Mixture of Butane, 1-chloro- + Cyclohexanone

Datasets

1. Mole fraction (2)
2. P_vap - Vapor or sublimation pressure, kPa (2)
3. ρ_l - Mass density, kg/m3 (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
0.0690	298.15	0.6500
0.1570	298.15	0.8220
0.2420	298.15	0.8850
0.3380	298.15	0.9230
0.4310	298.15	0.9450
0.5190	298.15	0.9590
0.6190	298.15	0.9710
0.7070	298.15	0.9790
0.7800	298.15	0.9850
0.8800	298.15	0.9920
0.9550	298.15	0.9970
1.0000	298.15	1.0000
0.0000	308.15	0.0000
0.0690	308.15	0.6090
0.1570	308.15	0.7920
0.2420	308.15	0.8630
0.3380	308.15	0.9070
0.4310	308.15	0.9330
0.5190	308.15	0.9500
0.6190	308.15	0.9640
0.7070	308.15	0.9740
0.7800	308.15	0.9820
0.8800	308.15	0.9900
0.9550	308.15	0.9960
1.0000	308.15	1.0000
0.0000	318.15	0.0000
0.0690	318.15	0.5690
0.1570	318.15	0.7680
0.2420	318.15	0.8480
0.3380	318.15	0.8990
0.4310	318.15	0.9270
0.5190	318.15	0.9460
0.6190	318.15	0.9620
0.7070	318.15	0.9730
0.7800	318.15	0.9810
0.8800	318.15	0.9900
0.9550	318.15	0.9960
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
0.0690	298.15	0.6500
0.1570	298.15	0.8220
0.2420	298.15	0.8850
0.3380	298.15	0.9230
0.4310	298.15	0.9450
0.5190	298.15	0.9590
0.6190	298.15	0.9710
0.7070	298.15	0.9790
0.7800	298.15	0.9850
0.8800	298.15	0.9920
0.9550	298.15	0.9970
1.0000	298.15	1.0000
0.0000	308.15	0.0000
0.0690	308.15	0.6090
0.1570	308.15	0.7920
0.2420	308.15	0.8630
0.3380	308.15	0.9070
0.4310	308.15	0.9330
0.5190	308.15	0.9500
0.6190	308.15	0.9640
0.7070	308.15	0.9740
0.7800	308.15	0.9820
0.8800	308.15	0.9900
0.9550	308.15	0.9960
1.0000	308.15	1.0000
0.0000	318.15	0.0000
0.0690	318.15	0.5690
0.1570	318.15	0.7680
0.2420	318.15	0.8480
0.3380	318.15	0.8990
0.4310	318.15	0.9270
0.5190	318.15	0.9460
0.6190	318.15	0.9620
0.7070	318.15	0.9730
0.7800	318.15	0.9810
0.8800	318.15	0.9900
0.9550	318.15	0.9960
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	0.64
0.0690	298.15	1.56
0.1570	298.15	3.06
0.2420	298.15	4.31
0.3380	298.15	5.70
0.4310	298.15	6.84
0.5190	298.15	7.93
0.6190	298.15	9.14
0.7070	298.15	10.22
0.7800	298.15	11.06
0.8800	298.15	12.27
0.9550	298.15	13.26
1.0000	298.15	13.72
0.0000	308.15	1.16
0.0690	308.15	2.73
0.1570	308.15	4.88
0.2420	308.15	6.65
0.3380	308.15	8.29
0.4310	308.15	10.29
0.5190	308.15	11.92
0.6190	308.15	13.78
0.7070	308.15	15.33
0.7800	308.15	16.74
0.8800	308.15	18.71
0.9550	308.15	20.04
1.0000	308.15	20.66
0.0000	318.15	1.92
0.0690	318.15	4.22
0.1570	318.15	7.27
0.2420	318.15	9.77
0.3380	318.15	12.42
0.4310	318.15	15.46
0.5190	318.15	18.10
0.6190	318.15	21.00
0.7070	318.15	23.30
0.7800	318.15	25.49
0.8800	318.15	28.30
0.9550	318.15	30.26
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	0.64
0.0690	298.15	1.56
0.1570	298.15	3.06
0.2420	298.15	4.31
0.3380	298.15	5.70
0.4310	298.15	6.84
0.5190	298.15	7.93
0.6190	298.15	9.14
0.7070	298.15	10.22
0.7800	298.15	11.06
0.8800	298.15	12.27
0.9550	298.15	13.26
1.0000	298.15	13.72
0.0000	308.15	1.16
0.0690	308.15	2.73
0.1570	308.15	4.88
0.2420	308.15	6.65
0.3380	308.15	8.29
0.4310	308.15	10.29
0.5190	308.15	11.92
0.6190	308.15	13.78
0.7070	308.15	15.33
0.7800	308.15	16.74
0.8800	308.15	18.71
0.9550	308.15	20.04
1.0000	308.15	20.66
0.0000	318.15	1.92
0.0690	318.15	4.22
0.1570	318.15	7.27
0.2420	318.15	9.77
0.3380	318.15	12.42
0.4310	318.15	15.46
0.5190	318.15	18.10
0.6190	318.15	21.00
0.7070	318.15	23.30
0.7800	318.15	25.49
0.8800	318.15	28.30
0.9550	318.15	30.26
1.0000	318.15	31.46

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	951.69
288.15	0.1152	945.58
288.15	0.2084	940.43
288.15	0.3068	934.95
288.15	0.4067	929.27
288.15	0.5041	923.6
288.15	0.5841	918.86
288.15	0.6920	912.28
288.15	0.7881	906.18
288.15	0.8820	900.11
288.15	1.0000	892.1
298.15	0.0000	942.76
298.15	0.1152	936.47
298.15	0.2084	931.18
298.15	0.3068	925.51
298.15	0.4067	919.65
298.15	0.5041	913.78
298.15	0.5841	908.86
298.15	0.6920	902.02
298.15	0.7881	895.71
298.15	0.8820	889.37
298.15	1.0000	881.05
308.15	0.0000	933.8
308.15	0.1152	927.34
308.15	0.2084	921.88
308.15	0.3068	916.03
308.15	0.4067	909.97
308.15	0.5041	903.89
308.15	0.5841	898.78
308.15	0.6920	891.68
308.15	0.7881	885.12
308.15	0.8820	878.54
308.15	1.0000	869.86
318.15	0.0000	924.82
318.15	0.1152	918.17
318.15	0.2084	912.54
318.15	0.3068	906.5
318.15	0.4067	900.22
318.15	0.5041	893.92
318.15	0.5841	888.63
318.15	0.6920	881.25
318.15	0.7881	874.42
318.15	0.8820	867.57
318.15	1.0000	858.52

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	951.69
288.15	0.1152	945.58
288.15	0.2084	940.43
288.15	0.3068	934.95
288.15	0.4067	929.27
288.15	0.5041	923.6
288.15	0.5841	918.86
288.15	0.6920	912.28
288.15	0.7881	906.18
288.15	0.8820	900.11
288.15	1.0000	892.1
298.15	0.0000	942.76
298.15	0.1152	936.47
298.15	0.2084	931.18
298.15	0.3068	925.51
298.15	0.4067	919.65
298.15	0.5041	913.78
298.15	0.5841	908.86
298.15	0.6920	902.02
298.15	0.7881	895.71
298.15	0.8820	889.37
298.15	1.0000	881.05
308.15	0.0000	933.8
308.15	0.1152	927.34
308.15	0.2084	921.88
308.15	0.3068	916.03
308.15	0.4067	909.97
308.15	0.5041	903.89
308.15	0.5841	898.78
308.15	0.6920	891.68
308.15	0.7881	885.12
308.15	0.8820	878.54
308.15	1.0000	869.86
318.15	0.0000	924.82
318.15	0.1152	918.17
318.15	0.2084	912.54
318.15	0.3068	906.5
318.15	0.4067	900.22
318.15	0.5041	893.92
318.15	0.5841	888.63
318.15	0.6920	881.25
318.15	0.7881	874.42
318.15	0.8820	867.57
318.15	1.0000	858.52

Sources

• (Vapour + liquid) equilibria and excess Gibbs free energies of (cyclohexanone + 1- chlorobutane and + 1,1,1-trichloroethane) binary mixtures at temperatures from (298.15 to 318.15) K
• Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K