Mixture of 1,2-Ethanediol + Ethanol + Water

Datasets

1. Temperature, K x Mole fraction (8)
2. η - Viscosity, Pa*s (2)
3. Refractive index (other wavelength) (2)
4. ρ_l - Mass density, kg/m3 (2)
5. T_boil - Boiling temperature at pressure P, K (2)
6. Vapor Liquid Equilibrium at Constant Pressure (2)
7. Vapor Liquid Equilibrium at Constant Temperature

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 10264.2 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Mole fraction of Water (3) - Liquid	Mole fraction of Water (3) - Gas	Mole fraction of Ethanol (2) - Gas
388.59	0.0290	0.4260	0.7350	0.2450
374.60	0.0400	0.6820	0.7200	0.2700
408.43	0.0690	0.0780	0.2350	0.6930
375.46	0.0870	0.4710	0.5400	0.4540
396.32	0.0880	0.1600	0.3480	0.6250
366.35	0.0880	0.7140	0.5820	0.4170
370.35	0.0880	0.5930	0.5380	0.4610
381.01	0.0890	0.3550	0.4990	0.4910
362.42	0.0920	0.8240	0.5540	0.4450
383.88	0.1790	0.0940	0.1370	0.8510
359.04	0.1980	0.6850	0.4430	0.5560
375.64	0.1980	0.2250	0.2530	0.7410
370.64	0.2010	0.3040	0.3100	0.6880
356.85	0.2010	0.7640	0.4470	0.5520
366.08	0.2030	0.4120	0.3610	0.6380
362.76	0.2060	0.5270	0.4030	0.5960
379.88	0.2490	0.0320	0.0340	0.9530
370.75	0.2860	0.1540	0.1600	0.8370
366.34	0.2940	0.2480	0.2290	0.7700
362.71	0.3010	0.3610	0.2890	0.7100
359.45	0.3060	0.4760	0.3400	0.6590
356.41	0.3070	0.6000	0.3820	0.6170
367.12	0.3920	0.0900	0.0830	0.9150
354.30	0.3990	0.5690	0.3630	0.6360
363.19	0.3990	0.2060	0.1760	0.8230
357.10	0.4020	0.4320	0.3090	0.6900
359.60	0.4170	0.3190	0.2480	0.7510
365.21	0.4770	0.0410	0.0340	0.9650
360.81	0.4980	0.1610	0.1360	0.8620
357.83	0.5030	0.2680	0.2100	0.7890
354.91	0.5060	0.3890	0.2810	0.7180
359.44	0.5960	0.0970	0.0840	0.9150
356.32	0.5990	0.2100	0.1710	0.8280
352.70	0.6370	0.3290	0.2540	0.7450
358.05	0.6940	0.0400	0.0340	0.9650
353.83	0.7280	0.1720	0.1490	0.8500
353.57	0.8110	0.0970	0.0900	0.9090
352.37	0.9100	0.0460	0.0460	0.9530

Mole fraction of Water (3) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Fixed		Measured
Solvent: Mole fraction of Ethanol (2) - Liquid	Mass fraction of 1,2-Ethanediol (1) - Liquid	Mole fraction of Water (3) - Gas
0.1992	0.8035	0.4738
0.2004	0.7012	0.4673
0.2012	0.6032	0.4582
0.2004	0.5051	0.4548
0.2007	0.4003	0.4564
0.2000	0.3018	0.4552
0.2005	0.2003	0.4555
0.2000	0.1010	0.4624
0.9514	0.8026	0.0170
0.9502	0.7038	0.0206
0.9504	0.6007	0.0240
0.9504	0.5015	0.0274
0.9505	0.4021	0.0313
0.9500	0.3021	0.0362
0.9506	0.2035	0.0409
0.9503	0.1010	0.0467

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Fixed		Measured
Solvent: Mole fraction of Ethanol (2) - Liquid	Mass fraction of 1,2-Ethanediol (1) - Liquid	Mole fraction of Ethanol (2) - Gas
0.1992	0.8035	0.5088
0.2004	0.7012	0.5247
0.2012	0.6032	0.5355
0.2004	0.5051	0.5425
0.2007	0.4003	0.5417
0.2000	0.3018	0.5436
0.2005	0.2003	0.5438
0.2000	0.1010	0.5373
0.9514	0.8026	0.9607
0.9502	0.7038	0.9669
0.9504	0.6007	0.9663
0.9504	0.5015	0.9653
0.9505	0.4021	0.9636
0.9500	0.3021	0.9603
0.9506	0.2035	0.9568
0.9503	0.1010	0.9523

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Mole fraction of Water (3) - Liquid	Mole fraction of Water (3) - Gas	Mole fraction of Ethanol (2) - Gas
365.94	0.0780	0.7530	0.5980	0.4010
366.41	0.1030	0.6640	0.5480	0.4510
362.64	0.1590	0.6330	0.4740	0.5250
368.94	0.1720	0.4260	0.4000	0.5940
371.77	0.1810	0.3330	0.3440	0.6480
364.51	0.1870	0.5160	0.4220	0.5760
367.63	0.1920	0.4210	0.3770	0.6180
365.43	0.1930	0.4830	0.4060	0.5910
368.76	0.2100	0.3550	0.3380	0.6570
361.77	0.2300	0.5280	0.4010	0.5980
366.50	0.2310	0.3740	0.3340	0.6610
363.60	0.2350	0.4580	0.3700	0.6270
361.83	0.2550	0.4780	0.3690	0.6290
364.40	0.2550	0.3950	0.3340	0.6630
367.79	0.2680	0.2780	0.2620	0.7340
362.54	0.2790	0.4160	0.3360	0.6620
365.48	0.2960	0.2960	0.2640	0.7310
368.45	0.3400	0.1440	0.1420	0.8520
362.39	0.3930	0.2400	0.2100	0.7870
368.91	0.4030	0.0390	0.0410	0.9500
363.98	0.4160	0.1650	0.1520	0.8440
360.58	0.4290	0.2550	0.2140	0.7840
367.81	0.4410	0.0190	0.0200	0.9740
358.86	0.4670	0.2700	0.2230	0.7760
360.55	0.4910	0.1900	0.1620	0.8360
362.39	0.5080	0.0990	0.0890	0.9070
359.93	0.5710	0.1100	0.0980	0.8990
357.14	0.5810	0.2150	0.1800	0.8190
359.74	0.6070	0.0750	0.0710	0.9270
359.79	0.6130	0.0690	0.0660	0.9310
358.43	0.6640	0.0530	0.0500	0.9480
356.24	0.6780	0.1230	0.1100	0.8890
353.77	0.9100	0.0020	0.0030	0.9960

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 10264.2 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Mole fraction of Water (3) - Liquid	Mole fraction of Water (3) - Gas	Mole fraction of Ethanol (2) - Gas
388.59	0.0290	0.4260	0.7350	0.2450
374.60	0.0400	0.6820	0.7200	0.2700
408.43	0.0690	0.0780	0.2350	0.6930
375.46	0.0870	0.4710	0.5400	0.4540
396.32	0.0880	0.1600	0.3480	0.6250
366.35	0.0880	0.7140	0.5820	0.4170
370.35	0.0880	0.5930	0.5380	0.4610
381.01	0.0890	0.3550	0.4990	0.4910
362.42	0.0920	0.8240	0.5540	0.4450
383.88	0.1790	0.0940	0.1370	0.8510
359.04	0.1980	0.6850	0.4430	0.5560
375.64	0.1980	0.2250	0.2530	0.7410
370.64	0.2010	0.3040	0.3100	0.6880
356.85	0.2010	0.7640	0.4470	0.5520
366.08	0.2030	0.4120	0.3610	0.6380
362.76	0.2060	0.5270	0.4030	0.5960
379.88	0.2490	0.0320	0.0340	0.9530
370.75	0.2860	0.1540	0.1600	0.8370
366.34	0.2940	0.2480	0.2290	0.7700
362.71	0.3010	0.3610	0.2890	0.7100
359.45	0.3060	0.4760	0.3400	0.6590
356.41	0.3070	0.6000	0.3820	0.6170
367.12	0.3920	0.0900	0.0830	0.9150
354.30	0.3990	0.5690	0.3630	0.6360
363.19	0.3990	0.2060	0.1760	0.8230
357.10	0.4020	0.4320	0.3090	0.6900
359.60	0.4170	0.3190	0.2480	0.7510
365.21	0.4770	0.0410	0.0340	0.9650
360.81	0.4980	0.1610	0.1360	0.8620
357.83	0.5030	0.2680	0.2100	0.7890
354.91	0.5060	0.3890	0.2810	0.7180
359.44	0.5960	0.0970	0.0840	0.9150
356.32	0.5990	0.2100	0.1710	0.8280
352.70	0.6370	0.3290	0.2540	0.7450
358.05	0.6940	0.0400	0.0340	0.9650
353.83	0.7280	0.1720	0.1490	0.8500
353.57	0.8110	0.0970	0.0900	0.9090
352.37	0.9100	0.0460	0.0460	0.9530

Mole fraction of Water (3) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Fixed		Measured
Solvent: Mole fraction of Ethanol (2) - Liquid	Mass fraction of 1,2-Ethanediol (1) - Liquid	Mole fraction of Water (3) - Gas
0.1992	0.8035	0.4738
0.2004	0.7012	0.4673
0.2012	0.6032	0.4582
0.2004	0.5051	0.4548
0.2007	0.4003	0.4564
0.2000	0.3018	0.4552
0.2005	0.2003	0.4555
0.2000	0.1010	0.4624
0.9514	0.8026	0.0170
0.9502	0.7038	0.0206
0.9504	0.6007	0.0240
0.9504	0.5015	0.0274
0.9505	0.4021	0.0313
0.9500	0.3021	0.0362
0.9506	0.2035	0.0409
0.9503	0.1010	0.0467

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Fixed		Measured
Solvent: Mole fraction of Ethanol (2) - Liquid	Mass fraction of 1,2-Ethanediol (1) - Liquid	Mole fraction of Ethanol (2) - Gas
0.1992	0.8035	0.5088
0.2004	0.7012	0.5247
0.2012	0.6032	0.5355
0.2004	0.5051	0.5425
0.2007	0.4003	0.5417
0.2000	0.3018	0.5436
0.2005	0.2003	0.5438
0.2000	0.1010	0.5373
0.9514	0.8026	0.9607
0.9502	0.7038	0.9669
0.9504	0.6007	0.9663
0.9504	0.5015	0.9653
0.9505	0.4021	0.9636
0.9500	0.3021	0.9603
0.9506	0.2035	0.9568
0.9503	0.1010	0.9523

Temperature, K x Mole fraction [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Mole fraction of Water (3) - Liquid	Mole fraction of Water (3) - Gas	Mole fraction of Ethanol (2) - Gas
365.94	0.0780	0.7530	0.5980	0.4010
366.41	0.1030	0.6640	0.5480	0.4510
362.64	0.1590	0.6330	0.4740	0.5250
368.94	0.1720	0.4260	0.4000	0.5940
371.77	0.1810	0.3330	0.3440	0.6480
364.51	0.1870	0.5160	0.4220	0.5760
367.63	0.1920	0.4210	0.3770	0.6180
365.43	0.1930	0.4830	0.4060	0.5910
368.76	0.2100	0.3550	0.3380	0.6570
361.77	0.2300	0.5280	0.4010	0.5980
366.50	0.2310	0.3740	0.3340	0.6610
363.60	0.2350	0.4580	0.3700	0.6270
361.83	0.2550	0.4780	0.3690	0.6290
364.40	0.2550	0.3950	0.3340	0.6630
367.79	0.2680	0.2780	0.2620	0.7340
362.54	0.2790	0.4160	0.3360	0.6620
365.48	0.2960	0.2960	0.2640	0.7310
368.45	0.3400	0.1440	0.1420	0.8520
362.39	0.3930	0.2400	0.2100	0.7870
368.91	0.4030	0.0390	0.0410	0.9500
363.98	0.4160	0.1650	0.1520	0.8440
360.58	0.4290	0.2550	0.2140	0.7840
367.81	0.4410	0.0190	0.0200	0.9740
358.86	0.4670	0.2700	0.2230	0.7760
360.55	0.4910	0.1900	0.1620	0.8360
362.39	0.5080	0.0990	0.0890	0.9070
359.93	0.5710	0.1100	0.0980	0.8990
357.14	0.5810	0.2150	0.1800	0.8190
359.74	0.6070	0.0750	0.0710	0.9270
359.79	0.6130	0.0690	0.0660	0.9310
358.43	0.6640	0.0530	0.0500	0.9480
356.24	0.6780	0.1230	0.1100	0.8890
353.77	0.9100	0.0020	0.0030	0.9960

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Water (3) - Liquid	Mole fraction of Ethanol (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.4024	0.2725	0.0046
298.15	0.8369	0.1135	0.0024
298.15	0.7015	0.2350	0.0028
298.15	0.7496	0.0969	0.0032
298.15	0.6972	0.1921	0.0031
298.15	0.6064	0.2391	0.0033
298.15	0.3099	0.2050	0.0065
298.15	0.5988	0.2058	0.0037
298.15	0.5101	0.2408	0.0041
298.15	0.6944	0.1130	0.0036
298.15	0.6172	0.1056	0.0045
298.15	0.7674	0.1960	0.0026
298.15	0.2892	0.2887	0.0053
298.15	0.8011	0.1000	0.0027
298.15	0.1074	0.4050	0.0051
298.15	0.2766	0.4220	0.0037
298.15	0.1097	0.5862	0.0030
298.15	0.4213	0.4769	0.0025
298.15	0.2107	0.6868	0.0019
298.15	0.3126	0.4726	0.0030
298.15	0.5023	0.2981	0.0035
298.15	0.5076	0.3919	0.0027
298.15	0.1130	0.6858	0.0023
298.15	0.7919	0.0490	0.0029
298.15	0.1998	0.5973	0.0026
298.15	0.3940	0.4086	0.0032
298.15	0.1025	0.4945	0.0039
298.15	0.2997	0.5938	0.0022
298.15	0.1177	0.7891	0.0017
298.15	0.0010	0.9071	0.0014
298.15	0.0010	0.7826	0.0020
298.15	0.0009	0.6667	0.0028
298.15	0.0009	0.5990	0.0033
298.15	0.0009	0.4943	0.0045
308.15	0.4024	0.2725	0.0034
308.15	0.8369	0.1135	0.0017
308.15	0.7015	0.2350	0.0020
308.15	0.7496	0.0969	0.0023
308.15	0.6972	0.1921	0.0022
308.15	0.6064	0.2391	0.0025
308.15	0.3099	0.2050	0.0047
308.15	0.5988	0.2058	0.0027
308.15	0.5101	0.2408	0.0030
308.15	0.6944	0.1130	0.0026
308.15	0.6172	0.1056	0.0032
308.15	0.7674	0.1960	0.0019
308.15	0.2892	0.2887	0.0039
308.15	0.8011	0.1000	0.0020
308.15	0.1074	0.4050	0.0038
318.15	0.4024	0.2725	0.0026
318.15	0.8369	0.1135	0.0013
318.15	0.7015	0.2350	0.0015
318.15	0.7496	0.0969	0.0018
318.15	0.6972	0.1921	0.0017
318.15	0.6064	0.2391	0.0019
318.15	0.3099	0.2050	0.0035
318.15	0.5988	0.2058	0.0021
318.15	0.5101	0.2408	0.0023
318.15	0.6944	0.1130	0.0020
318.15	0.6172	0.1056	0.0025
318.15	0.7674	0.1960	0.0014
318.15	0.2892	0.2887	0.0030
318.15	0.8011	0.1000	0.0015
318.15	0.1074	0.4050	0.0029
328.15	0.4024	0.2725	0.0020
328.15	0.8369	0.1135	0.0010
328.15	0.7015	0.2350	0.0012
328.15	0.7496	0.0969	0.0014
328.15	0.6972	0.1921	0.0013
328.15	0.6064	0.2391	0.0015
328.15	0.3099	0.2050	0.0027
328.15	0.5988	0.2058	0.0016
328.15	0.5101	0.2408	0.0018
328.15	0.6944	0.1130	0.0016
328.15	0.6172	0.1056	0.0019
328.15	0.7674	0.1960	0.0011
328.15	0.2892	0.2887	0.0023
328.15	0.8011	0.1000	0.0012

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Water (3) - Liquid	Mole fraction of Ethanol (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.4024	0.2725	0.0046
298.15	0.8369	0.1135	0.0024
298.15	0.7015	0.2350	0.0028
298.15	0.7496	0.0969	0.0032
298.15	0.6972	0.1921	0.0031
298.15	0.6064	0.2391	0.0033
298.15	0.3099	0.2050	0.0065
298.15	0.5988	0.2058	0.0037
298.15	0.5101	0.2408	0.0041
298.15	0.6944	0.1130	0.0036
298.15	0.6172	0.1056	0.0045
298.15	0.7674	0.1960	0.0026
298.15	0.2892	0.2887	0.0053
298.15	0.8011	0.1000	0.0027
298.15	0.1074	0.4050	0.0051
298.15	0.2766	0.4220	0.0037
298.15	0.1097	0.5862	0.0030
298.15	0.4213	0.4769	0.0025
298.15	0.2107	0.6868	0.0019
298.15	0.3126	0.4726	0.0030
298.15	0.5023	0.2981	0.0035
298.15	0.5076	0.3919	0.0027
298.15	0.1130	0.6858	0.0023
298.15	0.7919	0.0490	0.0029
298.15	0.1998	0.5973	0.0026
298.15	0.3940	0.4086	0.0032
298.15	0.1025	0.4945	0.0039
298.15	0.2997	0.5938	0.0022
298.15	0.1177	0.7891	0.0017
298.15	0.0010	0.9071	0.0014
298.15	0.0010	0.7826	0.0020
298.15	0.0009	0.6667	0.0028
298.15	0.0009	0.5990	0.0033
298.15	0.0009	0.4943	0.0045
308.15	0.4024	0.2725	0.0034
308.15	0.8369	0.1135	0.0017
308.15	0.7015	0.2350	0.0020
308.15	0.7496	0.0969	0.0023
308.15	0.6972	0.1921	0.0022
308.15	0.6064	0.2391	0.0025
308.15	0.3099	0.2050	0.0047
308.15	0.5988	0.2058	0.0027
308.15	0.5101	0.2408	0.0030
308.15	0.6944	0.1130	0.0026
308.15	0.6172	0.1056	0.0032
308.15	0.7674	0.1960	0.0019
308.15	0.2892	0.2887	0.0039
308.15	0.8011	0.1000	0.0020
308.15	0.1074	0.4050	0.0038
318.15	0.4024	0.2725	0.0026
318.15	0.8369	0.1135	0.0013
318.15	0.7015	0.2350	0.0015
318.15	0.7496	0.0969	0.0018
318.15	0.6972	0.1921	0.0017
318.15	0.6064	0.2391	0.0019
318.15	0.3099	0.2050	0.0035
318.15	0.5988	0.2058	0.0021
318.15	0.5101	0.2408	0.0023
318.15	0.6944	0.1130	0.0020
318.15	0.6172	0.1056	0.0025
318.15	0.7674	0.1960	0.0014
318.15	0.2892	0.2887	0.0030
318.15	0.8011	0.1000	0.0015
318.15	0.1074	0.4050	0.0029
328.15	0.4024	0.2725	0.0020
328.15	0.8369	0.1135	0.0010
328.15	0.7015	0.2350	0.0012
328.15	0.7496	0.0969	0.0014
328.15	0.6972	0.1921	0.0013
328.15	0.6064	0.2391	0.0015
328.15	0.3099	0.2050	0.0027
328.15	0.5988	0.2058	0.0016
328.15	0.5101	0.2408	0.0018
328.15	0.6944	0.1130	0.0016
328.15	0.6172	0.1056	0.0019
328.15	0.7674	0.1960	0.0011
328.15	0.2892	0.2887	0.0023
328.15	0.8011	0.1000	0.0012

Refractive index (other wavelength) [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Fixed			Measured
Mass fraction of Water (3) - Liquid	Mass fraction of Ethanol (2) - Liquid	Wavelength, nm - Liquid	Refractive index (other wavelength) - Liquid
0.0000	0.0000	670.0	1.4287
0.0000	0.0996	670.0	1.421
0.0000	0.1994	670.0	1.4135
0.0000	0.2999	670.0	1.4058
0.0000	0.4003	670.0	1.3984
0.0000	0.5002	670.0	1.3912
0.0000	0.5999	670.0	1.3843
0.0000	0.7006	670.0	1.3776
0.0000	0.8002	670.0	1.3708
0.0000	0.9000	670.0	1.3645
0.0000	1.0000	670.0	1.3584
0.0985	0.8031	670.0	1.3667
0.0992	0.0997	670.0	1.4127
0.0995	0.6009	670.0	1.3789
0.0995	0.7012	670.0	1.3727
0.0998	0.3996	670.0	1.392
0.1000	0.4995	670.0	1.3853
0.1001	0.3002	670.0	1.3988
0.1002	0.0000	670.0	1.4197
0.1008	0.8992	670.0	1.361
0.1017	0.1995	670.0	1.4055
0.1998	0.0996	670.0	1.4041
0.1999	0.0000	670.0	1.4104
0.2000	0.4000	670.0	1.3852
0.2002	0.3003	670.0	1.3914
0.2003	0.6995	670.0	1.3673
0.2006	0.2002	670.0	1.3977
0.2006	0.5994	670.0	1.373
0.2008	0.4994	670.0	1.3791
0.2045	0.7955	670.0	1.3619
0.2975	0.7025	670.0	1.3615
0.2995	0.0000	670.0	1.4007
0.2996	0.4001	670.0	1.378
0.2998	0.5000	670.0	1.3723
0.2999	0.0998	670.0	1.3951
0.3002	0.1999	670.0	1.3894
0.3036	0.2984	670.0	1.3835
0.3078	0.5933	670.0	1.3667
0.3993	0.5011	670.0	1.3654
0.3994	0.1999	670.0	1.381
0.3996	0.0000	670.0	1.3908
0.4001	0.1002	670.0	1.3859
0.4006	0.3999	670.0	1.3705
0.4018	0.2991	670.0	1.3756
0.4032	0.5968	670.0	1.3603
0.4974	0.5026	670.0	1.3584
0.4992	0.1999	670.0	1.3723
0.4996	0.3005	670.0	1.3678
0.5001	0.1000	670.0	1.3764
0.5003	0.0000	670.0	1.3805
0.5004	0.4003	670.0	1.3629
0.5994	0.3002	670.0	1.3594
0.5998	0.1001	670.0	1.3668
0.6001	0.0000	670.0	1.3705
0.6006	0.1996	670.0	1.3632
0.6008	0.3992	670.0	1.3551
0.6996	0.0000	670.0	1.3603
0.6999	0.2004	670.0	1.354
0.7001	0.0997	670.0	1.357
0.7013	0.2987	670.0	1.3506
0.7985	0.2015	670.0	1.3447
0.7994	0.0999	670.0	1.3473
0.7997	0.0000	670.0	1.3503
0.8946	0.1054	670.0	1.338
0.9001	0.0000	670.0	1.3405
1.0000	0.0000	670.0	1.331
0.0000	0.0000	925.0	1.424
0.0000	0.0996	925.0	1.4164
0.0000	0.1994	925.0	1.4089
0.0000	0.2999	925.0	1.4013
0.0000	0.4003	925.0	1.394
0.0000	0.5002	925.0	1.3871
0.0000	0.5999	925.0	1.3803
0.0000	0.7006	925.0	1.3734
0.0000	0.8002	925.0	1.367
0.0000	0.9000	925.0	1.3606
0.0000	1.0000	925.0	1.3545
0.0985	0.8031	925.0	1.3626
0.0992	0.0997	925.0	1.4081
0.0995	0.6009	925.0	1.3747
0.0995	0.7012	925.0	1.3686
0.0998	0.3996	925.0	1.3876
0.1000	0.4995	925.0	1.3811
0.1001	0.3002	925.0	1.3941
0.1002	0.0000	925.0	1.415
0.1008	0.8992	925.0	1.3571
0.1017	0.1995	925.0	1.401
0.1998	0.0996	925.0	1.3994
0.1999	0.0000	925.0	1.4056
0.2000	0.4000	925.0	1.3808
0.2002	0.3003	925.0	1.3869
0.2003	0.6995	925.0	1.3632
0.2006	0.2002	925.0	1.3931
0.2006	0.5994	925.0	1.3689
0.2008	0.4994	925.0	1.3748
0.2045	0.7955	925.0	1.3578
0.2975	0.7025	925.0	1.3574
0.2995	0.0000	925.0	1.396
0.2996	0.4001	925.0	1.3737
0.2998	0.5000	925.0	1.368
0.2999	0.0998	925.0	1.3905
0.3002	0.1999	925.0	1.3848
0.3036	0.2984	925.0	1.379
0.3078	0.5933	925.0	1.3625
0.3993	0.5011	925.0	1.361
0.3994	0.1999	925.0	1.3763
0.3996	0.0000	925.0	1.3861
0.4001	0.1002	925.0	1.3813
0.4006	0.3999	925.0	1.3661
0.4018	0.2991	925.0	1.3711
0.4032	0.5968	925.0	1.3561
0.4974	0.5026	925.0	1.354
0.4992	0.1999	925.0	1.3675
0.4996	0.3005	925.0	1.3631
0.5001	0.1000	925.0	1.3717
0.5003	0.0000	925.0	1.3758
0.5004	0.4003	925.0	1.3585
0.5994	0.3002	925.0	1.3548
0.5998	0.1001	925.0	1.3621
0.6001	0.0000	925.0	1.3657
0.6006	0.1996	925.0	1.3584
0.6008	0.3992	925.0	1.3507
0.6996	0.0000	925.0	1.3555
0.6999	0.2004	925.0	1.3494
0.7001	0.0997	925.0	1.3523
0.7013	0.2987	925.0	1.3461
0.7985	0.2015	925.0	1.34
0.7994	0.0999	925.0	1.3426
0.7997	0.0000	925.0	1.3455
0.8946	0.1054	925.0	1.3332
0.9001	0.0000	925.0	1.3357
1.0000	0.0000	925.0	1.3264

Refractive index (other wavelength) [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Fixed			Measured
Mass fraction of Water (3) - Liquid	Mass fraction of Ethanol (2) - Liquid	Wavelength, nm - Liquid	Refractive index (other wavelength) - Liquid
0.0000	0.0000	670.0	1.4287
0.0000	0.0996	670.0	1.421
0.0000	0.1994	670.0	1.4135
0.0000	0.2999	670.0	1.4058
0.0000	0.4003	670.0	1.3984
0.0000	0.5002	670.0	1.3912
0.0000	0.5999	670.0	1.3843
0.0000	0.7006	670.0	1.3776
0.0000	0.8002	670.0	1.3708
0.0000	0.9000	670.0	1.3645
0.0000	1.0000	670.0	1.3584
0.0985	0.8031	670.0	1.3667
0.0992	0.0997	670.0	1.4127
0.0995	0.6009	670.0	1.3789
0.0995	0.7012	670.0	1.3727
0.0998	0.3996	670.0	1.392
0.1000	0.4995	670.0	1.3853
0.1001	0.3002	670.0	1.3988
0.1002	0.0000	670.0	1.4197
0.1008	0.8992	670.0	1.361
0.1017	0.1995	670.0	1.4055
0.1998	0.0996	670.0	1.4041
0.1999	0.0000	670.0	1.4104
0.2000	0.4000	670.0	1.3852
0.2002	0.3003	670.0	1.3914
0.2003	0.6995	670.0	1.3673
0.2006	0.2002	670.0	1.3977
0.2006	0.5994	670.0	1.373
0.2008	0.4994	670.0	1.3791
0.2045	0.7955	670.0	1.3619
0.2975	0.7025	670.0	1.3615
0.2995	0.0000	670.0	1.4007
0.2996	0.4001	670.0	1.378
0.2998	0.5000	670.0	1.3723
0.2999	0.0998	670.0	1.3951
0.3002	0.1999	670.0	1.3894
0.3036	0.2984	670.0	1.3835
0.3078	0.5933	670.0	1.3667
0.3993	0.5011	670.0	1.3654
0.3994	0.1999	670.0	1.381
0.3996	0.0000	670.0	1.3908
0.4001	0.1002	670.0	1.3859
0.4006	0.3999	670.0	1.3705
0.4018	0.2991	670.0	1.3756
0.4032	0.5968	670.0	1.3603
0.4974	0.5026	670.0	1.3584
0.4992	0.1999	670.0	1.3723
0.4996	0.3005	670.0	1.3678
0.5001	0.1000	670.0	1.3764
0.5003	0.0000	670.0	1.3805
0.5004	0.4003	670.0	1.3629
0.5994	0.3002	670.0	1.3594
0.5998	0.1001	670.0	1.3668
0.6001	0.0000	670.0	1.3705
0.6006	0.1996	670.0	1.3632
0.6008	0.3992	670.0	1.3551
0.6996	0.0000	670.0	1.3603
0.6999	0.2004	670.0	1.354
0.7001	0.0997	670.0	1.357
0.7013	0.2987	670.0	1.3506
0.7985	0.2015	670.0	1.3447
0.7994	0.0999	670.0	1.3473
0.7997	0.0000	670.0	1.3503
0.8946	0.1054	670.0	1.338
0.9001	0.0000	670.0	1.3405
1.0000	0.0000	670.0	1.331
0.0000	0.0000	925.0	1.424
0.0000	0.0996	925.0	1.4164
0.0000	0.1994	925.0	1.4089
0.0000	0.2999	925.0	1.4013
0.0000	0.4003	925.0	1.394
0.0000	0.5002	925.0	1.3871
0.0000	0.5999	925.0	1.3803
0.0000	0.7006	925.0	1.3734
0.0000	0.8002	925.0	1.367
0.0000	0.9000	925.0	1.3606
0.0000	1.0000	925.0	1.3545
0.0985	0.8031	925.0	1.3626
0.0992	0.0997	925.0	1.4081
0.0995	0.6009	925.0	1.3747
0.0995	0.7012	925.0	1.3686
0.0998	0.3996	925.0	1.3876
0.1000	0.4995	925.0	1.3811
0.1001	0.3002	925.0	1.3941
0.1002	0.0000	925.0	1.415
0.1008	0.8992	925.0	1.3571
0.1017	0.1995	925.0	1.401
0.1998	0.0996	925.0	1.3994
0.1999	0.0000	925.0	1.4056
0.2000	0.4000	925.0	1.3808
0.2002	0.3003	925.0	1.3869
0.2003	0.6995	925.0	1.3632
0.2006	0.2002	925.0	1.3931
0.2006	0.5994	925.0	1.3689
0.2008	0.4994	925.0	1.3748
0.2045	0.7955	925.0	1.3578
0.2975	0.7025	925.0	1.3574
0.2995	0.0000	925.0	1.396
0.2996	0.4001	925.0	1.3737
0.2998	0.5000	925.0	1.368
0.2999	0.0998	925.0	1.3905
0.3002	0.1999	925.0	1.3848
0.3036	0.2984	925.0	1.379
0.3078	0.5933	925.0	1.3625
0.3993	0.5011	925.0	1.361
0.3994	0.1999	925.0	1.3763
0.3996	0.0000	925.0	1.3861
0.4001	0.1002	925.0	1.3813
0.4006	0.3999	925.0	1.3661
0.4018	0.2991	925.0	1.3711
0.4032	0.5968	925.0	1.3561
0.4974	0.5026	925.0	1.354
0.4992	0.1999	925.0	1.3675
0.4996	0.3005	925.0	1.3631
0.5001	0.1000	925.0	1.3717
0.5003	0.0000	925.0	1.3758
0.5004	0.4003	925.0	1.3585
0.5994	0.3002	925.0	1.3548
0.5998	0.1001	925.0	1.3621
0.6001	0.0000	925.0	1.3657
0.6006	0.1996	925.0	1.3584
0.6008	0.3992	925.0	1.3507
0.6996	0.0000	925.0	1.3555
0.6999	0.2004	925.0	1.3494
0.7001	0.0997	925.0	1.3523
0.7013	0.2987	925.0	1.3461
0.7985	0.2015	925.0	1.34
0.7994	0.0999	925.0	1.3426
0.7997	0.0000	925.0	1.3455
0.8946	0.1054	925.0	1.3332
0.9001	0.0000	925.0	1.3357
1.0000	0.0000	925.0	1.3264

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Water (3) - Liquid	Mole fraction of Ethanol (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.4024	0.2725	984.38
298.15	0.8369	0.1135	977.58
298.15	0.7015	0.2350	942.83
298.15	0.7496	0.0969	1011.46
298.15	0.6972	0.1921	968.95
298.15	0.6064	0.2391	964.07
298.15	0.3099	0.2050	1023.78
298.15	0.5988	0.2058	983.27
298.15	0.5101	0.2408	981.86
298.15	0.6944	0.1130	1018.22
298.15	0.6172	0.1056	1030.42
298.15	0.7674	0.1960	947.08
298.15	0.2892	0.2887	992.82
298.15	0.8011	0.1000	997.03
298.15	0.1074	0.4050	971.71
298.15	0.2766	0.4220	942.18
298.15	0.1097	0.5862	907.68
298.15	0.4213	0.4769	891.54
298.15	0.2107	0.6868	851.46
298.15	0.3126	0.4726	915.49
298.15	0.5023	0.2981	956.01
298.15	0.5076	0.3919	909.58
298.15	0.1130	0.6858	871.65
298.15	0.7919	0.0490	1030.09
298.15	0.1998	0.5973	888.87
298.15	0.3940	0.4086	926.94
298.15	0.1025	0.4945	941.17
298.15	0.2997	0.5938	868.59
298.15	0.1177	0.7891	833.74
298.15	0.0010	0.9071	816.74
298.15	0.0010	0.7826	858.81
298.15	0.0009	0.6667	897.53
298.15	0.0009	0.5990	919.81
298.15	0.0009	0.4943	954.24
308.15	0.4024	0.2725	976.68
308.15	0.8369	0.1135	971.23
308.15	0.7015	0.2350	935.01
308.15	0.7496	0.0969	1004.78
308.15	0.6972	0.1921	961.44
308.15	0.6064	0.2391	956.31
308.15	0.3099	0.2050	1016.34
308.15	0.5988	0.2058	975.7
308.15	0.5101	0.2408	974.18
308.15	0.6944	0.1130	1011.33
308.15	0.6172	0.1056	1023.34
308.15	0.7674	0.1960	939.55
308.15	0.2892	0.2887	985.18
308.15	0.8011	0.1000	990.59
308.15	0.1074	0.4050	963.96
318.15	0.4024	0.2725	968.82
318.15	0.8369	0.1135	964.45
318.15	0.7015	0.2350	926.95
318.15	0.7496	0.0969	997.79
318.15	0.6972	0.1921	953.68
318.15	0.6064	0.2391	948.34
318.15	0.3099	0.2050	1008.76
318.15	0.5988	0.2058	967.91
318.15	0.5101	0.2408	966.32
318.15	0.6944	0.1130	1004.19
318.15	0.6172	0.1056	1016.05
318.15	0.7674	0.1960	931.73
318.15	0.2892	0.2887	977.39
318.15	0.8011	0.1000	983.79
318.15	0.1074	0.4050	956.1
328.15	0.4024	0.2725	960.78
328.15	0.8369	0.1135	957.29
328.15	0.7015	0.2350	918.61
328.15	0.7496	0.0969	990.51
328.15	0.6972	0.1921	945.65
328.15	0.6064	0.2391	940.14
328.15	0.3099	0.2050	1001.04
328.15	0.5988	0.2058	959.9
328.15	0.5101	0.2408	958.25
328.15	0.6944	0.1130	996.79
328.15	0.6172	0.1056	1008.54
328.15	0.7674	0.1960	923.62
328.15	0.2892	0.2887	969.45
328.15	0.8011	0.1000	976.64

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed			Measured
Temperature, K - Liquid	Mole fraction of Water (3) - Liquid	Mole fraction of Ethanol (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.4024	0.2725	984.38
298.15	0.8369	0.1135	977.58
298.15	0.7015	0.2350	942.83
298.15	0.7496	0.0969	1011.46
298.15	0.6972	0.1921	968.95
298.15	0.6064	0.2391	964.07
298.15	0.3099	0.2050	1023.78
298.15	0.5988	0.2058	983.27
298.15	0.5101	0.2408	981.86
298.15	0.6944	0.1130	1018.22
298.15	0.6172	0.1056	1030.42
298.15	0.7674	0.1960	947.08
298.15	0.2892	0.2887	992.82
298.15	0.8011	0.1000	997.03
298.15	0.1074	0.4050	971.71
298.15	0.2766	0.4220	942.18
298.15	0.1097	0.5862	907.68
298.15	0.4213	0.4769	891.54
298.15	0.2107	0.6868	851.46
298.15	0.3126	0.4726	915.49
298.15	0.5023	0.2981	956.01
298.15	0.5076	0.3919	909.58
298.15	0.1130	0.6858	871.65
298.15	0.7919	0.0490	1030.09
298.15	0.1998	0.5973	888.87
298.15	0.3940	0.4086	926.94
298.15	0.1025	0.4945	941.17
298.15	0.2997	0.5938	868.59
298.15	0.1177	0.7891	833.74
298.15	0.0010	0.9071	816.74
298.15	0.0010	0.7826	858.81
298.15	0.0009	0.6667	897.53
298.15	0.0009	0.5990	919.81
298.15	0.0009	0.4943	954.24
308.15	0.4024	0.2725	976.68
308.15	0.8369	0.1135	971.23
308.15	0.7015	0.2350	935.01
308.15	0.7496	0.0969	1004.78
308.15	0.6972	0.1921	961.44
308.15	0.6064	0.2391	956.31
308.15	0.3099	0.2050	1016.34
308.15	0.5988	0.2058	975.7
308.15	0.5101	0.2408	974.18
308.15	0.6944	0.1130	1011.33
308.15	0.6172	0.1056	1023.34
308.15	0.7674	0.1960	939.55
308.15	0.2892	0.2887	985.18
308.15	0.8011	0.1000	990.59
308.15	0.1074	0.4050	963.96
318.15	0.4024	0.2725	968.82
318.15	0.8369	0.1135	964.45
318.15	0.7015	0.2350	926.95
318.15	0.7496	0.0969	997.79
318.15	0.6972	0.1921	953.68
318.15	0.6064	0.2391	948.34
318.15	0.3099	0.2050	1008.76
318.15	0.5988	0.2058	967.91
318.15	0.5101	0.2408	966.32
318.15	0.6944	0.1130	1004.19
318.15	0.6172	0.1056	1016.05
318.15	0.7674	0.1960	931.73
318.15	0.2892	0.2887	977.39
318.15	0.8011	0.1000	983.79
318.15	0.1074	0.4050	956.1
328.15	0.4024	0.2725	960.78
328.15	0.8369	0.1135	957.29
328.15	0.7015	0.2350	918.61
328.15	0.7496	0.0969	990.51
328.15	0.6972	0.1921	945.65
328.15	0.6064	0.2391	940.14
328.15	0.3099	0.2050	1001.04
328.15	0.5988	0.2058	959.9
328.15	0.5101	0.2408	958.25
328.15	0.6944	0.1130	996.79
328.15	0.6172	0.1056	1008.54
328.15	0.7674	0.1960	923.62
328.15	0.2892	0.2887	969.45
328.15	0.8011	0.1000	976.64

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Solvent: Mole fraction of Ethanol (2) - Liquid	Mass fraction of 1,2-Ethanediol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.1992	0.8035	385.08
0.2004	0.7012	375.23
0.2012	0.6032	369.46
0.2004	0.5051	365.62
0.2007	0.4003	362.42
0.2000	0.3018	360.35
0.2005	0.2003	358.66
0.2000	0.1010	356.81
0.9514	0.8026	380.34
0.9502	0.7038	371.85
0.9504	0.6007	366.51
0.9504	0.5015	362.83
0.9505	0.4021	359.87
0.9500	0.3021	357.22
0.9506	0.2035	355.24
0.9503	0.1010	353.24

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Solvent: Mole fraction of Ethanol (2) - Liquid	Mass fraction of 1,2-Ethanediol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.1992	0.8035	385.08
0.2004	0.7012	375.23
0.2012	0.6032	369.46
0.2004	0.5051	365.62
0.2007	0.4003	362.42
0.2000	0.3018	360.35
0.2005	0.2003	358.66
0.2000	0.1010	356.81
0.9514	0.8026	380.34
0.9502	0.7038	371.85
0.9504	0.6007	366.51
0.9504	0.5015	362.83
0.9505	0.4021	359.87
0.9500	0.3021	357.22
0.9506	0.2035	355.24
0.9503	0.1010	353.24

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Water (3) - Liquid	x2[mol/mol] of 1,2-Ethanediol (1) - Liquid
353.45	0.1547	0.1319
355.45	0.1453	0.2419
355.65	0.1372	0.3356
356.35	0.1236	0.4873
358.05	0.1063	0.6640
359.85	0.0983	0.7502
362.25	0.2948	0.0374
362.25	0.2872	0.1069
362.75	0.2806	0.1633
362.15	0.2620	0.3100
363.05	0.2476	0.4199
364.45	0.2284	0.5463
371.65	0.2000	0.7264
375.45	0.1870	0.7967

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Water (3) - Liquid	x2[mol/mol] of 1,2-Ethanediol (1) - Liquid
369.15	0.0324	0.8676
363.15	0.0873	0.8127
358.15	0.1836	0.7164
357.65	0.2763	0.6237
355.15	0.3555	0.5445
353.65	0.4500	0.4500
353.65	0.4644	0.4356
353.35	0.5103	0.3897
353.05	0.6057	0.2943
352.65	0.6255	0.2745
352.25	0.7299	0.1701
352.15	0.8226	0.0774
351.65	0.8676	0.0324

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 323.15 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of Water (3) - Liquid	x2[mol/mol] of 1,2-Ethanediol (1) - Liquid
29.476	0.0000	0.0000
12.346	1.0000	0.0000
0.1160	0.0000	1.0000
26.812	0.4926	0.0204
26.145	0.4744	0.0510
25.049	0.4498	0.1006
23.903	0.4244	0.1513
22.707	0.3994	0.2014
21.574	0.3745	0.2512
20.358	0.3493	0.3015
19.132	0.3239	0.3523
17.903	0.2991	0.4019
16.637	0.2742	0.4517
15.333	0.2492	0.5016
13.768	0.0304	0.6487
14.012	0.0638	0.6264
14.467	0.1251	0.5853
14.895	0.1835	0.5462
15.289	0.2405	0.5081
15.665	0.2969	0.4704
16.024	0.3527	0.4331
16.34	0.4068	0.3968
16.617	0.4593	0.3618
16.851	0.5106	0.3274
17.015	0.5605	0.2941
21.87	0.0499	0.3137
22.156	0.1002	0.2971
22.362	0.1504	0.2805
22.567	0.2005	0.2640
22.739	0.2507	0.2474
22.875	0.3003	0.2310
23.049	0.3501	0.2146
23.075	0.4003	0.1980
23.097	0.4502	0.1815
23.059	0.4990	0.1654
9.145	0.6627	0.3266
10.572	0.6517	0.3211
12.712	0.6327	0.3118
14.515	0.6124	0.3018
16.089	0.5913	0.2914
17.428	0.5691	0.2804
18.59	0.5459	0.2690
19.621	0.5212	0.2568
20.552	0.4950	0.2439
21.748	0.4547	0.2241
22.188	0.4378	0.2157
4.88	0.3250	0.6595
6.407	0.3173	0.6438
8.693	0.3042	0.6172
10.644	0.2909	0.5904
12.36	0.2773	0.5627
13.89	0.2633	0.5344
15.264	0.2488	0.5050
16.507	0.2341	0.4750
17.655	0.2188	0.4440
18.638	0.2033	0.4125
19.773	0.1873	0.3800

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Phase equilibria for the ternary systems ethanol, water + ethylene glycol or + glycerol at 101.3 kPa
• Experimental and predicted refractive index properties in ternary mixtures of associated liquids
• Viscosity and density data for the ternary system water(1) ethanol(2) ethylene glycol(3) between 298.15 K and 328.15 K
• Experimental Measurement and Modeling of Vapor Liquid Equilibrium for the Ternary Systems Water + Ethanol + Ethylene Glycol, Water + 2-Propanol + Ethylene Glycol, and Water + 1-Propanol + Ethylene Glycol
• Isobaric Vapor-Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems