Mixture of 1,3-Dioxolane + n-Propyl chloride

Datasets

1. Mole fraction (6)
2. T_boil - Boiling temperature at pressure P, K (6)

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

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of 1,3-Dioxolane (1) - Liquid	Mole fraction of 1,3-Dioxolane (1) - Gas
0.0704	0.0401
0.1309	0.0676
0.2212	0.1156
0.3188	0.1594
0.4511	0.2120
0.5107	0.2532
0.6129	0.3150
0.7197	0.4186
0.7997	0.5044
0.9010	0.6935
0.9419	0.8052

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

Operational condition: Pressure, kPa = 70 (Liquid)

Mole fraction of 1,3-Dioxolane (1) - Liquid	Mole fraction of 1,3-Dioxolane (1) - Gas
0.0655	0.0376
0.1213	0.0676
0.2166	0.1158
0.3132	0.1648
0.4281	0.2238
0.5181	0.2766
0.6063	0.3429
0.6950	0.4168
0.8017	0.5419
0.9063	0.7218
0.9428	0.8188

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

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of 1,3-Dioxolane (1) - Liquid	Mole fraction of 1,3-Dioxolane (1) - Gas
0.0655	0.0455
0.1240	0.0732
0.2120	0.1178
0.3138	0.1715
0.4210	0.2335
0.5164	0.2912
0.6014	0.3534
0.6903	0.4352
0.7972	0.5570
0.8981	0.7228
0.9400	0.8163

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

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of 1,3-Dioxolane (1) - Liquid	Mole fraction of 1,3-Dioxolane (1) - Gas
0.0704	0.0401
0.1309	0.0676
0.2212	0.1156
0.3188	0.1594
0.4511	0.2120
0.5107	0.2532
0.6129	0.3150
0.7197	0.4186
0.7997	0.5044
0.9010	0.6935
0.9419	0.8052

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

Operational condition: Pressure, kPa = 70 (Liquid)

Mole fraction of 1,3-Dioxolane (1) - Liquid	Mole fraction of 1,3-Dioxolane (1) - Gas
0.0655	0.0376
0.1213	0.0676
0.2166	0.1158
0.3132	0.1648
0.4281	0.2238
0.5181	0.2766
0.6063	0.3429
0.6950	0.4168
0.8017	0.5419
0.9063	0.7218
0.9428	0.8188

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

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of 1,3-Dioxolane (1) - Liquid	Mole fraction of 1,3-Dioxolane (1) - Gas
0.0655	0.0455
0.1240	0.0732
0.2120	0.1178
0.3138	0.1715
0.4210	0.2335
0.5164	0.2912
0.6014	0.3534
0.6903	0.4352
0.7972	0.5570
0.8981	0.7228
0.9400	0.8163

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of 1,3-Dioxolane (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0704	295.92
0.1309	296.84
0.2212	298.04
0.3188	299.50
0.4511	301.75
0.5107	303.13
0.6129	305.25
0.7197	308.52
0.7997	311.18
0.9010	316.27
0.9419	318.48

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 70 (Liquid)

Mole fraction of 1,3-Dioxolane (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0655	310.21
0.1213	311.11
0.2166	312.22
0.3132	314.29
0.4281	316.41
0.5181	318.15
0.6063	320.28
0.6950	322.82
0.8017	326.35
0.9063	331.30
0.9428	333.66

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of 1,3-Dioxolane (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0655	320.93
0.1240	321.71
0.2120	323.00
0.3138	324.68
0.4210	326.81
0.5164	328.74
0.6014	330.79
0.6903	333.63
0.7972	337.27
0.8981	341.66
0.9400	344.27

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 40 (Liquid)

Mole fraction of 1,3-Dioxolane (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0704	295.92
0.1309	296.84
0.2212	298.04
0.3188	299.50
0.4511	301.75
0.5107	303.13
0.6129	305.25
0.7197	308.52
0.7997	311.18
0.9010	316.27
0.9419	318.48

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 70 (Liquid)

Mole fraction of 1,3-Dioxolane (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0655	310.21
0.1213	311.11
0.2166	312.22
0.3132	314.29
0.4281	316.41
0.5181	318.15
0.6063	320.28
0.6950	322.82
0.8017	326.35
0.9063	331.30
0.9428	333.66

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of 1,3-Dioxolane (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0655	320.93
0.1240	321.71
0.2120	323.00
0.3138	324.68
0.4210	326.81
0.5164	328.74
0.6014	330.79
0.6903	333.63
0.7972	337.27
0.8981	341.66
0.9400	344.27

Sources

• Study of isobaric vapour liquid equilibrium of some cyclic ethers with 1-chloropropane: Experimental results and SAFT-VR modelling