.15	9.00
0.8318	303.15	11.32
0.8318	308.15	14.04
0.8318	313.15	17.45
0.9340	298.15	9.99
0.9340	303.15	12.66
0.9340	308.15	15.73
0.9340	313.15	19.87
1.0000	298.15	10.47
1.0000	303.15	13.34
1.0000	308.15	16.77
1.0000	313.15	20.88

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethane, 1,2-dichloro- (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	298.15	1.61
0.0000	303.15	2.03
0.0000	308.15	2.68
0.0000	313.15	3.41
0.0421	298.15	1.71
0.0421	303.15	2.39
0.0421	308.15	2.99
0.0421	313.15	3.87
0.1259	298.15	2.14
0.1259	303.15	2.84
0.1259	308.15	3.76
0.1259	313.15	4.71
0.2243	298.15	2.93
0.2243	303.15	3.58
0.2243	308.15	4.49
0.2243	313.15	6.14
0.3021	298.15	3.61
0.3021	303.15	4.51
0.3021	308.15	5.61
0.3021	313.15	7.15
0.4378	298.15	4.53
0.4378	303.15	6.00
0.4378	308.15	7.47
0.4378	313.15	9.33
0.5220	298.15	5.47
0.5220	303.15	7.02
0.5220	308.15	8.89
0.5220	313.15	11.04
0.6141	298.15	6.52
0.6141	303.15	8.27
0.6141	308.15	10.35
0.6141	313.15	12.89
0.7075	298.15	7.41
0.7075	303.15	9.48
0.7075	308.15	11.88
0.7075	313.15	14.93
0.8318	298.15	9.00
0.8318	303.15	11.32
0.8318	308.15	14.04
0.8318	313.15	17.45
0.9340	298.15	9.99
0.9340	303.15	12.66
0.9340	308.15	15.73
0.9340	313.15	19.87
1.0000	298.15	10.47
1.0000	303.15	13.34
1.0000	308.15	16.77
1.0000	313.15	20.88

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,2-dichloro- (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	953.99
288.15	0.1186	986.57
288.15	0.1945	1007.9
288.15	0.3015	1038.6
288.15	0.4044	1068.85
288.15	0.5004	1097.68
288.15	0.6009	1128.64
288.15	0.6915	1157.24
288.15	0.7932	1190.15
288.15	0.8997	1225.7
288.15	1.0000	1260.33
298.15	0.0000	944.35
298.15	0.1186	976.53
298.15	0.1945	997.59
298.15	0.3015	1027.87
298.15	0.4044	1057.69
298.15	0.5004	1086.09
298.15	0.6009	1116.55
298.15	0.6915	1144.68
298.15	0.7932	1177.01
298.15	0.8997	1211.87
298.15	1.0000	1245.8
308.15	0.0000	934.69
308.15	0.1186	966.45
308.15	0.1945	987.23
308.15	0.3015	1017.08
308.15	0.4044	1046.46
308.15	0.5004	1074.43
308.15	0.6009	1104.39
308.15	0.6915	1132.02
308.15	0.7932	1163.76
308.15	0.8997	1197.94
308.15	1.0000	1231.15
318.15	0.0000	924.99
318.15	0.1186	956.32
318.15	0.1945	976.81
318.15	0.3015	1006.23
318.15	0.4044	1035.16
318.15	0.5004	1062.67
318.15	0.6009	1092.12
318.15	0.6915	1119.26
318.15	0.7932	1150.4
318.15	0.8997	1183.89
318.15	1.0000	1216.35

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,2-dichloro- (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	953.99
288.15	0.1186	986.57
288.15	0.1945	1007.9
288.15	0.3015	1038.6
288.15	0.4044	1068.85
288.15	0.5004	1097.68
288.15	0.6009	1128.64
288.15	0.6915	1157.24
288.15	0.7932	1190.15
288.15	0.8997	1225.7
288.15	1.0000	1260.33
298.15	0.0000	944.35
298.15	0.1186	976.53
298.15	0.1945	997.59
298.15	0.3015	1027.87
298.15	0.4044	1057.69
298.15	0.5004	1086.09
298.15	0.6009	1116.55
298.15	0.6915	1144.68
298.15	0.7932	1177.01
298.15	0.8997	1211.87
298.15	1.0000	1245.8
308.15	0.0000	934.69
308.15	0.1186	966.45
308.15	0.1945	987.23
308.15	0.3015	1017.08
308.15	0.4044	1046.46
308.15	0.5004	1074.43
308.15	0.6009	1104.39
308.15	0.6915	1132.02
308.15	0.7932	1163.76
308.15	0.8997	1197.94
308.15	1.0000	1231.15
318.15	0.0000	924.99
318.15	0.1186	956.32
318.15	0.1945	976.81
318.15	0.3015	1006.23
318.15	0.4044	1035.16
318.15	0.5004	1062.67
318.15	0.6009	1092.12
318.15	0.6915	1119.26
318.15	0.7932	1150.4
318.15	0.8997	1183.89
318.15	1.0000	1216.35

Sources

• Isothermal (vapour + liquid) equilibria in the binary mixtures (1,2-dichloroethane and 1,1,1-trichloroethane with cyclopentanone) within the temperature range (298.15 to 313.15) 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