Mixture of Butane, 1-chloro- + 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-chloro- (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
298.15	0.0000	1.71
298.15	0.0860	3.26
298.15	0.1740	4.42
298.15	0.2483	5.39
298.15	0.3464	6.50
298.15	0.4148	7.39
298.15	0.5001	8.34
298.15	0.5774	9.17
298.15	0.6604	10.18
298.15	0.7375	11.13
298.15	0.8143	12.00
298.15	0.9084	12.95
298.15	1.0000	13.70
308.15	0.0000	2.80
308.15	0.0860	5.03
308.15	0.1740	6.91
308.15	0.2483	8.31
308.15	0.3464	10.14
308.15	0.4148	11.44
308.15	0.5001	12.92
308.15	0.5774	14.16
308.15	0.6604	15.68
308.15	0.7375	17.05
308.15	0.8143	18.47
308.15	0.9084	19.93
308.15	1.0000	21.32
318.15	0.0000	4.40
318.15	0.0860	7.75
318.15	0.1740	10.72
318.15	0.2483	12.67
318.15	0.3464	15.24
318.15	0.4148	17.19
318.15	0.5001	19.57
318.15	0.5774	21.44
318.15	0.6604	23.49
318.15	0.7375	25.34
318.15	0.8143	27.58
318.15	0.9084	29.80
318.15	1.0000	31.86

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
298.15	0.0000	1.71
298.15	0.0860	3.26
298.15	0.1740	4.42
298.15	0.2483	5.39
298.15	0.3464	6.50
298.15	0.4148	7.39
298.15	0.5001	8.34
298.15	0.5774	9.17
298.15	0.6604	10.18
298.15	0.7375	11.13
298.15	0.8143	12.00
298.15	0.9084	12.95
298.15	1.0000	13.70
308.15	0.0000	2.80
308.15	0.0860	5.03
308.15	0.1740	6.91
308.15	0.2483	8.31
308.15	0.3464	10.14
308.15	0.4148	11.44
308.15	0.5001	12.92
308.15	0.5774	14.16
308.15	0.6604	15.68
308.15	0.7375	17.05
308.15	0.8143	18.47
308.15	0.9084	19.93
308.15	1.0000	21.32
318.15	0.0000	4.40
318.15	0.0860	7.75
318.15	0.1740	10.72
318.15	0.2483	12.67
318.15	0.3464	15.24
318.15	0.4148	17.19
318.15	0.5001	19.57
318.15	0.5774	21.44
318.15	0.6604	23.49
318.15	0.7375	25.34
318.15	0.8143	27.58
318.15	0.9084	29.80
318.15	1.0000	31.86

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	953.99
288.15	0.0970	947.69
288.15	0.2041	940.85
288.15	0.3226	933.38
288.15	0.4106	928.0
288.15	0.4991	922.46
288.15	0.6050	915.99
288.15	0.7051	910.0
288.15	0.7934	904.56
288.15	0.8965	898.44
288.15	1.0000	892.18
298.15	0.0000	944.35
298.15	0.0970	937.94
298.15	0.2041	930.96
298.15	0.3226	923.32
298.15	0.4106	917.83
298.15	0.4991	912.15
298.15	0.6050	905.53
298.15	0.7051	899.39
298.15	0.7934	893.82
298.15	0.8965	887.54
298.15	1.0000	881.12
308.15	0.0000	934.69
308.15	0.0970	928.14
308.15	0.2041	921.02
308.15	0.3226	913.2
308.15	0.4106	907.58
308.15	0.4991	901.77
308.15	0.6050	894.69
308.15	0.7051	888.68
308.15	0.7934	882.97
308.15	0.8965	876.52
308.15	1.0000	869.93
318.15	0.0000	924.99
318.15	0.0970	918.29
318.15	0.2041	911.0
318.15	0.3226	903.01
318.15	0.4106	897.24
318.15	0.4991	891.29
318.15	0.6050	884.33
318.15	0.7051	877.86
318.15	0.7934	871.98
318.15	0.8965	865.36
318.15	1.0000	858.58

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane, 1-chloro- (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	953.99
288.15	0.0970	947.69
288.15	0.2041	940.85
288.15	0.3226	933.38
288.15	0.4106	928.0
288.15	0.4991	922.46
288.15	0.6050	915.99
288.15	0.7051	910.0
288.15	0.7934	904.56
288.15	0.8965	898.44
288.15	1.0000	892.18
298.15	0.0000	944.35
298.15	0.0970	937.94
298.15	0.2041	930.96
298.15	0.3226	923.32
298.15	0.4106	917.83
298.15	0.4991	912.15
298.15	0.6050	905.53
298.15	0.7051	899.39
298.15	0.7934	893.82
298.15	0.8965	887.54
298.15	1.0000	881.12
308.15	0.0000	934.69
308.15	0.0970	928.14
308.15	0.2041	921.02
308.15	0.3226	913.2
308.15	0.4106	907.58
308.15	0.4991	901.77
308.15	0.6050	894.69
308.15	0.7051	888.68
308.15	0.7934	882.97
308.15	0.8965	876.52
308.15	1.0000	869.93
318.15	0.0000	924.99
318.15	0.0970	918.29
318.15	0.2041	911.0
318.15	0.3226	903.01
318.15	0.4106	897.24
318.15	0.4991	891.29
318.15	0.6050	884.33
318.15	0.7051	877.86
318.15	0.7934	871.98
318.15	0.8965	865.36
318.15	1.0000	858.58

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