Mixture of Trichloromethane + Cyclohexanone

Datasets

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

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Trichloromethane (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	951.69
288.15	0.1198	1004.15
288.15	0.2362	1058.19
288.15	0.3050	1091.64
288.15	0.4235	1151.88
288.15	0.5103	1198.22
288.15	0.6047	1250.45
288.15	0.6953	1303.06
288.15	0.8109	1372.1
288.15	0.9089	1433.35
288.15	1.0000	1491.86
298.15	0.0000	942.76
298.15	0.1198	994.58
298.15	0.2362	1047.93
298.15	0.3050	1080.94
298.15	0.4235	1140.29
298.15	0.5103	1185.89
298.15	0.6047	1237.16
298.15	0.6953	1288.8
298.15	0.8109	1356.3
298.15	0.9089	1416.12
298.15	1.0000	1473.16
308.15	0.0000	933.8
308.15	0.1198	984.97
308.15	0.2362	1037.61
308.15	0.3050	1070.16
308.15	0.4235	1128.62
308.15	0.5103	1173.48
308.15	0.6047	1223.78
308.15	0.6953	1274.42
308.15	0.8109	1340.36
308.15	0.9089	1398.68
308.15	1.0000	1454.07
318.15	0.0000	924.82
318.15	0.1198	975.32
318.15	0.2362	1027.25
318.15	0.3050	1059.32
318.15	0.4235	1116.88
318.15	0.5103	1160.97
318.15	0.6047	1210.28
318.15	0.6953	1259.9
318.15	0.8109	1324.23
318.15	0.9089	1381.01
318.15	1.0000	1434.72

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Trichloromethane (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	951.69
288.15	0.1198	1004.15
288.15	0.2362	1058.19
288.15	0.3050	1091.64
288.15	0.4235	1151.88
288.15	0.5103	1198.22
288.15	0.6047	1250.45
288.15	0.6953	1303.06
288.15	0.8109	1372.1
288.15	0.9089	1433.35
288.15	1.0000	1491.86
298.15	0.0000	942.76
298.15	0.1198	994.58
298.15	0.2362	1047.93
298.15	0.3050	1080.94
298.15	0.4235	1140.29
298.15	0.5103	1185.89
298.15	0.6047	1237.16
298.15	0.6953	1288.8
298.15	0.8109	1356.3
298.15	0.9089	1416.12
298.15	1.0000	1473.16
308.15	0.0000	933.8
308.15	0.1198	984.97
308.15	0.2362	1037.61
308.15	0.3050	1070.16
308.15	0.4235	1128.62
308.15	0.5103	1173.48
308.15	0.6047	1223.78
308.15	0.6953	1274.42
308.15	0.8109	1340.36
308.15	0.9089	1398.68
308.15	1.0000	1454.07
318.15	0.0000	924.82
318.15	0.1198	975.32
318.15	0.2362	1027.25
318.15	0.3050	1059.32
318.15	0.4235	1116.88
318.15	0.5103	1160.97
318.15	0.6047	1210.28
318.15	0.6953	1259.9
318.15	0.8109	1324.23
318.15	0.9089	1381.01
318.15	1.0000	1434.72

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Trichloromethane (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Gas
0.0000	298.15	0.64
0.0000	308.15	1.15
0.0000	318.15	1.91
0.0884	298.15	1.29
0.0884	308.15	2.29
0.0884	318.15	3.59
0.1709	298.15	2.34
0.1709	308.15	3.67
0.1709	318.15	5.57
0.2443	298.15	2.94
0.2443	308.15	4.80
0.2443	318.15	7.74
0.2981	298.15	3.84
0.2981	308.15	6.17
0.2981	318.15	9.53
0.3763	298.15	5.18
0.3763	308.15	8.33
0.3763	318.15	12.94
0.4433	298.15	6.66
0.4433	308.15	10.57
0.4433	318.15	16.15
0.4888	298.15	8.07
0.4888	308.15	12.32
0.4888	318.15	18.76
0.5876	298.15	10.97
0.5876	308.15	17.09
0.5876	318.15	25.60
0.6839	298.15	14.75
0.6839	308.15	22.59
0.6839	318.15	33.62
0.7571	298.15	17.88
0.7571	308.15	27.02
0.7571	318.15	40.05
0.8005	298.15	19.81
0.8005	308.15	29.94
0.8005	318.15	43.91
0.8595	298.15	22.05
0.8595	308.15	33.06
0.8595	318.15	48.67
0.9074	298.15	23.87
0.9074	308.15	36.05
0.9074	318.15	51.85
0.9635	298.15	25.46
0.9635	308.15	38.55
0.9635	318.15	56.78
1.0000	298.15	26.44
1.0000	308.15	40.19
1.0000	318.15	58.68

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Trichloromethane (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Gas
0.0000	298.15	0.64
0.0000	308.15	1.15
0.0000	318.15	1.91
0.0884	298.15	1.29
0.0884	308.15	2.29
0.0884	318.15	3.59
0.1709	298.15	2.34
0.1709	308.15	3.67
0.1709	318.15	5.57
0.2443	298.15	2.94
0.2443	308.15	4.80
0.2443	318.15	7.74
0.2981	298.15	3.84
0.2981	308.15	6.17
0.2981	318.15	9.53
0.3763	298.15	5.18
0.3763	308.15	8.33
0.3763	318.15	12.94
0.4433	298.15	6.66
0.4433	308.15	10.57
0.4433	318.15	16.15
0.4888	298.15	8.07
0.4888	308.15	12.32
0.4888	318.15	18.76
0.5876	298.15	10.97
0.5876	308.15	17.09
0.5876	318.15	25.60
0.6839	298.15	14.75
0.6839	308.15	22.59
0.6839	318.15	33.62
0.7571	298.15	17.88
0.7571	308.15	27.02
0.7571	318.15	40.05
0.8005	298.15	19.81
0.8005	308.15	29.94
0.8005	318.15	43.91
0.8595	298.15	22.05
0.8595	308.15	33.06
0.8595	318.15	48.67
0.9074	298.15	23.87
0.9074	308.15	36.05
0.9074	318.15	51.85
0.9635	298.15	25.46
0.9635	308.15	38.55
0.9635	318.15	56.78
1.0000	298.15	26.44
1.0000	308.15	40.19
1.0000	318.15	58.68

Sources

• Vapour pressure and excess Gibbs energy of binary 1,2-dichloroethane + cyclohexanone, chloroform + cyclopentanone and chloroform + cyclohexanone 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