Mixture of Cyclohexanone + Ethane, 1,2-dichloro-

Datasets

1. ρ_l - Mass density, kg/m3 (2)
2. Vapor or sublimation pressure, kPa (2)
3. Excess molar volume, m3/mol (2)

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	951.69
288.15	0.1142	978.81
288.15	0.2318	1008.61
288.15	0.3197	1032.1
288.15	0.4227	1061.02
288.15	0.5190	1089.5
288.15	0.6155	1119.7
288.15	0.7061	1149.67
288.15	0.8134	1187.43
288.15	0.9145	1225.5
288.15	1.0000	1260.01
298.15	0.0000	942.76
298.15	0.1142	969.5
298.15	0.2318	998.88
298.15	0.3197	1022.0
298.15	0.4227	1050.47
298.15	0.5190	1078.46
298.15	0.6155	1108.12
298.15	0.7061	1137.52
298.15	0.8134	1174.53
298.15	0.9145	1211.76
298.15	1.0000	1245.48
308.15	0.0000	933.8
308.15	0.1142	960.16
308.15	0.2318	989.1
308.15	0.3197	1011.86
308.15	0.4227	1039.86
308.15	0.5190	1067.36
308.15	0.6155	1096.48
308.15	0.7061	1125.3
308.15	0.8134	1161.53
308.15	0.9145	1197.92
308.15	1.0000	1230.83
318.15	0.0000	924.82
318.15	0.1142	950.78
318.15	0.2318	979.28
318.15	0.3197	1001.67
318.15	0.4227	1029.19
318.15	0.5190	1056.19
318.15	0.6155	1084.75
318.15	0.7061	1112.98
318.15	0.8134	1148.42
318.15	0.9145	1183.96
318.15	1.0000	1216.04

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	951.69
288.15	0.1142	978.81
288.15	0.2318	1008.61
288.15	0.3197	1032.1
288.15	0.4227	1061.02
288.15	0.5190	1089.5
288.15	0.6155	1119.7
288.15	0.7061	1149.67
288.15	0.8134	1187.43
288.15	0.9145	1225.5
288.15	1.0000	1260.01
298.15	0.0000	942.76
298.15	0.1142	969.5
298.15	0.2318	998.88
298.15	0.3197	1022.0
298.15	0.4227	1050.47
298.15	0.5190	1078.46
298.15	0.6155	1108.12
298.15	0.7061	1137.52
298.15	0.8134	1174.53
298.15	0.9145	1211.76
298.15	1.0000	1245.48
308.15	0.0000	933.8
308.15	0.1142	960.16
308.15	0.2318	989.1
308.15	0.3197	1011.86
308.15	0.4227	1039.86
308.15	0.5190	1067.36
308.15	0.6155	1096.48
308.15	0.7061	1125.3
308.15	0.8134	1161.53
308.15	0.9145	1197.92
308.15	1.0000	1230.83
318.15	0.0000	924.82
318.15	0.1142	950.78
318.15	0.2318	979.28
318.15	0.3197	1001.67
318.15	0.4227	1029.19
318.15	0.5190	1056.19
318.15	0.6155	1084.75
318.15	0.7061	1112.98
318.15	0.8134	1148.42
318.15	0.9145	1183.96
318.15	1.0000	1216.04

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Gas
0.0000	308.15	1.15
0.0000	318.15	1.91
0.0736	308.15	1.75
0.0736	318.15	2.98
0.1476	308.15	2.74
0.1476	318.15	4.12
0.2469	308.15	3.92
0.2469	318.15	5.90
0.3170	308.15	4.76
0.3170	318.15	7.40
0.4115	298.15	3.85
0.4115	308.15	6.34
0.4115	318.15	9.66
0.4815	298.15	4.64
0.4815	308.15	7.50
0.4815	318.15	11.33
0.5685	298.15	5.74
0.5685	308.15	8.96
0.5685	318.15	13.68
0.6298	298.15	6.35
0.6298	308.15	10.11
0.6298	318.15	15.41
0.7147	298.15	7.49
0.7147	308.15	11.91
0.7147	318.15	18.10
0.7703	298.15	8.11
0.7703	308.15	12.69
0.7703	318.15	19.55
0.8424	298.15	9.06
0.8424	308.15	14.17
0.8424	318.15	21.65
0.9307	298.15	10.04
0.9307	308.15	15.74
0.9307	318.15	24.05
1.0000	298.15	10.81
1.0000	308.15	17.02
1.0000	318.15	25.77

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethane, 1,2-dichloro- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Gas
0.0000	308.15	1.15
0.0000	318.15	1.91
0.0736	308.15	1.75
0.0736	318.15	2.98
0.1476	308.15	2.74
0.1476	318.15	4.12
0.2469	308.15	3.92
0.2469	318.15	5.90
0.3170	308.15	4.76
0.3170	318.15	7.40
0.4115	298.15	3.85
0.4115	308.15	6.34
0.4115	318.15	9.66
0.4815	298.15	4.64
0.4815	308.15	7.50
0.4815	318.15	11.33
0.5685	298.15	5.74
0.5685	308.15	8.96
0.5685	318.15	13.68
0.6298	298.15	6.35
0.6298	308.15	10.11
0.6298	318.15	15.41
0.7147	298.15	7.49
0.7147	308.15	11.91
0.7147	318.15	18.10
0.7703	298.15	8.11
0.7703	308.15	12.69
0.7703	318.15	19.55
0.8424	298.15	9.06
0.8424	308.15	14.17
0.8424	318.15	21.65
0.9307	298.15	10.04
0.9307	308.15	15.74
0.9307	318.15	24.05
1.0000	298.15	10.81
1.0000	308.15	17.02
1.0000	318.15	25.77

Excess molar volume, m3/mol [ref]

Fixed		Measured
Mole fraction of Cyclohexanone (1) - Liquid	Temperature, K - Liquid	Excess molar volume, m3/mol - Liquid
0.0494	288.15	3.1700e-08
0.1004	288.15	6.3100e-08
0.1499	288.15	8.8000e-08
0.2002	288.15	1.0900e-07
0.2500	288.15	1.1980e-07
0.3002	288.15	1.2740e-07
0.3496	288.15	1.3080e-07
0.3997	288.15	1.3080e-07
0.4487	288.15	1.2330e-07
0.5000	288.15	1.1870e-07
0.5498	288.15	1.0840e-07
0.5997	288.15	9.9500e-08
0.6500	288.15	8.6700e-08
0.6994	288.15	7.1000e-08
0.7503	288.15	5.0000e-08
0.7993	288.15	2.7100e-08
0.8494	288.15	0.0000
0.8985	288.15	-1.3300e-08
0.9477	288.15	-1.9500e-08
0.0494	293.15	2.7200e-08
0.1004	293.15	5.9200e-08
0.1499	293.15	8.2500e-08
0.2002	293.15	1.0200e-07
0.2500	293.15	1.1320e-07
0.3002	293.15	1.2000e-07
0.3496	293.15	1.2090e-07
0.3997	293.15	1.2150e-07
0.4487	293.15	1.1410e-07
0.5000	293.15	1.0870e-07
0.5498	293.15	9.9100e-08
0.5997	293.15	9.0800e-08
0.6500	293.15	8.1100e-08
0.6994	293.15	6.7000e-08
0.7503	293.15	5.0200e-08
0.7993	293.15	2.9400e-08
0.8494	293.15	0.0000
0.8985	293.15	-1.1700e-08
0.9477	293.15	-1.8900e-08
0.0494	298.15	2.4600e-08
0.1004	298.15	5.4900e-08
0.1499	298.15	7.7000e-08
0.2002	298.15	9.5000e-08
0.2500	298.15	1.0560e-07
0.3002	298.15	1.1150e-07
0.3496	298.15	1.0920e-07
0.3997	298.15	1.0810e-07
0.4487	298.15	1.0420e-07
0.5000	298.15	9.8800e-08
0.5498	298.15	8.9400e-08
0.5997	298.15	8.4700e-08
0.6500	298.15	7.5500e-08
0.6994	298.15	6.4900e-08
0.7503	298.15	4.9200e-08
0.7993	298.15	2.9300e-08
0.8494	298.15	0.0000
0.8985	298.15	-1.0800e-08
0.9477	298.15	-1.8400e-08
0.0494	303.15	2.2900e-08
0.1004	303.15	5.0400e-08
0.1499	303.15	7.1400e-08
0.2002	303.15	8.7900e-08
0.2500	303.15	9.7200e-08
0.3002	303.15	1.0180e-07
0.3496	303.15	9.8700e-08
0.3997	303.15	9.7500e-08
0.4487	303.15	9.3300e-08
0.5000	303.15	8.8300e-08
0.5498	303.15	7.9100e-08
0.5997	303.15	7.3800e-08
0.6500	303.15	6.5900e-08
0.6994	303.15	5.5800e-08
0.7503	303.15	4.1000e-08
0.7993	303.15	2.3700e-08
0.8494	303.15	0.0000
0.8985	303.15	-1.0200e-08
0.9477	303.15	-1.6500e-08
0.0494	308.15	2.1300e-08
0.1004	308.15	4.6000e-08
0.1499	308.15	6.5000e-08
0.2002	308.15	8.0300e-08
0.2500	308.15	8.8600e-08
0.3002	308.15	9.2500e-08
0.3496	308.15	8.9400e-08
0.3997	308.15	8.6400e-08
0.4487	308.15	8.2400e-08
0.5000	308.15	7.7500e-08
0.5498	308.15	6.8300e-08
0.5997	308.15	6.1500e-08
0.6500	308.15	5.4300e-08
0.6994	308.15	4.5300e-08
0.7503	308.15	3.3300e-08
0.7993	308.15	1.8600e-08
0.8494	308.15	0.0000
0.8985	308.15	-0.0000
0.9477	308.15	-1.4700e-08
0.0494	313.15	1.9500e-08
0.1004	313.15	4.0900e-08
0.1499	313.15	5.8400e-08
0.2002	313.15	7.2200e-08
0.2500	313.15	7.9800e-08
0.3002	313.15	8.2100e-08
0.3496	313.15	7.9400e-08
0.3997	313.15	7.5500e-08
0.4487	313.15	7.0200e-08
0.5000	313.15	6.5900e-08
0.5498	313.15	5.7200e-08
0.5997	313.15	5.0900e-08
0.6500	313.15	4.3500e-08
0.6994	313.15	3.5100e-08
0.7503	313.15	2.5000e-08
0.7993	313.15	1.2900e-08
0.8494	313.15	0.0000
0.8985	313.15	-0.0000
0.9477	313.15	-1.2700e-08

Excess molar volume, m3/mol [ref]

Fixed		Measured
Mole fraction of Cyclohexanone (1) - Liquid	Temperature, K - Liquid	Excess molar volume, m3/mol - Liquid
0.0494	288.15	3.1700e-08
0.1004	288.15	6.3100e-08
0.1499	288.15	8.8000e-08
0.2002	288.15	1.0900e-07
0.2500	288.15	1.1980e-07
0.3002	288.15	1.2740e-07
0.3496	288.15	1.3080e-07
0.3997	288.15	1.3080e-07
0.4487	288.15	1.2330e-07
0.5000	288.15	1.1870e-07
0.5498	288.15	1.0840e-07
0.5997	288.15	9.9500e-08
0.6500	288.15	8.6700e-08
0.6994	288.15	7.1000e-08
0.7503	288.15	5.0000e-08
0.7993	288.15	2.7100e-08
0.8494	288.15	0.0000
0.8985	288.15	-1.3300e-08
0.9477	288.15	-1.9500e-08
0.0494	293.15	2.7200e-08
0.1004	293.15	5.9200e-08
0.1499	293.15	8.2500e-08
0.2002	293.15	1.0200e-07
0.2500	293.15	1.1320e-07
0.3002	293.15	1.2000e-07
0.3496	293.15	1.2090e-07
0.3997	293.15	1.2150e-07
0.4487	293.15	1.1410e-07
0.5000	293.15	1.0870e-07
0.5498	293.15	9.9100e-08
0.5997	293.15	9.0800e-08
0.6500	293.15	8.1100e-08
0.6994	293.15	6.7000e-08
0.7503	293.15	5.0200e-08
0.7993	293.15	2.9400e-08
0.8494	293.15	0.0000
0.8985	293.15	-1.1700e-08
0.9477	293.15	-1.8900e-08
0.0494	298.15	2.4600e-08
0.1004	298.15	5.4900e-08
0.1499	298.15	7.7000e-08
0.2002	298.15	9.5000e-08
0.2500	298.15	1.0560e-07
0.3002	298.15	1.1150e-07
0.3496	298.15	1.0920e-07
0.3997	298.15	1.0810e-07
0.4487	298.15	1.0420e-07
0.5000	298.15	9.8800e-08
0.5498	298.15	8.9400e-08
0.5997	298.15	8.4700e-08
0.6500	298.15	7.5500e-08
0.6994	298.15	6.4900e-08
0.7503	298.15	4.9200e-08
0.7993	298.15	2.9300e-08
0.8494	298.15	0.0000
0.8985	298.15	-1.0800e-08
0.9477	298.15	-1.8400e-08
0.0494	303.15	2.2900e-08
0.1004	303.15	5.0400e-08
0.1499	303.15	7.1400e-08
0.2002	303.15	8.7900e-08
0.2500	303.15	9.7200e-08
0.3002	303.15	1.0180e-07
0.3496	303.15	9.8700e-08
0.3997	303.15	9.7500e-08
0.4487	303.15	9.3300e-08
0.5000	303.15	8.8300e-08
0.5498	303.15	7.9100e-08
0.5997	303.15	7.3800e-08
0.6500	303.15	6.5900e-08
0.6994	303.15	5.5800e-08
0.7503	303.15	4.1000e-08
0.7993	303.15	2.3700e-08
0.8494	303.15	0.0000
0.8985	303.15	-1.0200e-08
0.9477	303.15	-1.6500e-08
0.0494	308.15	2.1300e-08
0.1004	308.15	4.6000e-08
0.1499	308.15	6.5000e-08
0.2002	308.15	8.0300e-08
0.2500	308.15	8.8600e-08
0.3002	308.15	9.2500e-08
0.3496	308.15	8.9400e-08
0.3997	308.15	8.6400e-08
0.4487	308.15	8.2400e-08
0.5000	308.15	7.7500e-08
0.5498	308.15	6.8300e-08
0.5997	308.15	6.1500e-08
0.6500	308.15	5.4300e-08
0.6994	308.15	4.5300e-08
0.7503	308.15	3.3300e-08
0.7993	308.15	1.8600e-08
0.8494	308.15	0.0000
0.8985	308.15	-0.0000
0.9477	308.15	-1.4700e-08
0.0494	313.15	1.9500e-08
0.1004	313.15	4.0900e-08
0.1499	313.15	5.8400e-08
0.2002	313.15	7.2200e-08
0.2500	313.15	7.9800e-08
0.3002	313.15	8.2100e-08
0.3496	313.15	7.9400e-08
0.3997	313.15	7.5500e-08
0.4487	313.15	7.0200e-08
0.5000	313.15	6.5900e-08
0.5498	313.15	5.7200e-08
0.5997	313.15	5.0900e-08
0.6500	313.15	4.3500e-08
0.6994	313.15	3.5100e-08
0.7503	313.15	2.5000e-08
0.7993	313.15	1.2900e-08
0.8494	313.15	0.0000
0.8985	313.15	-0.0000
0.9477	313.15	-1.2700e-08

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
• Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
• Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K