Mixture of Ethane, 1,1,1-trichloro- + Cyclopentanone

Datasets

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

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	1.61
0.0000	303.15	2.03
0.0000	308.15	2.68
0.0000	313.15	3.41
0.0675	298.15	2.81
0.0675	303.15	3.53
0.0675	308.15	4.44
0.0675	313.15	5.35
0.1239	298.15	3.66
0.1239	303.15	4.56
0.1239	308.15	5.68
0.1239	313.15	7.18
0.2112	298.15	4.88
0.2112	303.15	6.06
0.2112	308.15	7.51
0.2112	313.15	9.44
0.2783	298.15	5.94
0.2783	303.15	7.46
0.2783	308.15	9.21
0.2783	313.15	11.43
0.3559	298.15	7.30
0.3559	303.15	9.03
0.3559	308.15	10.95
0.3559	313.15	13.67
0.4288	298.15	8.38
0.4288	303.15	10.43
0.4288	308.15	12.82
0.4288	313.15	15.67
0.5248	298.15	9.67
0.5248	303.15	12.15
0.5248	308.15	15.08
0.5248	313.15	18.19
0.6382	298.15	11.20
0.6382	303.15	13.93
0.6382	308.15	17.31
0.6382	313.15	21.30
0.7347	298.15	12.89
0.7347	303.15	15.96
0.7347	308.15	19.74
0.7347	313.15	24.13
0.8747	298.15	14.98
0.8747	303.15	18.47
0.8747	308.15	22.78
0.8747	313.15	27.69
0.9315	298.15	15.95
0.9315	303.15	19.21
0.9315	308.15	23.82
0.9315	313.15	29.10
1.0000	298.15	16.69
1.0000	303.15	20.34
1.0000	308.15	25.22
1.0000	313.15	30.78

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	953.99
288.15	0.1165	1006.37
288.15	0.2125	1048.24
288.15	0.3002	1085.47
288.15	0.4003	1126.73
288.15	0.4938	1164.1
288.15	0.5938	1202.79
288.15	0.6952	1240.7
288.15	0.7988	1277.98
288.15	0.9110	1316.7
288.15	1.0000	1346.17
298.15	0.0000	944.35
298.15	0.1165	995.99
298.15	0.2125	1037.23
298.15	0.3002	1073.88
298.15	0.4003	1114.46
298.15	0.4938	1151.18
298.15	0.5938	1189.17
298.15	0.6952	1226.35
298.15	0.7988	1262.86
298.15	0.9110	1300.71
298.15	1.0000	1329.49
308.15	0.0000	934.69
308.15	0.1165	985.56
308.15	0.2125	1026.17
308.15	0.3002	1062.22
308.15	0.4003	1102.11
308.15	0.4938	1138.19
308.15	0.5938	1175.46
308.15	0.6952	1211.89
308.15	0.7988	1247.62
308.15	0.9110	1284.6
308.15	1.0000	1312.65
318.15	0.0000	924.99
318.15	0.1165	975.08
318.15	0.2125	1015.04
318.15	0.3002	1050.49
318.15	0.4003	1089.7
318.15	0.4938	1125.09
318.15	0.5938	1161.64
318.15	0.6952	1197.32
318.15	0.7988	1232.24
318.15	0.9110	1268.34
318.15	1.0000	1295.66

Sources

• Isothermal (vapour + liquid) equilibria in the binary mixtures (1,2-dichloroethane and 1,1,1-trichloroethane with cyclopentanone) within the temperature range (298.15 to 313.15) 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

Note: These property values are available through the Cheméo API. A free account gives you an access key.