Mixture of 1,3-Dioxolan-2-one + Water

Datasets

1. Mass fraction (2)
2. P_vap - Vapor or sublimation pressure, kPa (2)
3. n₀ - Refractive index (Na D-line) (2)
4. ρ_l - Mass density, kg/m3 (2)

Mass fraction of 1,3-Dioxolan-2-one (1) [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass fraction of 1,3-Dioxolan-2-one (1) - Liquid
298.15	100.00	0.9190

Mass fraction of 1,3-Dioxolan-2-one (1) [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass fraction of 1,3-Dioxolan-2-one (1) - Liquid
298.15	100.00	0.9190

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Water (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.4000	314.23	6.58
0.4000	319.95	8.73
0.4000	325.63	11.43
0.4000	333.13	16.16
0.4000	340.17	21.60
0.4000	347.39	28.82
0.4000	353.95	37.42
0.4000	360.15	46.75
0.4000	365.87	57.24
0.4000	372.15	70.03
0.4000	378.02	84.38
0.4000	383.13	98.73
0.6000	312.99	6.61
0.6000	318.53	8.85
0.6000	323.90	11.50
0.6000	331.35	16.36
0.6000	337.81	21.89
0.6000	344.39	29.05
0.6000	350.47	37.28
0.6000	356.26	46.74
0.6000	361.65	57.44
0.6000	367.27	70.14
0.6000	372.69	85.13
0.6000	377.48	99.97
0.8000	312.91	6.74
0.8000	319.29	9.41
0.8000	324.66	12.30
0.8000	332.14	17.63
0.8000	338.09	23.11
0.8000	344.45	30.43
0.8000	351.27	40.39
0.8000	356.72	50.23
0.8000	361.61	60.72
0.8000	366.88	73.88
0.8000	372.12	89.27
0.8000	375.15	99.37

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Water (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.4000	314.23	6.58
0.4000	319.95	8.73
0.4000	325.63	11.43
0.4000	333.13	16.16
0.4000	340.17	21.60
0.4000	347.39	28.82
0.4000	353.95	37.42
0.4000	360.15	46.75
0.4000	365.87	57.24
0.4000	372.15	70.03
0.4000	378.02	84.38
0.4000	383.13	98.73
0.6000	312.99	6.61
0.6000	318.53	8.85
0.6000	323.90	11.50
0.6000	331.35	16.36
0.6000	337.81	21.89
0.6000	344.39	29.05
0.6000	350.47	37.28
0.6000	356.26	46.74
0.6000	361.65	57.44
0.6000	367.27	70.14
0.6000	372.69	85.13
0.6000	377.48	99.97
0.8000	312.91	6.74
0.8000	319.29	9.41
0.8000	324.66	12.30
0.8000	332.14	17.63
0.8000	338.09	23.11
0.8000	344.45	30.43
0.8000	351.27	40.39
0.8000	356.72	50.23
0.8000	361.61	60.72
0.8000	366.88	73.88
0.8000	372.12	89.27
0.8000	375.15	99.37

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Water (2) - Liquid	Refractive index (Na D-line) - Liquid
298.20	0.9778	1.34
298.20	0.9593	1.345
298.20	0.9186	1.356
298.20	0.8810	1.364
298.20	0.8239	1.375
298.20	0.7789	1.3805
298.20	0.7258	1.386
298.20	0.6887	1.391
298.20	0.6159	1.397
298.20	0.5766	1.399
298.20	0.5337	1.401
298.20	0.4758	1.4055
298.20	0.4172	1.4085
298.20	0.3321	1.4125
298.20	0.2943	1.414
298.20	0.1962	1.4175
298.20	0.0993	1.4205
308.20	0.9777	1.3385
308.20	0.9591	1.3435
308.20	0.9183	1.354
308.20	0.8807	1.361
308.20	0.8234	1.3705
308.20	0.7785	1.3765
308.20	0.7250	1.381
308.20	0.6880	1.3875
308.20	0.6159	1.3925
308.20	0.5753	1.3955
308.20	0.5337	1.3985
308.20	0.4739	1.4015
308.20	0.4172	1.4055
308.20	0.3321	1.409
308.20	0.2943	1.411
308.20	0.1962	1.4145
308.20	0.0993	1.417
318.20	0.9777	1.337
318.20	0.9590	1.3425
318.20	0.9181	1.3505
318.20	0.8803	1.3585
318.20	0.8228	1.368
318.20	0.7779	1.374
318.20	0.7243	1.3785
318.20	0.6871	1.384
318.20	0.6147	1.3895
318.20	0.5744	1.3925
318.20	0.5315	1.395
318.20	0.4730	1.3985
318.20	0.4172	1.4015
318.20	0.3321	1.406
318.20	0.2943	1.4075
318.20	0.1962	1.4105
318.20	0.0993	1.414

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Water (2) - Liquid	Refractive index (Na D-line) - Liquid
298.20	0.9778	1.34
298.20	0.9593	1.345
298.20	0.9186	1.356
298.20	0.8810	1.364
298.20	0.8239	1.375
298.20	0.7789	1.3805
298.20	0.7258	1.386
298.20	0.6887	1.391
298.20	0.6159	1.397
298.20	0.5766	1.399
298.20	0.5337	1.401
298.20	0.4758	1.4055
298.20	0.4172	1.4085
298.20	0.3321	1.4125
298.20	0.2943	1.414
298.20	0.1962	1.4175
298.20	0.0993	1.4205
308.20	0.9777	1.3385
308.20	0.9591	1.3435
308.20	0.9183	1.354
308.20	0.8807	1.361
308.20	0.8234	1.3705
308.20	0.7785	1.3765
308.20	0.7250	1.381
308.20	0.6880	1.3875
308.20	0.6159	1.3925
308.20	0.5753	1.3955
308.20	0.5337	1.3985
308.20	0.4739	1.4015
308.20	0.4172	1.4055
308.20	0.3321	1.409
308.20	0.2943	1.411
308.20	0.1962	1.4145
308.20	0.0993	1.417
318.20	0.9777	1.337
318.20	0.9590	1.3425
318.20	0.9181	1.3505
318.20	0.8803	1.3585
318.20	0.8228	1.368
318.20	0.7779	1.374
318.20	0.7243	1.3785
318.20	0.6871	1.384
318.20	0.6147	1.3895
318.20	0.5744	1.3925
318.20	0.5315	1.395
318.20	0.4730	1.3985
318.20	0.4172	1.4015
318.20	0.3321	1.406
318.20	0.2943	1.4075
318.20	0.1962	1.4105
318.20	0.0993	1.414

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 100 (Liquid)

Mass fraction of 1,3-Dioxolan-2-one (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	997.03
0.1000	1026.64
0.2000	1056.71
0.3000	1087.25
0.4000	1118.6

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 100 (Liquid)

Mass fraction of 1,3-Dioxolan-2-one (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	997.03
0.1000	1026.64
0.2000	1056.71
0.3000	1087.25
0.4000	1118.6

Sources

• Thermophysical properties of 1-ethyl-3-methylimidazolium bromide ionic liquid in water + ethylene carbonate mixtures at T = (298.2, 308.2 and 318.2) K
• Phase equilibrium and activity coefficients in ternary systems at 298.15 K: RbCl/CsCl + ethylene carbonate + water
• Phase Equilibria in Binary Mixtures of Water with Cyclic Alkylene Carbonates