Mixture of 1,3-Dioxolane + 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 1,3-Dioxolane (1) [ref]

Fixed		Measured
Mole fraction of 1,3-Dioxolane (1) - Liquid	Pressure, kPa - Gas	Mole fraction of 1,3-Dioxolane (1) - Gas
0.0305	40.00	0.2200
0.0350	101.33	0.2003
0.0730	40.00	0.4500
0.0825	101.33	0.3848
0.1474	101.33	0.5697
0.1489	40.00	0.6224
0.1868	40.00	0.6814
0.2232	101.33	0.6743
0.2654	101.33	0.7123
0.2708	40.00	0.7711
0.3529	40.00	0.8194
0.3581	101.33	0.7954
0.4342	101.33	0.8428
0.4405	40.00	0.8672
0.4846	40.00	0.8834
0.4971	101.33	0.8639
0.5894	101.33	0.8992
0.5953	40.00	0.9144
0.6298	40.00	0.9214
0.6395	101.33	0.9131
0.7027	40.00	0.9390
0.7040	101.33	0.9278
0.7651	101.33	0.9434
0.7701	40.00	0.9494
0.8058	101.33	0.9527
0.8078	40.00	0.9577
0.8424	101.33	0.9604
0.8683	101.33	0.9657
0.8687	40.00	0.9690
0.8990	40.00	0.9762

Mole fraction of 1,3-Dioxolane (1) [ref]

Fixed		Measured
Mole fraction of 1,3-Dioxolane (1) - Liquid	Temperature, K - Gas	Mole fraction of 1,3-Dioxolane (1) - Gas
0.0115	328.15	0.1240
0.0160	298.15	0.2263
0.0239	328.15	0.2398
0.0340	298.15	0.3882
0.0492	328.15	0.3868
0.0680	298.15	0.5488
0.0969	298.15	0.6373
0.1055	328.15	0.5917
0.1239	298.15	0.6965
0.1468	298.15	0.7267
0.1794	328.15	0.7071
0.1924	298.15	0.7841
0.2272	328.15	0.7570
0.2932	328.15	0.8125
0.2988	298.15	0.8543
0.3588	298.15	0.8765
0.3719	328.15	0.8469
0.4029	298.15	0.8889
0.4096	328.15	0.8676
0.4682	298.15	0.9090
0.4843	328.15	0.8921
0.5566	298.15	0.9264
0.5611	328.15	0.9123
0.6450	298.15	0.9432
0.6504	328.15	0.9309
0.7240	328.15	0.9458
0.7277	298.15	0.9554
0.8203	298.15	0.9678
0.8232	328.15	0.9627
0.9222	298.15	0.9840
0.9241	328.15	0.9818

Mole fraction of 1,3-Dioxolane (1) [ref]

Fixed		Measured
Mole fraction of 1,3-Dioxolane (1) - Liquid	Pressure, kPa - Gas	Mole fraction of 1,3-Dioxolane (1) - Gas
0.0305	40.00	0.2200
0.0350	101.33	0.2003
0.0730	40.00	0.4500
0.0825	101.33	0.3848
0.1474	101.33	0.5697
0.1489	40.00	0.6224
0.1868	40.00	0.6814
0.2232	101.33	0.6743
0.2654	101.33	0.7123
0.2708	40.00	0.7711
0.3529	40.00	0.8194
0.3581	101.33	0.7954
0.4342	101.33	0.8428
0.4405	40.00	0.8672
0.4846	40.00	0.8834
0.4971	101.33	0.8639
0.5894	101.33	0.8992
0.5953	40.00	0.9144
0.6298	40.00	0.9214
0.6395	101.33	0.9131
0.7027	40.00	0.9390
0.7040	101.33	0.9278
0.7651	101.33	0.9434
0.7701	40.00	0.9494
0.8058	101.33	0.9527
0.8078	40.00	0.9577
0.8424	101.33	0.9604
0.8683	101.33	0.9657
0.8687	40.00	0.9690
0.8990	40.00	0.9762

Mole fraction of 1,3-Dioxolane (1) [ref]

Fixed		Measured
Mole fraction of 1,3-Dioxolane (1) - Liquid	Temperature, K - Gas	Mole fraction of 1,3-Dioxolane (1) - Gas
0.0115	328.15	0.1240
0.0160	298.15	0.2263
0.0239	328.15	0.2398
0.0340	298.15	0.3882
0.0492	328.15	0.3868
0.0680	298.15	0.5488
0.0969	298.15	0.6373
0.1055	328.15	0.5917
0.1239	298.15	0.6965
0.1468	298.15	0.7267
0.1794	328.15	0.7071
0.1924	298.15	0.7841
0.2272	328.15	0.7570
0.2932	328.15	0.8125
0.2988	298.15	0.8543
0.3588	298.15	0.8765
0.3719	328.15	0.8469
0.4029	298.15	0.8889
0.4096	328.15	0.8676
0.4682	298.15	0.9090
0.4843	328.15	0.8921
0.5566	298.15	0.9264
0.5611	328.15	0.9123
0.6450	298.15	0.9432
0.6504	328.15	0.9309
0.7240	328.15	0.9458
0.7277	298.15	0.9554
0.8203	298.15	0.9678
0.8232	328.15	0.9627
0.9222	298.15	0.9840
0.9241	328.15	0.9818

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,3-Dioxolane (1) - Liquid	Kinematic viscosity, m2/s - Liquid
283.15	0.0000	9.4780e-07
283.15	0.0584	9.3010e-07
283.15	0.1044	9.1650e-07
283.15	0.2045	8.8810e-07
283.15	0.3055	8.5910e-07
283.15	0.4039	8.3150e-07
283.15	0.5020	8.0390e-07
283.15	0.6018	7.7550e-07
283.15	0.7009	7.4620e-07
283.15	0.8019	7.1610e-07
283.15	0.9017	6.8500e-07
283.15	0.9507	6.6900e-07
283.15	1.0000	6.5290e-07
298.15	0.0000	7.9480e-07
298.15	0.0584	7.8120e-07
298.15	0.1044	7.7320e-07
298.15	0.2045	7.4940e-07
298.15	0.3055	7.2610e-07
298.15	0.4039	7.0360e-07
298.15	0.5020	6.8050e-07
298.15	0.6018	6.5650e-07
298.15	0.7009	6.3280e-07
298.15	0.8019	6.0880e-07
298.15	0.9017	5.8290e-07
298.15	0.9507	5.6780e-07
298.15	1.0000	5.5590e-07
313.15	0.0000	6.7660e-07
313.15	0.0584	6.6540e-07
313.15	0.1044	6.5880e-07
313.15	0.2045	6.3940e-07
313.15	0.3055	6.2050e-07
313.15	0.4039	6.0180e-07
313.15	0.5020	5.8290e-07
313.15	0.6018	5.6290e-07
313.15	0.7009	5.4370e-07
313.15	0.8019	5.2310e-07
313.15	0.9017	5.0160e-07
313.15	0.9507	4.8880e-07
313.15	1.0000	4.7840e-07

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,3-Dioxolane (1) - Liquid	Kinematic viscosity, m2/s - Liquid
283.15	0.0000	9.4780e-07
283.15	0.0584	9.3010e-07
283.15	0.1044	9.1650e-07
283.15	0.2045	8.8810e-07
283.15	0.3055	8.5910e-07
283.15	0.4039	8.3150e-07
283.15	0.5020	8.0390e-07
283.15	0.6018	7.7550e-07
283.15	0.7009	7.4620e-07
283.15	0.8019	7.1610e-07
283.15	0.9017	6.8500e-07
283.15	0.9507	6.6900e-07
283.15	1.0000	6.5290e-07
298.15	0.0000	7.9480e-07
298.15	0.0584	7.8120e-07
298.15	0.1044	7.7320e-07
298.15	0.2045	7.4940e-07
298.15	0.3055	7.2610e-07
298.15	0.4039	7.0360e-07
298.15	0.5020	6.8050e-07
298.15	0.6018	6.5650e-07
298.15	0.7009	6.3280e-07
298.15	0.8019	6.0880e-07
298.15	0.9017	5.8290e-07
298.15	0.9507	5.6780e-07
298.15	1.0000	5.5590e-07
313.15	0.0000	6.7660e-07
313.15	0.0584	6.6540e-07
313.15	0.1044	6.5880e-07
313.15	0.2045	6.3940e-07
313.15	0.3055	6.2050e-07
313.15	0.4039	6.0180e-07
313.15	0.5020	5.8290e-07
313.15	0.6018	5.6290e-07
313.15	0.7009	5.4370e-07
313.15	0.8019	5.2310e-07
313.15	0.9017	5.0160e-07
313.15	0.9507	4.8880e-07
313.15	1.0000	4.7840e-07

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of 1,3-Dioxolane (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0115	328.15	6.91
0.0160	298.15	1.58
0.0239	328.15	7.74
0.0340	298.15	2.00
0.0492	328.15	9.70
0.0680	298.15	2.70
0.0969	298.15	3.17
0.1055	328.15	13.48
0.1239	298.15	3.88
0.1468	298.15	4.21
0.1794	328.15	17.77
0.1924	298.15	5.12
0.2272	328.15	20.43
0.2932	328.15	23.83
0.2988	298.15	6.80
0.3588	298.15	7.38
0.3719	328.15	27.29
0.4029	298.15	7.94
0.4096	328.15	29.02
0.4682	298.15	8.85
0.4843	328.15	32.02
0.5566	298.15	9.77
0.5611	328.15	34.71
0.6450	298.15	10.47
0.6504	328.15	37.67
0.7240	328.15	39.95
0.7277	298.15	11.22
0.8203	298.15	11.91
0.8232	328.15	43.20
0.9222	298.15	12.80
0.9241	328.15	46.49

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of 1,3-Dioxolane (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0115	328.15	6.91
0.0160	298.15	1.58
0.0239	328.15	7.74
0.0340	298.15	2.00
0.0492	328.15	9.70
0.0680	298.15	2.70
0.0969	298.15	3.17
0.1055	328.15	13.48
0.1239	298.15	3.88
0.1468	298.15	4.21
0.1794	328.15	17.77
0.1924	298.15	5.12
0.2272	328.15	20.43
0.2932	328.15	23.83
0.2988	298.15	6.80
0.3588	298.15	7.38
0.3719	328.15	27.29
0.4029	298.15	7.94
0.4096	328.15	29.02
0.4682	298.15	8.85
0.4843	328.15	32.02
0.5566	298.15	9.77
0.5611	328.15	34.71
0.6450	298.15	10.47
0.6504	328.15	37.67
0.7240	328.15	39.95
0.7277	298.15	11.22
0.8203	298.15	11.91
0.8232	328.15	43.20
0.9222	298.15	12.80
0.9241	328.15	46.49

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,3-Dioxolane (1) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	887.11
283.15	0.0584	892.59
283.15	0.1044	896.89
283.15	0.2045	907.33
283.15	0.3055	919.33
283.15	0.4039	932.65
283.15	0.5020	948.0
283.15	0.6018	965.83
283.15	0.7009	986.87
283.15	0.8019	1012.01
283.15	0.9017	1041.75
283.15	0.9507	1058.59
283.15	1.0000	1077.65
298.15	0.0000	873.55
298.15	0.0578	878.52
298.15	0.0916	881.66
298.15	0.1946	891.91
298.15	0.2978	903.59
298.15	0.3974	916.57
298.15	0.4980	931.67
298.15	0.6013	949.73
298.15	0.7003	969.97
298.15	0.8003	994.09
298.15	0.9018	1023.67
298.15	0.9565	1042.27
298.15	1.0000	1058.64
313.15	0.0000	859.0
313.15	0.0578	864.14
313.15	0.0916	867.18
313.15	0.1946	877.07
313.15	0.2978	888.32
313.15	0.3974	900.8
313.15	0.4980	915.42
313.15	0.6013	933.03
313.15	0.7003	952.92
313.15	0.8003	976.49
313.15	0.9018	1005.38
313.15	0.9565	1023.53
313.15	1.0000	1039.92

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,3-Dioxolane (1) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	887.11
283.15	0.0584	892.59
283.15	0.1044	896.89
283.15	0.2045	907.33
283.15	0.3055	919.33
283.15	0.4039	932.65
283.15	0.5020	948.0
283.15	0.6018	965.83
283.15	0.7009	986.87
283.15	0.8019	1012.01
283.15	0.9017	1041.75
283.15	0.9507	1058.59
283.15	1.0000	1077.65
298.15	0.0000	873.55
298.15	0.0578	878.52
298.15	0.0916	881.66
298.15	0.1946	891.91
298.15	0.2978	903.59
298.15	0.3974	916.57
298.15	0.4980	931.67
298.15	0.6013	949.73
298.15	0.7003	969.97
298.15	0.8003	994.09
298.15	0.9018	1023.67
298.15	0.9565	1042.27
298.15	1.0000	1058.64
313.15	0.0000	859.0
313.15	0.0578	864.14
313.15	0.0916	867.18
313.15	0.1946	877.07
313.15	0.2978	888.32
313.15	0.3974	900.8
313.15	0.4980	915.42
313.15	0.6013	933.03
313.15	0.7003	952.92
313.15	0.8003	976.49
313.15	0.9018	1005.38
313.15	0.9565	1023.53
313.15	1.0000	1039.92

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of 1,3-Dioxolane (1) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0305	40.00	370.20
0.0350	101.33	401.15
0.0730	40.00	362.50
0.0825	101.33	393.58
0.1474	101.33	384.66
0.1489	40.00	353.92
0.1868	40.00	350.16
0.2232	101.33	377.11
0.2654	101.33	374.94
0.2708	40.00	344.64
0.3529	40.00	340.21
0.3581	101.33	368.74
0.4342	101.33	364.46
0.4405	40.00	336.08
0.4846	40.00	334.55
0.4971	101.33	362.15
0.5894	101.33	358.95
0.5953	40.00	331.49
0.6298	40.00	330.71
0.6395	101.33	357.35
0.7027	40.00	329.04
0.7040	101.33	355.76
0.7651	101.33	354.14
0.7701	40.00	327.83
0.8058	101.33	353.19
0.8078	40.00	327.14
0.8424	101.33	352.47
0.8683	101.33	351.84
0.8687	40.00	325.86
0.8990	40.00	325.26
1.0000	101.33	348.80

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of 1,3-Dioxolane (1) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0305	40.00	370.20
0.0350	101.33	401.15
0.0730	40.00	362.50
0.0825	101.33	393.58
0.1474	101.33	384.66
0.1489	40.00	353.92
0.1868	40.00	350.16
0.2232	101.33	377.11
0.2654	101.33	374.94
0.2708	40.00	344.64
0.3529	40.00	340.21
0.3581	101.33	368.74
0.4342	101.33	364.46
0.4405	40.00	336.08
0.4846	40.00	334.55
0.4971	101.33	362.15
0.5894	101.33	358.95
0.5953	40.00	331.49
0.6298	40.00	330.71
0.6395	101.33	357.35
0.7027	40.00	329.04
0.7040	101.33	355.76
0.7651	101.33	354.14
0.7701	40.00	327.83
0.8058	101.33	353.19
0.8078	40.00	327.14
0.8424	101.33	352.47
0.8683	101.33	351.84
0.8687	40.00	325.86
0.8990	40.00	325.26
1.0000	101.33	348.80

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