Mixture of n-Propyl chloride + 1,4-Dioxane

Datasets

1. Mole fraction (6)
2. n₀ - Refractive index (Na D-line) (2)
3. ρ_l - Mass density, kg/m3 (2)
4. T_boil - Boiling temperature at pressure P, K (6)

Mole fraction of 1,4-Dioxane (2) [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of 1,4-Dioxane (2) - Liquid	Mole fraction of 1,4-Dioxane (2) - Gas
0.0603	0.0132
0.2873	0.0556
0.3442	0.0709
0.4055	0.0926
0.5428	0.1350
0.6056	0.1635
0.7480	0.2653
0.8146	0.3517
0.8867	0.4882
0.9366	0.6456
0.9700	0.8041

Mole fraction of 1,4-Dioxane (2) [ref]

Operational condition: Pressure, kPa = 70 (Liquid)

Mole fraction of 1,4-Dioxane (2) - Liquid	Mole fraction of 1,4-Dioxane (2) - Gas
0.0576	0.0185
0.2720	0.0620
0.3347	0.0780
0.4141	0.0992
0.5240	0.1407
0.6012	0.1852
0.7287	0.2716
0.8100	0.3683
0.8929	0.5310
0.9347	0.6568
0.9701	0.8216

Mole fraction of 1,4-Dioxane (2) [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of 1,4-Dioxane (2) - Liquid	Mole fraction of 1,4-Dioxane (2) - Gas
0.0525	0.0194
0.2590	0.0603
0.3275	0.0800
0.4010	0.1041
0.5106	0.1325
0.6077	0.2032
0.6984	0.2629
0.7891	0.3529
0.8809	0.5262
0.9427	0.7068
0.9702	0.8310

Mole fraction of 1,4-Dioxane (2) [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of 1,4-Dioxane (2) - Liquid	Mole fraction of 1,4-Dioxane (2) - Gas
0.0603	0.0132
0.2873	0.0556
0.3442	0.0709
0.4055	0.0926
0.5428	0.1350
0.6056	0.1635
0.7480	0.2653
0.8146	0.3517
0.8867	0.4882
0.9366	0.6456
0.9700	0.8041

Mole fraction of 1,4-Dioxane (2) [ref]

Operational condition: Pressure, kPa = 70 (Liquid)

Mole fraction of 1,4-Dioxane (2) - Liquid	Mole fraction of 1,4-Dioxane (2) - Gas
0.0576	0.0185
0.2720	0.0620
0.3347	0.0780
0.4141	0.0992
0.5240	0.1407
0.6012	0.1852
0.7287	0.2716
0.8100	0.3683
0.8929	0.5310
0.9347	0.6568
0.9701	0.8216

Mole fraction of 1,4-Dioxane (2) [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of 1,4-Dioxane (2) - Liquid	Mole fraction of 1,4-Dioxane (2) - Gas
0.0525	0.0194
0.2590	0.0603
0.3275	0.0800
0.4010	0.1041
0.5106	0.1325
0.6077	0.2032
0.6984	0.2629
0.7891	0.3529
0.8809	0.5262
0.9427	0.7068
0.9702	0.8310

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Refractive index (Na D-line) - Liquid
298.15	0.0000	1.3856
298.15	0.1027	1.3892
298.15	0.2077	1.3928
298.15	0.3029	1.3961
298.15	0.4034	1.3996
298.15	0.5060	1.4031
298.15	0.6062	1.4065
298.15	0.7060	1.4099
298.15	0.8081	1.4134
298.15	0.9059	1.4167
298.15	0.9486	1.4182
298.15	1.0000	1.4199
313.15	0.0000	1.3767
313.15	0.1009	1.3805
313.15	0.2026	1.3843
313.15	0.3067	1.3881
313.15	0.4061	1.3917
313.15	0.5056	1.3952
313.15	0.6044	1.3987
313.15	0.7114	1.4025
313.15	0.8026	1.4058
313.15	0.9011	1.4092
313.15	0.9510	1.411
313.15	1.0000	1.4126

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Refractive index (Na D-line) - Liquid
298.15	0.0000	1.3856
298.15	0.1027	1.3892
298.15	0.2077	1.3928
298.15	0.3029	1.3961
298.15	0.4034	1.3996
298.15	0.5060	1.4031
298.15	0.6062	1.4065
298.15	0.7060	1.4099
298.15	0.8081	1.4134
298.15	0.9059	1.4167
298.15	0.9486	1.4182
298.15	1.0000	1.4199
313.15	0.0000	1.3767
313.15	0.1009	1.3805
313.15	0.2026	1.3843
313.15	0.3067	1.3881
313.15	0.4061	1.3917
313.15	0.5056	1.3952
313.15	0.6044	1.3987
313.15	0.7114	1.4025
313.15	0.8026	1.4058
313.15	0.9011	1.4092
313.15	0.9510	1.411
313.15	1.0000	1.4126

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	884.26
298.15	0.1027	898.64
298.15	0.2077	913.41
298.15	0.3029	926.89
298.15	0.4034	941.19
298.15	0.5060	955.87
298.15	0.6062	970.28
298.15	0.7060	984.73
298.15	0.8081	999.6
298.15	0.9059	1013.96
298.15	0.9486	1020.26
298.15	1.0000	1027.87
313.15	0.0000	865.14
313.15	0.1009	879.74
313.15	0.2026	894.27
313.15	0.3067	909.2
313.15	0.4061	923.53
313.15	0.5056	937.97
313.15	0.6044	952.38
313.15	0.7114	968.04
313.15	0.8026	981.42
313.15	0.9011	995.98
313.15	0.9510	1003.38
313.15	1.0000	1010.69

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,4-Dioxane (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	884.26
298.15	0.1027	898.64
298.15	0.2077	913.41
298.15	0.3029	926.89
298.15	0.4034	941.19
298.15	0.5060	955.87
298.15	0.6062	970.28
298.15	0.7060	984.73
298.15	0.8081	999.6
298.15	0.9059	1013.96
298.15	0.9486	1020.26
298.15	1.0000	1027.87
313.15	0.0000	865.14
313.15	0.1009	879.74
313.15	0.2026	894.27
313.15	0.3067	909.2
313.15	0.4061	923.53
313.15	0.5056	937.97
313.15	0.6044	952.38
313.15	0.7114	968.04
313.15	0.8026	981.42
313.15	0.9011	995.98
313.15	0.9510	1003.38
313.15	1.0000	1010.69

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of 1,4-Dioxane (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0603	296.32
0.2873	301.75
0.3442	303.03
0.4055	304.90
0.5428	310.63
0.6056	311.89
0.7480	319.93
0.8146	324.56
0.8867	330.52
0.9366	336.51
0.9700	341.47

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 70 (Liquid)

Mole fraction of 1,4-Dioxane (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0576	310.95
0.2720	316.34
0.3347	317.68
0.4141	320.55
0.5240	324.63
0.6012	327.95
0.7287	334.58
0.8100	340.26
0.8929	347.83
0.9347	352.39
0.9701	357.74

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of 1,4-Dioxane (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0525	321.39
0.2590	326.97
0.3275	328.86
0.4010	330.82
0.5106	334.70
0.6077	339.78
0.6984	343.71
0.7891	349.81
0.8809	358.16
0.9427	365.22
0.9702	369.37

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of 1,4-Dioxane (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0603	296.32
0.2873	301.75
0.3442	303.03
0.4055	304.90
0.5428	310.63
0.6056	311.89
0.7480	319.93
0.8146	324.56
0.8867	330.52
0.9366	336.51
0.9700	341.47

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 70 (Liquid)

Mole fraction of 1,4-Dioxane (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0576	310.95
0.2720	316.34
0.3347	317.68
0.4141	320.55
0.5240	324.63
0.6012	327.95
0.7287	334.58
0.8100	340.26
0.8929	347.83
0.9347	352.39
0.9701	357.74

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of 1,4-Dioxane (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0525	321.39
0.2590	326.97
0.3275	328.86
0.4010	330.82
0.5106	334.70
0.6077	339.78
0.6984	343.71
0.7891	349.81
0.8809	358.16
0.9427	365.22
0.9702	369.37

Sources

• Study of isobaric vapour liquid equilibrium of some cyclic ethers with 1-chloropropane: Experimental results and SAFT-VR modelling
• Volumetric and refractive properties of binary mixtures containing 1,4-dioxane and chloroalkanes