Mixture of Tetrahydropyran + Hexane, 1-chloro-

Datasets

1. Mole fraction (4)
2. ν - Kinematic viscosity, m2/s (2)
3. P_vap - Vapor or sublimation pressure, kPa (2)
4. ρ_l - Mass density, kg/m3 (2)
5. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of Tetrahydropyran (1) [ref]

Fixed		Measured
Mole fraction of Tetrahydropyran (1) - Liquid	Pressure, kPa - Gas	Mole fraction of Tetrahydropyran (1) - Gas
0.0551	101.33	0.1359
0.0598	40.00	0.1653
0.0970	40.00	0.2695
0.1047	101.33	0.2301
0.1378	40.00	0.3503
0.1378	101.33	0.3293
0.1819	101.33	0.4117
0.1891	40.00	0.4634
0.2384	40.00	0.5360
0.2398	101.33	0.5053
0.2618	101.33	0.5438
0.2686	40.00	0.5851
0.3375	40.00	0.6811
0.3400	101.33	0.6405
0.3882	40.00	0.7355
0.3919	101.33	0.6999
0.4670	40.00	0.8039
0.4693	101.33	0.7717
0.5449	101.33	0.8248
0.5483	40.00	0.8576
0.6301	101.33	0.8772
0.6395	40.00	0.8973
0.7155	101.33	0.9147
0.7164	40.00	0.9342
0.8004	101.33	0.9528
0.8074	40.00	0.9668
0.8748	101.33	0.9785
0.8805	40.00	0.9805
0.9505	40.00	0.9900
0.9513	101.33	0.9909

Mole fraction of Tetrahydropyran (1) [ref]

Fixed		Measured
Mole fraction of Tetrahydropyran (1) - Liquid	Temperature, K - Gas	Mole fraction of Tetrahydropyran (1) - Gas
0.0598	298.15	0.2476
0.0614	328.15	0.2008
0.1108	298.15	0.4182
0.1153	328.15	0.3532
0.1527	328.15	0.4499
0.1630	298.15	0.5479
0.2147	298.15	0.6320
0.2175	328.15	0.5793
0.2754	328.15	0.6487
0.2835	298.15	0.7293
0.3323	298.15	0.7708
0.3554	328.15	0.7393
0.4129	328.15	0.7907
0.4227	298.15	0.8384
0.4480	298.15	0.8658
0.4775	328.15	0.8451
0.5019	298.15	0.8797
0.5382	328.15	0.8707
0.5505	298.15	0.9068
0.6080	298.15	0.9303
0.6165	328.15	0.9100
0.7009	328.15	0.9443
0.7048	298.15	0.9591
0.7598	328.15	0.9606
0.7654	298.15	0.9770
0.8576	298.15	0.9850
0.8576	328.15	0.9827
0.9036	298.15	0.9900
0.9044	328.15	0.9890

Mole fraction of Tetrahydropyran (1) [ref]

Fixed		Measured
Mole fraction of Tetrahydropyran (1) - Liquid	Pressure, kPa - Gas	Mole fraction of Tetrahydropyran (1) - Gas
0.0551	101.33	0.1359
0.0598	40.00	0.1653
0.0970	40.00	0.2695
0.1047	101.33	0.2301
0.1378	40.00	0.3503
0.1378	101.33	0.3293
0.1819	101.33	0.4117
0.1891	40.00	0.4634
0.2384	40.00	0.5360
0.2398	101.33	0.5053
0.2618	101.33	0.5438
0.2686	40.00	0.5851
0.3375	40.00	0.6811
0.3400	101.33	0.6405
0.3882	40.00	0.7355
0.3919	101.33	0.6999
0.4670	40.00	0.8039
0.4693	101.33	0.7717
0.5449	101.33	0.8248
0.5483	40.00	0.8576
0.6301	101.33	0.8772
0.6395	40.00	0.8973
0.7155	101.33	0.9147
0.7164	40.00	0.9342
0.8004	101.33	0.9528
0.8074	40.00	0.9668
0.8748	101.33	0.9785
0.8805	40.00	0.9805
0.9505	40.00	0.9900
0.9513	101.33	0.9909

Mole fraction of Tetrahydropyran (1) [ref]

Fixed		Measured
Mole fraction of Tetrahydropyran (1) - Liquid	Temperature, K - Gas	Mole fraction of Tetrahydropyran (1) - Gas
0.0598	298.15	0.2476
0.0614	328.15	0.2008
0.1108	298.15	0.4182
0.1153	328.15	0.3532
0.1527	328.15	0.4499
0.1630	298.15	0.5479
0.2147	298.15	0.6320
0.2175	328.15	0.5793
0.2754	328.15	0.6487
0.2835	298.15	0.7293
0.3323	298.15	0.7708
0.3554	328.15	0.7393
0.4129	328.15	0.7907
0.4227	298.15	0.8384
0.4480	298.15	0.8658
0.4775	328.15	0.8451
0.5019	298.15	0.8797
0.5382	328.15	0.8707
0.5505	298.15	0.9068
0.6080	298.15	0.9303
0.6165	328.15	0.9100
0.7009	328.15	0.9443
0.7048	298.15	0.9591
0.7598	328.15	0.9606
0.7654	298.15	0.9770
0.8576	298.15	0.9850
0.8576	328.15	0.9827
0.9036	298.15	0.9900
0.9044	328.15	0.9890

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydropyran (1) - Liquid	Kinematic viscosity, m2/s - Liquid
283.15	0.0000	9.4780e-07
283.15	0.0501	9.5130e-07
283.15	0.1152	9.5730e-07
283.15	0.2090	9.6710e-07
283.15	0.2924	9.7640e-07
283.15	0.4074	9.9000e-07
283.15	0.4975	1.0009e-06
283.15	0.5988	1.0150e-06
283.15	0.6961	1.0313e-06
283.15	0.7996	1.0536e-06
283.15	0.8975	1.0815e-06
283.15	0.9493	1.0999e-06
283.15	1.0000	1.1205e-06
298.15	0.0000	7.9480e-07
298.15	0.0501	7.9790e-07
298.15	0.1152	8.0220e-07
298.15	0.2090	8.0800e-07
298.15	0.2924	8.1380e-07
298.15	0.4074	8.2250e-07
298.15	0.4975	8.3060e-07
298.15	0.5988	8.4000e-07
298.15	0.6961	8.5150e-07
298.15	0.7996	8.6620e-07
298.15	0.8975	8.8520e-07
298.15	0.9493	8.9630e-07
298.15	1.0000	9.1000e-07
313.15	0.0000	6.7660e-07
313.15	0.0501	6.7860e-07
313.15	0.1152	6.8170e-07
313.15	0.2090	6.8630e-07
313.15	0.2924	6.9060e-07
313.15	0.4074	6.9660e-07
313.15	0.4975	7.0230e-07
313.15	0.5988	7.0920e-07
313.15	0.6961	7.1680e-07
313.15	0.7996	7.2760e-07
313.15	0.8975	7.3970e-07
313.15	0.9493	7.4750e-07
313.15	1.0000	7.5710e-07

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydropyran (1) - Liquid	Kinematic viscosity, m2/s - Liquid
283.15	0.0000	9.4780e-07
283.15	0.0501	9.5130e-07
283.15	0.1152	9.5730e-07
283.15	0.2090	9.6710e-07
283.15	0.2924	9.7640e-07
283.15	0.4074	9.9000e-07
283.15	0.4975	1.0009e-06
283.15	0.5988	1.0150e-06
283.15	0.6961	1.0313e-06
283.15	0.7996	1.0536e-06
283.15	0.8975	1.0815e-06
283.15	0.9493	1.0999e-06
283.15	1.0000	1.1205e-06
298.15	0.0000	7.9480e-07
298.15	0.0501	7.9790e-07
298.15	0.1152	8.0220e-07
298.15	0.2090	8.0800e-07
298.15	0.2924	8.1380e-07
298.15	0.4074	8.2250e-07
298.15	0.4975	8.3060e-07
298.15	0.5988	8.4000e-07
298.15	0.6961	8.5150e-07
298.15	0.7996	8.6620e-07
298.15	0.8975	8.8520e-07
298.15	0.9493	8.9630e-07
298.15	1.0000	9.1000e-07
313.15	0.0000	6.7660e-07
313.15	0.0501	6.7860e-07
313.15	0.1152	6.8170e-07
313.15	0.2090	6.8630e-07
313.15	0.2924	6.9060e-07
313.15	0.4074	6.9660e-07
313.15	0.4975	7.0230e-07
313.15	0.5988	7.0920e-07
313.15	0.6961	7.1680e-07
313.15	0.7996	7.2760e-07
313.15	0.8975	7.3970e-07
313.15	0.9493	7.4750e-07
313.15	1.0000	7.5710e-07

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Tetrahydropyran (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0598	298.15	1.50
0.0614	328.15	7.00
0.1108	298.15	1.83
0.1153	328.15	8.22
0.1527	328.15	9.10
0.1630	298.15	2.23
0.2147	298.15	2.60
0.2175	328.15	10.80
0.2754	328.15	12.35
0.2835	298.15	3.21
0.3323	298.15	3.66
0.3554	328.15	14.60
0.4129	328.15	16.14
0.4227	298.15	4.33
0.4480	298.15	4.70
0.4775	328.15	18.21
0.5019	298.15	5.00
0.5382	328.15	19.89
0.5505	298.15	5.50
0.6080	298.15	6.04
0.6165	328.15	22.29
0.7009	328.15	25.00
0.7048	298.15	6.92
0.7598	328.15	26.75
0.7654	298.15	7.41
0.8576	298.15	8.17
0.8576	328.15	29.63
0.9036	298.15	8.63
0.9044	328.15	30.95

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Tetrahydropyran (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0598	298.15	1.50
0.0614	328.15	7.00
0.1108	298.15	1.83
0.1153	328.15	8.22
0.1527	328.15	9.10
0.1630	298.15	2.23
0.2147	298.15	2.60
0.2175	328.15	10.80
0.2754	328.15	12.35
0.2835	298.15	3.21
0.3323	298.15	3.66
0.3554	328.15	14.60
0.4129	328.15	16.14
0.4227	298.15	4.33
0.4480	298.15	4.70
0.4775	328.15	18.21
0.5019	298.15	5.00
0.5382	328.15	19.89
0.5505	298.15	5.50
0.6080	298.15	6.04
0.6165	328.15	22.29
0.7009	328.15	25.00
0.7048	298.15	6.92
0.7598	328.15	26.75
0.7654	298.15	7.41
0.8576	298.15	8.17
0.8576	328.15	29.63
0.9036	298.15	8.63
0.9044	328.15	30.95

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydropyran (1) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	887.11
283.15	0.0501	887.31
283.15	0.1152	887.6
283.15	0.2090	888.02
283.15	0.2924	888.37
283.15	0.4074	888.89
283.15	0.4975	889.4
283.15	0.5988	889.95
283.15	0.6961	890.62
283.15	0.7996	891.42
283.15	0.8975	892.37
283.15	0.9493	892.99
283.15	1.0000	893.62
298.15	0.0000	873.55
298.15	0.0501	873.67
298.15	0.1152	873.97
298.15	0.2090	874.26
298.15	0.2924	874.54
298.15	0.4074	875.02
298.15	0.4975	875.39
298.15	0.5988	875.83
298.15	0.6961	876.34
298.15	0.7996	876.93
298.15	0.8975	877.77
298.15	0.9493	878.28
298.15	1.0000	878.79
313.15	0.0000	859.0
313.15	0.0501	859.12
313.15	0.1152	859.32
313.15	0.2090	859.68
313.15	0.2924	859.83
313.15	0.4074	860.32
313.15	0.4975	860.6
313.15	0.5988	860.97
313.15	0.6961	861.47
313.15	0.7996	862.01
313.15	0.8975	862.78
313.15	0.9493	863.14
313.15	1.0000	863.69

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydropyran (1) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	887.11
283.15	0.0501	887.31
283.15	0.1152	887.6
283.15	0.2090	888.02
283.15	0.2924	888.37
283.15	0.4074	888.89
283.15	0.4975	889.4
283.15	0.5988	889.95
283.15	0.6961	890.62
283.15	0.7996	891.42
283.15	0.8975	892.37
283.15	0.9493	892.99
283.15	1.0000	893.62
298.15	0.0000	873.55
298.15	0.0501	873.67
298.15	0.1152	873.97
298.15	0.2090	874.26
298.15	0.2924	874.54
298.15	0.4074	875.02
298.15	0.4975	875.39
298.15	0.5988	875.83
298.15	0.6961	876.34
298.15	0.7996	876.93
298.15	0.8975	877.77
298.15	0.9493	878.28
298.15	1.0000	878.79
313.15	0.0000	859.0
313.15	0.0501	859.12
313.15	0.1152	859.32
313.15	0.2090	859.68
313.15	0.2924	859.83
313.15	0.4074	860.32
313.15	0.4975	860.6
313.15	0.5988	860.97
313.15	0.6961	861.47
313.15	0.7996	862.01
313.15	0.8975	862.78
313.15	0.9493	863.14
313.15	1.0000	863.69

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Tetrahydropyran (1) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0551	101.33	404.54
0.0598	40.00	373.55
0.0970	40.00	370.81
0.1047	101.33	402.25
0.1378	40.00	368.34
0.1378	101.33	399.31
0.1819	101.33	395.97
0.1891	40.00	364.72
0.2384	40.00	362.31
0.2398	101.33	392.31
0.2618	101.33	390.57
0.2686	40.00	360.02
0.3375	40.00	356.52
0.3400	101.33	387.04
0.3882	40.00	353.88
0.3919	101.33	384.62
0.4670	40.00	350.61
0.4693	101.33	380.49
0.5449	101.33	377.19
0.5483	40.00	347.17
0.6301	101.33	373.55
0.6395	40.00	344.15
0.7155	101.33	370.57
0.7164	40.00	341.44
0.8004	101.33	367.26
0.8074	40.00	338.51
0.8748	101.33	364.96
0.8805	40.00	336.62
0.9505	40.00	334.72
0.9513	101.33	362.73
1.0000	101.33	361.23

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Tetrahydropyran (1) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0551	101.33	404.54
0.0598	40.00	373.55
0.0970	40.00	370.81
0.1047	101.33	402.25
0.1378	40.00	368.34
0.1378	101.33	399.31
0.1819	101.33	395.97
0.1891	40.00	364.72
0.2384	40.00	362.31
0.2398	101.33	392.31
0.2618	101.33	390.57
0.2686	40.00	360.02
0.3375	40.00	356.52
0.3400	101.33	387.04
0.3882	40.00	353.88
0.3919	101.33	384.62
0.4670	40.00	350.61
0.4693	101.33	380.49
0.5449	101.33	377.19
0.5483	40.00	347.17
0.6301	101.33	373.55
0.6395	40.00	344.15
0.7155	101.33	370.57
0.7164	40.00	341.44
0.8004	101.33	367.26
0.8074	40.00	338.51
0.8748	101.33	364.96
0.8805	40.00	336.62
0.9505	40.00	334.72
0.9513	101.33	362.73
1.0000	101.33	361.23

Sources

• Vapour liquid equilibrium of cyclic ethers with 1-chlorohexane: Experimental results and UNIFAC predictions
• Isothermal (vapour + liquid) equilibrium of (cyclic ethers + chlorohexane) mixtures: Experimental results and SAFT modelling
• Experimental and predicted viscosities of binary mixtures of cyclic ethers with 1-chloropentane or 1-chlorohexane at 283.15, 298.15, and 313.15K