Mixture of Ethane, 1,1,1-trichloro- + 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 Ethane, 1,1,1-trichloro- (1) [ref]

Fixed		Measured
Mole fraction of Ethane, 1,1,1-trichloro- (1) - Liquid	Temperature, K - Liquid	Mole fraction of Ethane, 1,1,1-trichloro- (1) - Gas
0.0000	298.15	0.0000
0.0750	298.15	0.6660
0.1650	298.15	0.8310
0.2710	298.15	0.9030
0.3600	298.15	0.9340
0.4400	298.15	0.9520
0.5070	298.15	0.9630
0.5710	298.15	0.9710
0.6520	298.15	0.9790
0.7250	298.15	0.9850
0.7950	298.15	0.9900
0.8550	298.15	0.9930
0.9480	298.15	0.9980
1.0000	298.15	1.0000
0.0000	308.15	0.0000
0.0750	308.15	0.6290
0.1650	308.15	0.8050
0.2710	308.15	0.8860
0.3590	308.15	0.9220
0.4400	308.15	0.9430
0.5070	308.15	0.9560
0.5710	308.15	0.9660
0.6520	308.15	0.9760
0.7250	308.15	0.9830
0.7950	308.15	0.9880
0.8550	308.15	0.9930
0.9480	308.15	0.9980
1.0000	308.15	1.0000
0.0000	318.15	0.0000
0.0750	318.15	0.5970
0.1650	318.15	0.7870
0.2710	318.15	0.8760
0.3590	318.15	0.9150
0.4400	318.15	0.9380
0.5070	318.15	0.9520
0.5710	318.15	0.9620
0.6520	318.15	0.9730
0.7250	318.15	0.9810
0.7950	318.15	0.9860
0.8550	318.15	0.9910
0.9480	318.15	0.9970
1.0000	318.15	1.0000

Mole fraction of Ethane, 1,1,1-trichloro- (1) [ref]

Fixed		Measured
Mole fraction of Ethane, 1,1,1-trichloro- (1) - Liquid	Temperature, K - Liquid	Mole fraction of Ethane, 1,1,1-trichloro- (1) - Gas
0.0000	298.15	0.0000
0.0750	298.15	0.6660
0.1650	298.15	0.8310
0.2710	298.15	0.9030
0.3600	298.15	0.9340
0.4400	298.15	0.9520
0.5070	298.15	0.9630
0.5710	298.15	0.9710
0.6520	298.15	0.9790
0.7250	298.15	0.9850
0.7950	298.15	0.9900
0.8550	298.15	0.9930
0.9480	298.15	0.9980
1.0000	298.15	1.0000
0.0000	308.15	0.0000
0.0750	308.15	0.6290
0.1650	308.15	0.8050
0.2710	308.15	0.8860
0.3590	308.15	0.9220
0.4400	308.15	0.9430
0.5070	308.15	0.9560
0.5710	308.15	0.9660
0.6520	308.15	0.9760
0.7250	308.15	0.9830
0.7950	308.15	0.9880
0.8550	308.15	0.9930
0.9480	308.15	0.9980
1.0000	308.15	1.0000
0.0000	318.15	0.0000
0.0750	318.15	0.5970
0.1650	318.15	0.7870
0.2710	318.15	0.8760
0.3590	318.15	0.9150
0.4400	318.15	0.9380
0.5070	318.15	0.9520
0.5710	318.15	0.9620
0.6520	318.15	0.9730
0.7250	318.15	0.9810
0.7950	318.15	0.9860
0.8550	318.15	0.9910
0.9480	318.15	0.9970
1.0000	318.15	1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethane, 1,1,1-trichloro- (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	298.15	0.64
0.0750	298.15	1.73
0.1650	298.15	3.21
0.2710	298.15	4.77
0.3600	298.15	6.26
0.4400	298.15	7.59
0.5070	298.15	8.68
0.5710	298.15	9.69
0.6520	298.15	10.82
0.7250	298.15	12.02
0.7950	298.15	13.50
0.8550	298.15	14.36
0.9480	298.15	15.78
1.0000	298.15	16.64
0.0000	308.15	1.16
0.0750	308.15	2.83
0.1650	308.15	4.95
0.2710	308.15	7.51
0.3590	308.15	9.58
0.4400	308.15	11.64
0.5070	308.15	13.21
0.5710	308.15	14.96
0.6520	308.15	16.84
0.7250	308.15	18.69
0.7950	308.15	20.38
0.8550	308.15	22.17
0.9480	308.15	24.37
1.0000	308.15	25.85
0.0000	318.15	1.92
0.0750	318.15	4.48
0.1650	318.15	7.60
0.2710	318.15	11.52
0.3590	318.15	14.41
0.4400	318.15	17.37
0.5070	318.15	19.90
0.5710	318.15	22.32
0.6520	318.15	25.22
0.7250	318.15	27.98
0.7950	318.15	30.21
0.8550	318.15	32.50
0.9480	318.15	35.94
1.0000	318.15	37.61

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethane, 1,1,1-trichloro- (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	298.15	0.64
0.0750	298.15	1.73
0.1650	298.15	3.21
0.2710	298.15	4.77
0.3600	298.15	6.26
0.4400	298.15	7.59
0.5070	298.15	8.68
0.5710	298.15	9.69
0.6520	298.15	10.82
0.7250	298.15	12.02
0.7950	298.15	13.50
0.8550	298.15	14.36
0.9480	298.15	15.78
1.0000	298.15	16.64
0.0000	308.15	1.16
0.0750	308.15	2.83
0.1650	308.15	4.95
0.2710	308.15	7.51
0.3590	308.15	9.58
0.4400	308.15	11.64
0.5070	308.15	13.21
0.5710	308.15	14.96
0.6520	308.15	16.84
0.7250	308.15	18.69
0.7950	308.15	20.38
0.8550	308.15	22.17
0.9480	308.15	24.37
1.0000	308.15	25.85
0.0000	318.15	1.92
0.0750	318.15	4.48
0.1650	318.15	7.60
0.2710	318.15	11.52
0.3590	318.15	14.41
0.4400	318.15	17.37
0.5070	318.15	19.90
0.5710	318.15	22.32
0.6520	318.15	25.22
0.7250	318.15	27.98
0.7950	318.15	30.21
0.8550	318.15	32.50
0.9480	318.15	35.94
1.0000	318.15	37.61

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,1,1-trichloro- (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	951.69
288.15	0.1151	996.74
288.15	0.2288	1041.75
288.15	0.3155	1076.19
288.15	0.4163	1116.3
288.15	0.5167	1156.17
288.15	0.6059	1191.52
288.15	0.7081	1231.85
288.15	0.8062	1270.3
288.15	0.8979	1305.81
288.15	1.0000	1344.95
298.15	0.0000	942.76
298.15	0.1151	987.13
298.15	0.2288	1031.43
298.15	0.3155	1065.28
298.15	0.4163	1104.68
298.15	0.5167	1143.81
298.15	0.6059	1178.45
298.15	0.7081	1217.94
298.15	0.8062	1255.52
298.15	0.8979	1290.16
298.15	1.0000	1328.27
308.15	0.0000	933.8
308.15	0.1151	977.49
308.15	0.2288	1021.06
308.15	0.3155	1054.33
308.15	0.4163	1093.01
308.15	0.5167	1131.39
308.15	0.6059	1165.33
308.15	0.7081	1203.95
308.15	0.8062	1240.64
308.15	0.8979	1274.41
308.15	1.0000	1311.45
318.15	0.0000	924.82
318.15	0.1151	967.81
318.15	0.2288	1010.65
318.15	0.3155	1043.33
318.15	0.4163	1081.28
318.15	0.5167	1118.9
318.15	0.6059	1152.12
318.15	0.7081	1189.86
318.15	0.8062	1225.64
318.15	0.8979	1258.51
318.15	1.0000	1294.47

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,1,1-trichloro- (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	951.69
288.15	0.1151	996.74
288.15	0.2288	1041.75
288.15	0.3155	1076.19
288.15	0.4163	1116.3
288.15	0.5167	1156.17
288.15	0.6059	1191.52
288.15	0.7081	1231.85
288.15	0.8062	1270.3
288.15	0.8979	1305.81
288.15	1.0000	1344.95
298.15	0.0000	942.76
298.15	0.1151	987.13
298.15	0.2288	1031.43
298.15	0.3155	1065.28
298.15	0.4163	1104.68
298.15	0.5167	1143.81
298.15	0.6059	1178.45
298.15	0.7081	1217.94
298.15	0.8062	1255.52
298.15	0.8979	1290.16
298.15	1.0000	1328.27
308.15	0.0000	933.8
308.15	0.1151	977.49
308.15	0.2288	1021.06
308.15	0.3155	1054.33
308.15	0.4163	1093.01
308.15	0.5167	1131.39
308.15	0.6059	1165.33
308.15	0.7081	1203.95
308.15	0.8062	1240.64
308.15	0.8979	1274.41
308.15	1.0000	1311.45
318.15	0.0000	924.82
318.15	0.1151	967.81
318.15	0.2288	1010.65
318.15	0.3155	1043.33
318.15	0.4163	1081.28
318.15	0.5167	1118.9
318.15	0.6059	1152.12
318.15	0.7081	1189.86
318.15	0.8062	1225.64
318.15	0.8979	1258.51
318.15	1.0000	1294.47

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