Mixture of Ethanol + Glycerin

Datasets

1. Activity coefficient (2)
2. Mole fraction (4)
3. η - Viscosity, Pa*s (2)
4. P_vap - Vapor or sublimation pressure, kPa (6)
5. n₀ - Refractive index (Na D-line) (2)
6. ρ_l - Mass density, kg/m3 (6)
7. c_sound,fluid - Speed of Sound, m/s (2)
8. γ - Surface tension liquid-gas, N/m (4)
9. T_boil - Boiling temperature at pressure P, K (8)

Activity coefficient of Ethanol (1) [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Mass fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of Ethanol (1) - Liquid
313.15	4.76
333.15	3.98
353.15	3.73
373.15	3.52
393.15	3.25

Activity coefficient of Ethanol (1) [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Mass fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of Ethanol (1) - Liquid
313.15	4.76
333.15	3.98
353.15	3.73
373.15	3.52
393.15	3.25

Mole fraction of Ethanol (1) [ref]

Fixed		Measured
Temperature, K - Gas	Pressure, kPa - Gas	Mole fraction of Ethanol (1) - Gas
543.00	6540.00	0.9850
573.00	4730.00	0.9999
573.00	5520.00	0.9999
573.00	6520.00	0.9830
573.00	7510.00	0.9590
573.00	8780.00	0.9310

Mole fraction of Ethanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Ethanol (1) - Liquid
493.00	2270.00	0.5400
493.00	2660.00	0.6630
493.00	2810.00	0.6980
493.00	3010.00	0.7660
493.00	3150.00	0.8330
493.00	3390.00	0.8890
523.00	2510.00	0.3460
523.00	3260.00	0.4550
523.00	3940.00	0.5910
523.00	4600.00	0.7410
523.00	5320.00	0.8790
543.00	3120.00	0.3160
543.00	3760.00	0.4140
543.00	4430.00	0.4950
543.00	5120.00	0.6030
543.00	5810.00	0.7000
543.00	6540.00	0.8090
573.00	4730.00	0.3640
573.00	5520.00	0.4360
573.00	6520.00	0.5310
573.00	7510.00	0.6340
573.00	8780.00	0.7730

Mole fraction of Ethanol (1) [ref]

Fixed		Measured
Temperature, K - Gas	Pressure, kPa - Gas	Mole fraction of Ethanol (1) - Gas
543.00	6540.00	0.9850
573.00	4730.00	0.9999
573.00	5520.00	0.9999
573.00	6520.00	0.9830
573.00	7510.00	0.9590
573.00	8780.00	0.9310

Mole fraction of Ethanol (1) [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Ethanol (1) - Liquid
493.00	2270.00	0.5400
493.00	2660.00	0.6630
493.00	2810.00	0.6980
493.00	3010.00	0.7660
493.00	3150.00	0.8330
493.00	3390.00	0.8890
523.00	2510.00	0.3460
523.00	3260.00	0.4550
523.00	3940.00	0.5910
523.00	4600.00	0.7410
523.00	5320.00	0.8790
543.00	3120.00	0.3160
543.00	3760.00	0.4140
543.00	4430.00	0.4950
543.00	5120.00	0.6030
543.00	5810.00	0.7000
543.00	6540.00	0.8090
573.00	4730.00	0.3640
573.00	5520.00	0.4360
573.00	6520.00	0.5310
573.00	7510.00	0.6340
573.00	8780.00	0.7730

Viscosity, Pa*s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 294 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Viscosity, Pa*s - Liquid
0.0000	1.39
0.0840	0.8005
0.1222	0.6279
0.1761	0.4500
0.2037	0.3851
0.2385	0.2700
0.2789	0.2205
0.3510	0.1414
0.4138	0.0807
0.4841	0.0540
0.5497	0.0315
0.6046	0.0203
0.6526	0.0167
0.7451	0.0091
0.7984	0.0052
0.8336	0.0041
0.8777	0.0030
0.9353	0.0019
0.9596	0.0015
1.0000	0.0012

Viscosity, Pa*s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 294 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Viscosity, Pa*s - Liquid
0.0000	1.39
0.0840	0.8005
0.1222	0.6279
0.1761	0.4500
0.2037	0.3851
0.2385	0.2700
0.2789	0.2205
0.3510	0.1414
0.4138	0.0807
0.4841	0.0540
0.5497	0.0315
0.6046	0.0203
0.6526	0.0167
0.7451	0.0091
0.7984	0.0052
0.8336	0.0041
0.8777	0.0030
0.9353	0.0019
0.9596	0.0015
1.0000	0.0012

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
273.15	0.0815	0.36
273.15	0.2000	0.74
273.15	0.3500	1.06
273.15	0.5001	1.22
273.15	0.6250	1.30
273.15	0.7500	1.43
273.15	0.8000	1.37
273.15	0.9000	1.44
273.15	1.0000	1.59
283.15	0.0815	0.68
283.15	0.2000	1.44
283.15	0.3500	2.07
283.15	0.5001	2.35
283.15	0.6250	2.52
283.15	0.7500	2.75
283.15	0.8000	2.68
283.15	0.9000	2.82
283.15	1.0000	3.14
293.15	0.0815	1.20
293.15	0.2000	2.63
293.15	0.3500	3.81
293.15	0.5001	4.28
293.15	0.6250	4.59
293.15	0.7500	5.00
293.15	0.8000	4.97
293.15	0.9000	5.25
293.15	1.0000	5.87
303.15	0.0815	2.05
303.15	0.2000	4.59
303.15	0.3500	6.67
303.15	0.5001	7.42
303.15	0.6250	7.96
303.15	0.7500	8.70
303.15	0.8000	8.81
303.15	0.9000	9.33
303.15	1.0000	10.47
313.15	0.0815	3.35
313.15	0.2000	7.66
313.15	0.3500	11.20
313.15	0.5001	12.34
313.15	0.6250	13.18
313.15	0.7500	14.52
313.15	0.8000	14.97
313.15	0.9000	15.92
313.15	1.0000	17.89
323.15	0.0815	5.30
323.15	0.2000	12.28
323.15	0.3500	18.07
323.15	0.5001	19.74
323.15	0.6250	20.98
323.15	0.7500	23.36
323.15	0.8000	24.52
323.15	0.9000	26.19
323.15	1.0000	29.44
333.15	0.0000	0.00
333.15	0.0815	8.12
333.15	0.2000	19.02
333.15	0.3500	28.17
333.15	0.5001	30.55
333.15	0.6250	32.24
333.15	0.7500	36.36
333.15	0.8000	38.84
333.15	0.9000	41.67
333.15	1.0000	46.91
343.15	0.0000	0.00
343.15	0.0815	12.10
343.15	0.2000	28.53
343.15	0.3500	42.59
343.15	0.5001	45.84
343.15	0.6250	48.03
343.15	0.7500	54.94
343.15	0.8000	59.71
343.15	0.9000	64.37
343.15	1.0000	72.22
353.15	0.0000	0.01
353.15	0.0815	17.58
353.15	0.2000	41.63
353.15	0.3500	62.61
353.15	0.5001	66.96
353.15	0.6250	69.58
353.15	0.7500	80.80
353.15	0.8000	89.32
353.15	0.9000	96.78
353.15	1.0000	108.35

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
423.15	0.5000	530.00
423.15	0.6000	590.00
423.15	0.7100	660.00
423.15	0.7800	730.00
423.15	0.8300	780.00
423.15	0.9100	1010.00
423.15	0.9700	780.00
448.15	0.5000	1010.00
448.15	0.6000	1180.00
448.15	0.7100	1300.00
448.15	0.7800	1400.00
448.15	0.8300	1420.00
448.15	0.9100	1580.00
448.15	0.9700	1550.00
473.15	0.5000	1420.00
473.15	0.6000	1810.00
473.15	0.7100	2080.00
473.15	0.7800	2250.00
473.15	0.8300	2270.00
473.15	0.9100	2820.00
473.15	0.9700	2810.00
498.15	0.5000	2420.00
498.15	0.6000	2790.00
498.15	0.7100	3220.00
498.15	0.7800	3450.00
498.15	0.8300	3480.00
498.15	0.9100	4370.00
498.15	0.9700	4360.00
523.15	0.5000	3600.00
523.15	0.6000	4290.00
523.15	0.7100	4820.00
523.15	0.7800	5390.00
523.15	0.8300	5440.00
523.15	0.9100	5240.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
323.15	0.1018	6.00
323.15	0.2005	10.53
323.15	0.3002	13.33
323.15	0.4013	16.27
323.15	0.5018	17.60
323.15	0.6008	19.73
323.15	0.6995	21.60
323.15	0.7999	23.73
323.15	0.8994	26.00
323.15	1.0000	29.44
333.15	0.1018	7.47
333.15	0.2005	13.20
333.15	0.3002	17.60
333.15	0.4013	23.33
333.15	0.5018	26.00
333.15	0.6008	30.66
333.15	0.6995	33.33
333.15	0.7999	37.60
333.15	0.8994	40.66
333.15	1.0000	46.86

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
273.15	0.0815	0.36
273.15	0.2000	0.74
273.15	0.3500	1.06
273.15	0.5001	1.22
273.15	0.6250	1.30
273.15	0.7500	1.43
273.15	0.8000	1.37
273.15	0.9000	1.44
273.15	1.0000	1.59
283.15	0.0815	0.68
283.15	0.2000	1.44
283.15	0.3500	2.07
283.15	0.5001	2.35
283.15	0.6250	2.52
283.15	0.7500	2.75
283.15	0.8000	2.68
283.15	0.9000	2.82
283.15	1.0000	3.14
293.15	0.0815	1.20
293.15	0.2000	2.63
293.15	0.3500	3.81
293.15	0.5001	4.28
293.15	0.6250	4.59
293.15	0.7500	5.00
293.15	0.8000	4.97
293.15	0.9000	5.25
293.15	1.0000	5.87
303.15	0.0815	2.05
303.15	0.2000	4.59
303.15	0.3500	6.67
303.15	0.5001	7.42
303.15	0.6250	7.96
303.15	0.7500	8.70
303.15	0.8000	8.81
303.15	0.9000	9.33
303.15	1.0000	10.47
313.15	0.0815	3.35
313.15	0.2000	7.66
313.15	0.3500	11.20
313.15	0.5001	12.34
313.15	0.6250	13.18
313.15	0.7500	14.52
313.15	0.8000	14.97
313.15	0.9000	15.92
313.15	1.0000	17.89
323.15	0.0815	5.30
323.15	0.2000	12.28
323.15	0.3500	18.07
323.15	0.5001	19.74
323.15	0.6250	20.98
323.15	0.7500	23.36
323.15	0.8000	24.52
323.15	0.9000	26.19
323.15	1.0000	29.44
333.15	0.0000	0.00
333.15	0.0815	8.12
333.15	0.2000	19.02
333.15	0.3500	28.17
333.15	0.5001	30.55
333.15	0.6250	32.24
333.15	0.7500	36.36
333.15	0.8000	38.84
333.15	0.9000	41.67
333.15	1.0000	46.91
343.15	0.0000	0.00
343.15	0.0815	12.10
343.15	0.2000	28.53
343.15	0.3500	42.59
343.15	0.5001	45.84
343.15	0.6250	48.03
343.15	0.7500	54.94
343.15	0.8000	59.71
343.15	0.9000	64.37
343.15	1.0000	72.22
353.15	0.0000	0.01
353.15	0.0815	17.58
353.15	0.2000	41.63
353.15	0.3500	62.61
353.15	0.5001	66.96
353.15	0.6250	69.58
353.15	0.7500	80.80
353.15	0.8000	89.32
353.15	0.9000	96.78
353.15	1.0000	108.35

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
423.15	0.5000	530.00
423.15	0.6000	590.00
423.15	0.7100	660.00
423.15	0.7800	730.00
423.15	0.8300	780.00
423.15	0.9100	1010.00
423.15	0.9700	780.00
448.15	0.5000	1010.00
448.15	0.6000	1180.00
448.15	0.7100	1300.00
448.15	0.7800	1400.00
448.15	0.8300	1420.00
448.15	0.9100	1580.00
448.15	0.9700	1550.00
473.15	0.5000	1420.00
473.15	0.6000	1810.00
473.15	0.7100	2080.00
473.15	0.7800	2250.00
473.15	0.8300	2270.00
473.15	0.9100	2820.00
473.15	0.9700	2810.00
498.15	0.5000	2420.00
498.15	0.6000	2790.00
498.15	0.7100	3220.00
498.15	0.7800	3450.00
498.15	0.8300	3480.00
498.15	0.9100	4370.00
498.15	0.9700	4360.00
523.15	0.5000	3600.00
523.15	0.6000	4290.00
523.15	0.7100	4820.00
523.15	0.7800	5390.00
523.15	0.8300	5440.00
523.15	0.9100	5240.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
323.15	0.1018	6.00
323.15	0.2005	10.53
323.15	0.3002	13.33
323.15	0.4013	16.27
323.15	0.5018	17.60
323.15	0.6008	19.73
323.15	0.6995	21.60
323.15	0.7999	23.73
323.15	0.8994	26.00
323.15	1.0000	29.44
333.15	0.1018	7.47
333.15	0.2005	13.20
333.15	0.3002	17.60
333.15	0.4013	23.33
333.15	0.5018	26.00
333.15	0.6008	30.66
333.15	0.6995	33.33
333.15	0.7999	37.60
333.15	0.8994	40.66
333.15	1.0000	46.86

Refractive index (Na D-line) [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 294 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.474
0.0840	1.468
0.1222	1.466
0.1761	1.4619
0.2037	1.4592
0.2385	1.4562
0.2789	1.4528
0.3510	1.447
0.4138	1.4392
0.4841	1.4326
0.5497	1.4253
0.6046	1.4179
0.6526	1.4131
0.7451	1.4016
0.7984	1.3934
0.8336	1.3885
0.8777	1.3815
0.9353	1.3727
0.9596	1.3681
1.0000	1.3618

Refractive index (Na D-line) [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 294 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.474
0.0840	1.468
0.1222	1.466
0.1761	1.4619
0.2037	1.4592
0.2385	1.4562
0.2789	1.4528
0.3510	1.447
0.4138	1.4392
0.4841	1.4326
0.5497	1.4253
0.6046	1.4179
0.6526	1.4131
0.7451	1.4016
0.7984	1.3934
0.8336	1.3885
0.8777	1.3815
0.9353	1.3727
0.9596	1.3681
1.0000	1.3618

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 91.2 (Liquid)
• Temperature, K = 303.15 (Liquid)

Mass fraction of Glycerin (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	781.0
0.1529	835.0
0.2901	888.0
0.4124	939.0
0.5159	985.0
0.6211	1036.0
0.7096	1084.0
0.7971	1136.0
0.8690	1174.0
0.9357	1215.0
1.0000	1255.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	1267.0
283.15	0.0999	1233.0
283.15	0.2002	1199.0
283.15	0.2998	1161.0
283.15	0.4001	1120.0
283.15	0.4993	1077.0
283.15	0.6004	1029.0
283.15	0.6990	978.0
283.15	0.9002	862.0
283.15	1.0000	798.0
293.15	0.0000	1261.0
293.15	0.0999	1227.0
293.15	0.2002	1193.0
293.15	0.2998	1155.0
293.15	0.4001	1113.0
293.15	0.4993	1069.0
293.15	0.6004	1021.0
293.15	0.6990	970.0
293.15	0.9002	854.0
293.15	1.0000	790.0
303.15	0.0000	1255.0
303.15	0.0999	1220.0
303.15	0.2002	1186.0
303.15	0.2998	1148.0
303.15	0.4001	1106.0
303.15	0.4993	1062.0
303.15	0.6004	1014.0
303.15	0.6990	963.0
303.15	0.9002	845.0
303.15	1.0000	781.0
313.15	0.0000	1248.0
313.15	0.0999	1214.0
313.15	0.2002	1179.0
313.15	0.2998	1140.0
313.15	0.4001	1099.0
313.15	0.4993	1055.0
313.15	0.6004	1006.0
313.15	0.6990	955.0
313.15	0.9002	837.0
313.15	1.0000	772.0

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 294 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	1261.51
0.0840	1233.48
0.1222	1220.3
0.1761	1201.19
0.2037	1191.35
0.2385	1178.37
0.2789	1162.98
0.3510	1134.3
0.4138	1108.32
0.4841	1077.53
0.5497	1047.03
0.6046	1020.27
0.6526	995.96
0.7451	946.41
0.7984	916.05
0.8336	895.63
0.8777	868.79
0.9353	832.89
0.9596	816.85
1.0000	789.91

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 91.2 (Liquid)
• Temperature, K = 303.15 (Liquid)

Mass fraction of Glycerin (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	781.0
0.1529	835.0
0.2901	888.0
0.4124	939.0
0.5159	985.0
0.6211	1036.0
0.7096	1084.0
0.7971	1136.0
0.8690	1174.0
0.9357	1215.0
1.0000	1255.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	1267.0
283.15	0.0999	1233.0
283.15	0.2002	1199.0
283.15	0.2998	1161.0
283.15	0.4001	1120.0
283.15	0.4993	1077.0
283.15	0.6004	1029.0
283.15	0.6990	978.0
283.15	0.9002	862.0
283.15	1.0000	798.0
293.15	0.0000	1261.0
293.15	0.0999	1227.0
293.15	0.2002	1193.0
293.15	0.2998	1155.0
293.15	0.4001	1113.0
293.15	0.4993	1069.0
293.15	0.6004	1021.0
293.15	0.6990	970.0
293.15	0.9002	854.0
293.15	1.0000	790.0
303.15	0.0000	1255.0
303.15	0.0999	1220.0
303.15	0.2002	1186.0
303.15	0.2998	1148.0
303.15	0.4001	1106.0
303.15	0.4993	1062.0
303.15	0.6004	1014.0
303.15	0.6990	963.0
303.15	0.9002	845.0
303.15	1.0000	781.0
313.15	0.0000	1248.0
313.15	0.0999	1214.0
313.15	0.2002	1179.0
313.15	0.2998	1140.0
313.15	0.4001	1099.0
313.15	0.4993	1055.0
313.15	0.6004	1006.0
313.15	0.6990	955.0
313.15	0.9002	837.0
313.15	1.0000	772.0

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 294 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	1261.51
0.0840	1233.48
0.1222	1220.3
0.1761	1201.19
0.2037	1191.35
0.2385	1178.37
0.2789	1162.98
0.3510	1134.3
0.4138	1108.32
0.4841	1077.53
0.5497	1047.03
0.6046	1020.27
0.6526	995.96
0.7451	946.41
0.7984	916.05
0.8336	895.63
0.8777	868.79
0.9353	832.89
0.9596	816.85
1.0000	789.91

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Speed of sound, m/s - Liquid
283.15	0.0000	1942.3
283.15	0.0999	1882.1
283.15	0.2002	1804.3
283.15	0.2998	1721.8
283.15	0.4001	1639.2
283.15	0.4993	1557.7
283.15	0.6004	1476.1
283.15	0.6990	1401.7
283.15	0.9002	1263.5
283.15	1.0000	1196.8
293.15	0.0000	1922.9
293.15	0.0999	1852.5
293.15	0.2002	1778.9
293.15	0.2998	1696.1
293.15	0.4001	1613.3
293.15	0.4993	1530.9
293.15	0.6004	1448.4
293.15	0.6990	1372.8
293.15	0.9002	1231.4
293.15	1.0000	1162.3
303.15	0.0000	1901.0
303.15	0.0999	1827.9
303.15	0.2002	1753.4
303.15	0.2998	1671.4
303.15	0.4001	1587.9
303.15	0.4993	1504.6
303.15	0.6004	1421.1
303.15	0.6990	1344.2
303.15	0.9002	1199.4
303.15	1.0000	1128.2
313.15	0.0000	1879.3
313.15	0.0999	1804.6
313.15	0.2002	1729.7
313.15	0.2998	1647.2
313.15	0.4001	1562.8
313.15	0.4993	1478.5
313.15	0.6004	1394.0
313.15	0.6990	1315.8
313.15	0.9002	1167.7
313.15	1.0000	1094.5

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Speed of sound, m/s - Liquid
283.15	0.0000	1942.3
283.15	0.0999	1882.1
283.15	0.2002	1804.3
283.15	0.2998	1721.8
283.15	0.4001	1639.2
283.15	0.4993	1557.7
283.15	0.6004	1476.1
283.15	0.6990	1401.7
283.15	0.9002	1263.5
283.15	1.0000	1196.8
293.15	0.0000	1922.9
293.15	0.0999	1852.5
293.15	0.2002	1778.9
293.15	0.2998	1696.1
293.15	0.4001	1613.3
293.15	0.4993	1530.9
293.15	0.6004	1448.4
293.15	0.6990	1372.8
293.15	0.9002	1231.4
293.15	1.0000	1162.3
303.15	0.0000	1901.0
303.15	0.0999	1827.9
303.15	0.2002	1753.4
303.15	0.2998	1671.4
303.15	0.4001	1587.9
303.15	0.4993	1504.6
303.15	0.6004	1421.1
303.15	0.6990	1344.2
303.15	0.9002	1199.4
303.15	1.0000	1128.2
313.15	0.0000	1879.3
313.15	0.0999	1804.6
313.15	0.2002	1729.7
313.15	0.2998	1647.2
313.15	0.4001	1562.8
313.15	0.4993	1478.5
313.15	0.6004	1394.0
313.15	0.6990	1315.8
313.15	0.9002	1167.7
313.15	1.0000	1094.5

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
293.20	0.0000	0.0631
293.20	0.1000	0.0529
293.20	0.2000	0.0417
293.20	0.3000	0.0361
293.20	0.4000	0.0319
293.20	0.5000	0.0290
293.20	0.6000	0.0275
293.20	0.7000	0.0262
293.20	0.8000	0.0249
293.20	0.9000	0.0237
293.20	1.0000	0.0223
303.20	0.0000	0.0624
303.20	0.1000	0.0524
303.20	0.2000	0.0414
303.20	0.3000	0.0359
303.20	0.4000	0.0316
303.20	0.5000	0.0285
303.20	0.6000	0.0271
303.20	0.7000	0.0254
303.20	0.8000	0.0242
303.20	0.9000	0.0232
303.20	1.0000	0.0214
313.20	0.0000	0.0620
313.20	0.1000	0.0520
313.20	0.2000	0.0411
313.20	0.3000	0.0357
313.20	0.4000	0.0312
313.20	0.5000	0.0279
313.20	0.6000	0.0267
313.20	0.7000	0.0245
313.20	0.8000	0.0235
313.20	0.9000	0.0226
313.20	1.0000	0.0206
323.20	0.0000	0.0611
323.20	0.1000	0.0515
323.20	0.2000	0.0407
323.20	0.3000	0.0354
323.20	0.4000	0.0309
323.20	0.5000	0.0277
323.20	0.6000	0.0263
323.20	0.7000	0.0236
323.20	0.8000	0.0228
323.20	0.9000	0.0220
323.20	1.0000	0.0198
333.20	0.0000	0.0605
333.20	0.1000	0.0511
333.20	0.2000	0.0405
333.20	0.3000	0.0350
333.20	0.4000	0.0306
333.20	0.5000	0.0272
333.20	0.6000	0.0259
333.20	0.7000	0.0227
333.20	0.8000	0.0221
333.20	0.9000	0.0212
333.20	1.0000	0.0190

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 294 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.0000	0.0631
0.0840	0.0520
0.1222	0.0488
0.1761	0.0430
0.2037	0.0417
0.2385	0.0394
0.2789	0.0358
0.3510	0.0332
0.4138	0.0297
0.4841	0.0285
0.5497	0.0271
0.6046	0.0251
0.6526	0.0243
0.7451	0.0235
0.7984	0.0235
0.8336	0.0230
0.8777	0.0225
0.9353	0.0224
0.9596	0.0223
1.0000	0.0222

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
293.20	0.0000	0.0631
293.20	0.1000	0.0529
293.20	0.2000	0.0417
293.20	0.3000	0.0361
293.20	0.4000	0.0319
293.20	0.5000	0.0290
293.20	0.6000	0.0275
293.20	0.7000	0.0262
293.20	0.8000	0.0249
293.20	0.9000	0.0237
293.20	1.0000	0.0223
303.20	0.0000	0.0624
303.20	0.1000	0.0524
303.20	0.2000	0.0414
303.20	0.3000	0.0359
303.20	0.4000	0.0316
303.20	0.5000	0.0285
303.20	0.6000	0.0271
303.20	0.7000	0.0254
303.20	0.8000	0.0242
303.20	0.9000	0.0232
303.20	1.0000	0.0214
313.20	0.0000	0.0620
313.20	0.1000	0.0520
313.20	0.2000	0.0411
313.20	0.3000	0.0357
313.20	0.4000	0.0312
313.20	0.5000	0.0279
313.20	0.6000	0.0267
313.20	0.7000	0.0245
313.20	0.8000	0.0235
313.20	0.9000	0.0226
313.20	1.0000	0.0206
323.20	0.0000	0.0611
323.20	0.1000	0.0515
323.20	0.2000	0.0407
323.20	0.3000	0.0354
323.20	0.4000	0.0309
323.20	0.5000	0.0277
323.20	0.6000	0.0263
323.20	0.7000	0.0236
323.20	0.8000	0.0228
323.20	0.9000	0.0220
323.20	1.0000	0.0198
333.20	0.0000	0.0605
333.20	0.1000	0.0511
333.20	0.2000	0.0405
333.20	0.3000	0.0350
333.20	0.4000	0.0306
333.20	0.5000	0.0272
333.20	0.6000	0.0259
333.20	0.7000	0.0227
333.20	0.8000	0.0221
333.20	0.9000	0.0212
333.20	1.0000	0.0190

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 294 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.0000	0.0631
0.0840	0.0520
0.1222	0.0488
0.1761	0.0430
0.2037	0.0417
0.2385	0.0394
0.2789	0.0358
0.3510	0.0332
0.4138	0.0297
0.4841	0.0285
0.5497	0.0271
0.6046	0.0251
0.6526	0.0243
0.7451	0.0235
0.7984	0.0235
0.8336	0.0230
0.8777	0.0225
0.9353	0.0224
0.9596	0.0223
1.0000	0.0222

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0107	453.99
0.0168	438.00
0.0244	427.23
0.0541	416.50
0.0759	406.82
0.0902	399.89
0.1114	392.95
0.1321	388.91
0.1646	385.67
0.1791	382.72
0.1974	379.88
0.2229	377.68
0.2479	376.19
0.2902	372.84
0.3149	369.90
0.3434	366.25
0.3546	368.10
0.4246	364.91
0.4493	364.21
0.4754	363.51

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Ethanol (1) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0537	24.00	359.09
0.0537	34.20	369.74
0.0537	44.50	377.58
0.0537	54.60	384.33
0.0537	64.60	390.62
0.0537	74.70	397.52
0.0537	91.30	405.61
0.1029	18.30	344.25
0.1029	24.20	350.80
0.1029	34.30	360.09
0.1029	44.40	367.44
0.1029	54.40	373.28
0.1029	64.40	378.43
0.1029	74.60	382.98
0.1029	91.50	389.22
0.2575	23.80	337.76
0.2575	34.10	345.50
0.2575	44.20	353.00
0.2575	54.50	358.44
0.2575	64.60	363.64
0.2575	74.60	365.99
0.2575	91.80	371.69
0.2643	18.30	332.31
0.2643	24.20	338.46
0.2643	34.30	346.25
0.2643	44.50	353.50
0.2643	54.60	358.34
0.2643	64.60	362.84
0.2643	74.80	367.19
0.2643	92.00	373.58
0.3594	24.30	334.21
0.3594	34.10	341.10
0.3594	44.50	346.75
0.3594	54.40	351.90
0.3594	64.60	356.19
0.3594	74.70	360.24
0.3594	91.70	365.94
0.4173	18.70	324.51
0.4173	24.00	330.46
0.4173	34.30	338.66
0.4173	44.30	344.90
0.4173	54.40	349.65
0.4173	64.50	353.90
0.4173	74.60	357.84
0.4173	91.60	363.49
0.4790	18.80	322.02
0.4790	24.00	327.11
0.4790	34.30	335.36
0.4790	44.40	342.00
0.4790	54.40	347.20
0.4790	64.30	351.65
0.4790	74.80	355.60
0.4790	92.10	361.14
0.5525	18.70	321.12
0.5525	24.10	326.56
0.5525	34.10	334.41
0.5525	44.30	340.75
0.5525	54.40	345.70
0.5525	64.50	350.00
0.5525	74.60	353.90
0.5525	91.30	359.34
0.6505	18.70	320.42
0.6505	23.90	325.56
0.6505	34.00	333.51
0.6505	44.40	339.70
0.6505	54.40	344.70
0.6505	64.50	348.95
0.6505	74.80	352.70
0.6505	91.40	358.04

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mass fraction of Ethanol (1) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	6.70	477.25
0.0500	6.70	335.95
0.0750	6.70	327.35
0.1000	6.70	319.55
0.2000	6.70	307.85
0.3000	6.70	302.55
0.4000	6.70	299.85
0.5000	6.70	298.65
0.6000	6.70	297.75
0.7000	6.70	296.95
0.8000	6.70	296.35
0.9000	6.70	295.75
1.0000	6.70	295.25
0.0000	13.30	493.35
0.0500	13.30	352.65
0.0750	13.30	341.65
0.1000	13.30	334.25
0.2000	13.30	321.55
0.3000	13.30	315.35
0.4000	13.30	312.45
0.5000	13.30	311.25
0.6000	13.30	310.25
0.7000	13.30	309.35
0.8000	13.30	308.55
0.9000	13.30	307.95
1.0000	13.30	307.45
0.0000	20.00	505.55
0.0500	20.00	362.85
0.0750	20.00	351.65
0.1000	20.00	343.75
0.2000	20.00	329.85
0.3000	20.00	323.45
0.4000	20.00	320.45
0.5000	20.00	319.25
0.6000	20.00	318.25
0.7000	20.00	317.35
0.8000	20.00	316.45
0.9000	20.00	315.75
1.0000	20.00	315.05
0.0000	26.70	513.95
0.0500	26.70	370.75
0.0750	26.70	359.65
0.1000	26.70	350.55
0.2000	26.70	336.05
0.3000	26.70	329.35
0.4000	26.70	326.65
0.5000	26.70	325.35
0.6000	26.70	324.35
0.7000	26.70	323.45
0.8000	26.70	322.55
0.9000	26.70	321.75
1.0000	26.70	321.05
0.0000	33.30	520.65
0.0500	33.30	376.75
0.0750	33.30	365.95
0.1000	33.30	355.85
0.2000	33.30	341.65
0.3000	33.30	334.75
0.4000	33.30	331.55
0.5000	33.30	330.15
0.6000	33.30	329.15
0.7000	33.30	328.05
0.8000	33.30	327.15
0.9000	33.30	326.35
1.0000	33.30	325.65
0.0500	40.00	382.35
0.0750	40.00	371.35
0.1000	40.00	360.85
0.2000	40.00	346.45
0.3000	40.00	338.95
0.4000	40.00	335.65
0.5000	40.00	334.25
0.6000	40.00	333.15
0.7000	40.00	332.05
0.8000	40.00	331.15
0.9000	40.00	330.25
1.0000	40.00	329.55
0.0500	46.70	386.45
0.0750	46.70	375.65
0.1000	46.70	364.85
0.2000	46.70	348.75
0.3000	46.70	342.55
0.4000	46.70	339.35
0.5000	46.70	337.85
0.6000	46.70	336.65
0.7000	46.70	335.55
0.8000	46.70	334.55
0.9000	46.70	333.65
1.0000	46.70	332.85
0.0500	53.30	390.45
0.0750	53.30	379.25
0.1000	53.30	368.95
0.2000	53.30	352.85
0.3000	53.30	345.55
0.4000	53.30	342.65
0.5000	53.30	341.05
0.6000	53.30	339.85
0.7000	53.30	338.65
0.8000	53.30	337.65
0.9000	53.30	336.75
1.0000	53.30	335.95
0.0500	60.00	394.55
0.0750	60.00	382.95
0.1000	60.00	372.45
0.2000	60.00	355.95
0.3000	60.00	348.55
0.4000	60.00	345.55
0.5000	60.00	343.85
0.6000	60.00	342.65
0.7000	60.00	341.45
0.8000	60.00	340.45
0.9000	60.00	339.55
1.0000	60.00	338.65
0.0500	66.70	397.85
0.0750	66.70	385.95
0.1000	66.70	375.85
0.2000	66.70	359.25
0.3000	66.70	351.35
0.4000	66.70	348.35
0.5000	66.70	346.55
0.6000	66.70	345.35
0.7000	66.70	344.15
0.8000	66.70	343.05
0.9000	66.70	342.05
1.0000	66.70	341.15

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 91.2 (Liquid)

Mass fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.8328	351.05
0.7641	351.95
0.7229	352.75
0.6469	353.75
0.5442	354.55
0.4461	355.45
0.3675	357.65
0.2620	360.85
0.1748	366.75
0.1058	378.55
0.0801	384.75
0.0413	406.95
0.0360	417.55
0.0235	429.75
0.0207	435.85
0.0186	443.25

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0107	453.99
0.0168	438.00
0.0244	427.23
0.0541	416.50
0.0759	406.82
0.0902	399.89
0.1114	392.95
0.1321	388.91
0.1646	385.67
0.1791	382.72
0.1974	379.88
0.2229	377.68
0.2479	376.19
0.2902	372.84
0.3149	369.90
0.3434	366.25
0.3546	368.10
0.4246	364.91
0.4493	364.21
0.4754	363.51

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Ethanol (1) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0537	24.00	359.09
0.0537	34.20	369.74
0.0537	44.50	377.58
0.0537	54.60	384.33
0.0537	64.60	390.62
0.0537	74.70	397.52
0.0537	91.30	405.61
0.1029	18.30	344.25
0.1029	24.20	350.80
0.1029	34.30	360.09
0.1029	44.40	367.44
0.1029	54.40	373.28
0.1029	64.40	378.43
0.1029	74.60	382.98
0.1029	91.50	389.22
0.2575	23.80	337.76
0.2575	34.10	345.50
0.2575	44.20	353.00
0.2575	54.50	358.44
0.2575	64.60	363.64
0.2575	74.60	365.99
0.2575	91.80	371.69
0.2643	18.30	332.31
0.2643	24.20	338.46
0.2643	34.30	346.25
0.2643	44.50	353.50
0.2643	54.60	358.34
0.2643	64.60	362.84
0.2643	74.80	367.19
0.2643	92.00	373.58
0.3594	24.30	334.21
0.3594	34.10	341.10
0.3594	44.50	346.75
0.3594	54.40	351.90
0.3594	64.60	356.19
0.3594	74.70	360.24
0.3594	91.70	365.94
0.4173	18.70	324.51
0.4173	24.00	330.46
0.4173	34.30	338.66
0.4173	44.30	344.90
0.4173	54.40	349.65
0.4173	64.50	353.90
0.4173	74.60	357.84
0.4173	91.60	363.49
0.4790	18.80	322.02
0.4790	24.00	327.11
0.4790	34.30	335.36
0.4790	44.40	342.00
0.4790	54.40	347.20
0.4790	64.30	351.65
0.4790	74.80	355.60
0.4790	92.10	361.14
0.5525	18.70	321.12
0.5525	24.10	326.56
0.5525	34.10	334.41
0.5525	44.30	340.75
0.5525	54.40	345.70
0.5525	64.50	350.00
0.5525	74.60	353.90
0.5525	91.30	359.34
0.6505	18.70	320.42
0.6505	23.90	325.56
0.6505	34.00	333.51
0.6505	44.40	339.70
0.6505	54.40	344.70
0.6505	64.50	348.95
0.6505	74.80	352.70
0.6505	91.40	358.04

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mass fraction of Ethanol (1) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	6.70	477.25
0.0500	6.70	335.95
0.0750	6.70	327.35
0.1000	6.70	319.55
0.2000	6.70	307.85
0.3000	6.70	302.55
0.4000	6.70	299.85
0.5000	6.70	298.65
0.6000	6.70	297.75
0.7000	6.70	296.95
0.8000	6.70	296.35
0.9000	6.70	295.75
1.0000	6.70	295.25
0.0000	13.30	493.35
0.0500	13.30	352.65
0.0750	13.30	341.65
0.1000	13.30	334.25
0.2000	13.30	321.55
0.3000	13.30	315.35
0.4000	13.30	312.45
0.5000	13.30	311.25
0.6000	13.30	310.25
0.7000	13.30	309.35
0.8000	13.30	308.55
0.9000	13.30	307.95
1.0000	13.30	307.45
0.0000	20.00	505.55
0.0500	20.00	362.85
0.0750	20.00	351.65
0.1000	20.00	343.75
0.2000	20.00	329.85
0.3000	20.00	323.45
0.4000	20.00	320.45
0.5000	20.00	319.25
0.6000	20.00	318.25
0.7000	20.00	317.35
0.8000	20.00	316.45
0.9000	20.00	315.75
1.0000	20.00	315.05
0.0000	26.70	513.95
0.0500	26.70	370.75
0.0750	26.70	359.65
0.1000	26.70	350.55
0.2000	26.70	336.05
0.3000	26.70	329.35
0.4000	26.70	326.65
0.5000	26.70	325.35
0.6000	26.70	324.35
0.7000	26.70	323.45
0.8000	26.70	322.55
0.9000	26.70	321.75
1.0000	26.70	321.05
0.0000	33.30	520.65
0.0500	33.30	376.75
0.0750	33.30	365.95
0.1000	33.30	355.85
0.2000	33.30	341.65
0.3000	33.30	334.75
0.4000	33.30	331.55
0.5000	33.30	330.15
0.6000	33.30	329.15
0.7000	33.30	328.05
0.8000	33.30	327.15
0.9000	33.30	326.35
1.0000	33.30	325.65
0.0500	40.00	382.35
0.0750	40.00	371.35
0.1000	40.00	360.85
0.2000	40.00	346.45
0.3000	40.00	338.95
0.4000	40.00	335.65
0.5000	40.00	334.25
0.6000	40.00	333.15
0.7000	40.00	332.05
0.8000	40.00	331.15
0.9000	40.00	330.25
1.0000	40.00	329.55
0.0500	46.70	386.45
0.0750	46.70	375.65
0.1000	46.70	364.85
0.2000	46.70	348.75
0.3000	46.70	342.55
0.4000	46.70	339.35
0.5000	46.70	337.85
0.6000	46.70	336.65
0.7000	46.70	335.55
0.8000	46.70	334.55
0.9000	46.70	333.65
1.0000	46.70	332.85
0.0500	53.30	390.45
0.0750	53.30	379.25
0.1000	53.30	368.95
0.2000	53.30	352.85
0.3000	53.30	345.55
0.4000	53.30	342.65
0.5000	53.30	341.05
0.6000	53.30	339.85
0.7000	53.30	338.65
0.8000	53.30	337.65
0.9000	53.30	336.75
1.0000	53.30	335.95
0.0500	60.00	394.55
0.0750	60.00	382.95
0.1000	60.00	372.45
0.2000	60.00	355.95
0.3000	60.00	348.55
0.4000	60.00	345.55
0.5000	60.00	343.85
0.6000	60.00	342.65
0.7000	60.00	341.45
0.8000	60.00	340.45
0.9000	60.00	339.55
1.0000	60.00	338.65
0.0500	66.70	397.85
0.0750	66.70	385.95
0.1000	66.70	375.85
0.2000	66.70	359.25
0.3000	66.70	351.35
0.4000	66.70	348.35
0.5000	66.70	346.55
0.6000	66.70	345.35
0.7000	66.70	344.15
0.8000	66.70	343.05
0.9000	66.70	342.05
1.0000	66.70	341.15

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 91.2 (Liquid)

Mass fraction of Ethanol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.8328	351.05
0.7641	351.95
0.7229	352.75
0.6469	353.75
0.5442	354.55
0.4461	355.45
0.3675	357.65
0.2620	360.85
0.1748	366.75
0.1058	378.55
0.0801	384.75
0.0413	406.95
0.0360	417.55
0.0235	429.75
0.0207	435.85
0.0186	443.25

Sources

• Phase equilibria of glycerol containing systems and their description with the Cubic-Plus-Association (CPA) Equation of State
• Measurement and calculation of vapor liquid equilibria for methanol + glycerol and ethanol + glycerol systems at 493 573K
• (Vapor + liquid) equilibrium for the binary systems {water + glycerol} and {ethanol + glycerol, ethyl stearate, and ethyl palmitate} at low pressures
• Thermophysical properties of biodiesel and related systems. Part I. Vapour liquid equilibrium at low pressures of binary and ternary systems involving methanol, ethanol, glycerol, water and NaCl
• (Vapor-liquid) equilibria and excess Gibbs free energy functions of (ethanol + glycerol), or (water + glycerol) binary mixtures at several temperatures
• NaCl and KCl effect on (vapour + liquid) equilibrium of binary, ternary and quaternary systems involving water, ethanol and glycerol at low pressures
• Effect of temperature on density, sound velocity, and their derived properties for the binary systems glycerol with water or alcohols
• Experimental and modeling vapor-liquid equilibrium for the binary systems {ethanol(1) + glycerol(2)} and {tert-butanol(1) + glycerol(2)} at high pressures
• Surface tension and interfacial compositions of binary glycerol/alcohol mixtures
• Vapor Liquid Equilibrium of Water + Ethanol + Glycerol: Experimental Measurement and Modeling for Ethanol Dehydration by Extractive Distillation
• Isothermal Vapor Liquid Equilibrium of Ethanol + Glycerol and 2-Propanol + Glycerol at Different Temperatures
• Physical Properties (Density, Excess Molar Volume, Viscosity, Surface Tension, and Refractive Index) of Ethanol + Glycerol