Mixture of Cyclopentanone + Ethane, 1,1,2,2-tetrachloro-

Datasets

1. Azeotropic composition: mole fraction (4)
2. P_vap - Vapor or sublimation pressure, kPa (2)
3. ρ_l - Mass density, kg/m3 (2)
4. Azeotropic pressure, kPa (2)

Azeotropic composition: mole fraction of Cyclopentanone (1) [ref]

Temperature, K - Liquid	Azeotropic composition: mole fraction of Cyclopentanone (1) - Liquid
343.15	0.3038
353.15	0.2806
363.15	0.2746

Mole fraction of Cyclopentanone (1) [ref]

Fixed		Measured
Mole fraction of Cyclopentanone (1) - Liquid	Temperature, K - Gas	Mole fraction of Cyclopentanone (1) - Gas
0.0000	343.15	0.0000
0.0000	353.15	0.0000
0.0000	363.15	0.0000
0.0623	353.15	0.0497
0.0623	363.15	0.0522
0.0648	343.15	0.0497
0.1045	343.15	0.0748
0.1144	353.15	0.0848
0.1144	363.15	0.0897
0.1556	363.15	0.1314
0.1580	343.15	0.1266
0.1580	353.15	0.1266
0.2169	343.15	0.1889
0.2169	353.15	0.1959
0.2169	363.15	0.1959
0.2741	353.15	0.2786
0.2741	363.15	0.2853
0.2763	343.15	0.2718
0.3402	343.15	0.3892
0.3440	363.15	0.3912
0.3446	353.15	0.3892
0.4222	343.15	0.5284
0.4222	353.15	0.5284
0.4243	363.15	0.5208
0.4803	343.15	0.6260
0.4803	363.15	0.6225
0.4842	353.15	0.6225
0.5527	343.15	0.7244
0.5527	363.15	0.7244
0.5582	353.15	0.7244
0.6260	343.15	0.8093
0.6260	353.15	0.8107
0.6260	363.15	0.8079
0.6927	363.15	0.8659
0.6943	353.15	0.8709
0.6960	343.15	0.8796
0.7695	343.15	0.9312
0.7753	353.15	0.9238
0.7783	363.15	0.9249
0.8507	343.15	0.9648
0.8520	353.15	0.9568
0.8520	363.15	0.9588
0.9149	343.15	0.9851
0.9149	363.15	0.9832
0.9194	353.15	0.9832
0.9658	343.15	0.9960
0.9658	353.15	0.9951
0.9658	363.15	0.9951
0.9841	343.15	0.9969
0.9841	353.15	0.9996
0.9841	363.15	0.9969
1.0000	343.15	1.0000
1.0000	353.15	1.0000
1.0000	363.15	1.0000

Azeotropic composition: mole fraction of Cyclopentanone (1) [ref]

Temperature, K - Liquid	Azeotropic composition: mole fraction of Cyclopentanone (1) - Liquid
343.15	0.3038
353.15	0.2806
363.15	0.2746

Mole fraction of Cyclopentanone (1) [ref]

Fixed		Measured
Mole fraction of Cyclopentanone (1) - Liquid	Temperature, K - Gas	Mole fraction of Cyclopentanone (1) - Gas
0.0000	343.15	0.0000
0.0000	353.15	0.0000
0.0000	363.15	0.0000
0.0623	353.15	0.0497
0.0623	363.15	0.0522
0.0648	343.15	0.0497
0.1045	343.15	0.0748
0.1144	353.15	0.0848
0.1144	363.15	0.0897
0.1556	363.15	0.1314
0.1580	343.15	0.1266
0.1580	353.15	0.1266
0.2169	343.15	0.1889
0.2169	353.15	0.1959
0.2169	363.15	0.1959
0.2741	353.15	0.2786
0.2741	363.15	0.2853
0.2763	343.15	0.2718
0.3402	343.15	0.3892
0.3440	363.15	0.3912
0.3446	353.15	0.3892
0.4222	343.15	0.5284
0.4222	353.15	0.5284
0.4243	363.15	0.5208
0.4803	343.15	0.6260
0.4803	363.15	0.6225
0.4842	353.15	0.6225
0.5527	343.15	0.7244
0.5527	363.15	0.7244
0.5582	353.15	0.7244
0.6260	343.15	0.8093
0.6260	353.15	0.8107
0.6260	363.15	0.8079
0.6927	363.15	0.8659
0.6943	353.15	0.8709
0.6960	343.15	0.8796
0.7695	343.15	0.9312
0.7753	353.15	0.9238
0.7783	363.15	0.9249
0.8507	343.15	0.9648
0.8520	353.15	0.9568
0.8520	363.15	0.9588
0.9149	343.15	0.9851
0.9149	363.15	0.9832
0.9194	353.15	0.9832
0.9658	343.15	0.9960
0.9658	353.15	0.9951
0.9658	363.15	0.9951
0.9841	343.15	0.9969
0.9841	353.15	0.9996
0.9841	363.15	0.9969
1.0000	343.15	1.0000
1.0000	353.15	1.0000
1.0000	363.15	1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Cyclopentanone (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	343.15	7.24
0.0000	353.15	11.23
0.0000	363.15	16.65
0.0623	353.15	10.67
0.0623	363.15	16.13
0.0648	343.15	7.17
0.1045	343.15	6.97
0.1144	353.15	10.40
0.1144	363.15	15.74
0.1556	363.15	15.60
0.1580	343.15	6.75
0.1580	353.15	10.32
0.2169	343.15	6.63
0.2169	353.15	10.17
0.2169	363.15	15.38
0.2741	353.15	10.18
0.2741	363.15	15.36
0.2763	343.15	6.56
0.3402	343.15	6.64
0.3440	363.15	15.53
0.3446	353.15	10.23
0.4222	343.15	6.79
0.4222	353.15	10.49
0.4243	363.15	15.97
0.4803	343.15	7.08
0.4803	363.15	16.58
0.4842	353.15	10.92
0.5527	343.15	7.52
0.5527	363.15	17.62
0.5582	353.15	11.69
0.6260	343.15	8.16
0.6260	353.15	12.53
0.6260	363.15	18.80
0.6927	363.15	20.16
0.6943	353.15	13.44
0.6960	343.15	8.80
0.7695	343.15	9.72
0.7753	353.15	14.78
0.7783	363.15	22.21
0.8507	343.15	10.73
0.8520	353.15	16.26
0.8520	363.15	24.09
0.9149	343.15	11.85
0.9149	363.15	26.08
0.9194	353.15	17.72
0.9658	343.15	12.56
0.9658	353.15	18.88
0.9658	363.15	27.81
0.9841	343.15	12.83
0.9841	353.15	19.20
0.9841	363.15	28.40
1.0000	343.15	13.03
1.0000	353.15	19.61
1.0000	363.15	28.61

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Cyclopentanone (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	343.15	7.24
0.0000	353.15	11.23
0.0000	363.15	16.65
0.0623	353.15	10.67
0.0623	363.15	16.13
0.0648	343.15	7.17
0.1045	343.15	6.97
0.1144	353.15	10.40
0.1144	363.15	15.74
0.1556	363.15	15.60
0.1580	343.15	6.75
0.1580	353.15	10.32
0.2169	343.15	6.63
0.2169	353.15	10.17
0.2169	363.15	15.38
0.2741	353.15	10.18
0.2741	363.15	15.36
0.2763	343.15	6.56
0.3402	343.15	6.64
0.3440	363.15	15.53
0.3446	353.15	10.23
0.4222	343.15	6.79
0.4222	353.15	10.49
0.4243	363.15	15.97
0.4803	343.15	7.08
0.4803	363.15	16.58
0.4842	353.15	10.92
0.5527	343.15	7.52
0.5527	363.15	17.62
0.5582	353.15	11.69
0.6260	343.15	8.16
0.6260	353.15	12.53
0.6260	363.15	18.80
0.6927	363.15	20.16
0.6943	353.15	13.44
0.6960	343.15	8.80
0.7695	343.15	9.72
0.7753	353.15	14.78
0.7783	363.15	22.21
0.8507	343.15	10.73
0.8520	353.15	16.26
0.8520	363.15	24.09
0.9149	343.15	11.85
0.9149	363.15	26.08
0.9194	353.15	17.72
0.9658	343.15	12.56
0.9658	353.15	18.88
0.9658	363.15	27.81
0.9841	343.15	12.83
0.9841	353.15	19.20
0.9841	363.15	28.40
1.0000	343.15	13.03
1.0000	353.15	19.61
1.0000	363.15	28.61

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,1,2,2-tetrachloro- (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	953.99
288.15	0.1209	1047.22
288.15	0.2041	1109.07
288.15	0.3218	1193.26
288.15	0.4139	1256.69
288.15	0.5120	1321.38
288.15	0.6132	1385.46
288.15	0.7097	1443.91
288.15	0.7901	1490.55
288.15	0.9004	1551.95
288.15	1.0000	1604.78
298.15	0.0000	944.35
298.15	0.1209	1036.91
298.15	0.2041	1098.28
298.15	0.3218	1181.79
298.15	0.4139	1244.71
298.15	0.5120	1308.82
298.15	0.6132	1372.29
298.15	0.7097	1430.16
298.15	0.7901	1476.32
298.15	0.9004	1537.02
298.15	1.0000	1589.19
308.15	0.0000	934.69
308.15	0.1209	1026.54
308.15	0.2041	1087.44
308.15	0.3218	1170.29
308.15	0.4139	1232.66
308.15	0.5120	1296.19
308.15	0.6132	1359.06
308.15	0.7097	1416.37
308.15	0.7901	1462.03
308.15	0.9004	1522.06
308.15	1.0000	1573.59
318.15	0.0000	924.99
318.15	0.1209	1016.11
318.15	0.2041	1076.53
318.15	0.3218	1158.7
318.15	0.4139	1220.54
318.15	0.5120	1283.5
318.15	0.6132	1345.77
318.15	0.7097	1402.5
318.15	0.7901	1447.69
318.15	0.9004	1507.05
318.15	1.0000	1557.95

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,1,2,2-tetrachloro- (2) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0000	953.99
288.15	0.1209	1047.22
288.15	0.2041	1109.07
288.15	0.3218	1193.26
288.15	0.4139	1256.69
288.15	0.5120	1321.38
288.15	0.6132	1385.46
288.15	0.7097	1443.91
288.15	0.7901	1490.55
288.15	0.9004	1551.95
288.15	1.0000	1604.78
298.15	0.0000	944.35
298.15	0.1209	1036.91
298.15	0.2041	1098.28
298.15	0.3218	1181.79
298.15	0.4139	1244.71
298.15	0.5120	1308.82
298.15	0.6132	1372.29
298.15	0.7097	1430.16
298.15	0.7901	1476.32
298.15	0.9004	1537.02
298.15	1.0000	1589.19
308.15	0.0000	934.69
308.15	0.1209	1026.54
308.15	0.2041	1087.44
308.15	0.3218	1170.29
308.15	0.4139	1232.66
308.15	0.5120	1296.19
308.15	0.6132	1359.06
308.15	0.7097	1416.37
308.15	0.7901	1462.03
308.15	0.9004	1522.06
308.15	1.0000	1573.59
318.15	0.0000	924.99
318.15	0.1209	1016.11
318.15	0.2041	1076.53
318.15	0.3218	1158.7
318.15	0.4139	1220.54
318.15	0.5120	1283.5
318.15	0.6132	1345.77
318.15	0.7097	1402.5
318.15	0.7901	1447.69
318.15	0.9004	1507.05
318.15	1.0000	1557.95

Azeotropic pressure, kPa [ref]

Temperature, K - Liquid	Azeotropic pressure, kPa - Liquid
343.15	6.54
353.15	10.07
363.15	15.27

Azeotropic pressure, kPa [ref]

Temperature, K - Liquid	Azeotropic pressure, kPa - Liquid
343.15	6.54
353.15	10.07
363.15	15.27

Sources

• Isothermal (vapour + liquid) equilibria for the binary (cyclopentanone or cyclohexanone with 1,1,2,2-tetrachloroethane) systems at temperatures of (343.15, 353.15, and 363.15) 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