Mixture of 1,2-Ethanediol + Water

Datasets

1. Mole fraction (4)
2. C_p,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
3. η - Viscosity, Pa*s (12)
4. Excess molar heat capacity, J/K/mol (4)
5. P_vap - Vapor or sublimation pressure, kPa (6)
6. n₀ - Refractive index (Na D-line) (2)
7. ρ_l - Mass density, kg/m3 (28)
8. c_sound,fluid - Speed of Sound, m/s (14)
9. γ - Surface tension liquid-gas, N/m (8)
10. T_boil - Boiling temperature at pressure P, K (6)
11. λ - Thermal conductivity, W/m/K (2)
12. Binary diffusion coefficient, m2/s (10)
13. Vapor Liquid Equilibrium at Constant Pressure (3)
14. v_spec - Specific volume, m3/kg (4)
15. Excess molar volume, m3/mol (4)

Mole fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Water (2) - Liquid	Mole fraction of Water (2) - Gas
0.1792	0.8263
0.2468	0.8918
0.3181	0.9303
0.3805	0.9496
0.4451	0.9631
0.5845	0.9819

Mole fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Water (2) - Liquid	Mole fraction of Water (2) - Gas
0.0200	0.2270
0.0630	0.5270
0.1040	0.6810
0.1280	0.7420
0.1670	0.8100
0.1970	0.8480
0.2500	0.8920
0.2790	0.9100
0.3170	0.9280
0.3460	0.9390
0.4090	0.9560
0.4440	0.9640
0.5010	0.9730
0.5570	0.9800
0.6740	0.9890
0.7470	0.9930
0.7970	0.9950
0.8610	0.9970
0.9000	0.9980

Mole fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Water (2) - Liquid	Mole fraction of Water (2) - Gas
0.1792	0.8263
0.2468	0.8918
0.3181	0.9303
0.3805	0.9496
0.4451	0.9631
0.5845	0.9819

Mole fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Water (2) - Liquid	Mole fraction of Water (2) - Gas
0.0200	0.2270
0.0630	0.5270
0.1040	0.6810
0.1280	0.7420
0.1670	0.8100
0.1970	0.8480
0.2500	0.8920
0.2790	0.9100
0.3170	0.9280
0.3460	0.9390
0.4090	0.9560
0.4440	0.9640
0.5010	0.9730
0.5570	0.9800
0.6740	0.9890
0.7470	0.9930
0.7970	0.9950
0.8610	0.9970
0.9000	0.9980

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
0.1105	293.15	86.70
0.1105	303.15	87.05
0.1105	313.15	87.48
0.1105	323.15	87.53
0.1105	333.15	87.76
0.1105	343.15	88.31
0.1105	353.15	88.97
0.1105	363.15	89.27
0.1105	373.15	89.52
0.1620	293.15	89.39
0.1620	303.15	89.67
0.1620	313.15	90.47
0.1620	323.15	91.00
0.1620	333.15	91.50
0.1620	343.15	92.56
0.1620	353.15	92.31
0.1620	363.15	93.51
0.1620	373.15	93.89
0.2248	293.15	93.61
0.2248	303.15	94.42
0.2248	313.15	94.89
0.2248	323.15	95.93
0.2248	333.15	96.60
0.2248	343.15	97.46
0.2248	353.15	98.61
0.2248	363.15	99.61
0.2248	373.15	100.23
0.3031	293.15	98.37
0.3031	303.15	99.15
0.3031	313.15	100.31
0.3031	323.15	101.88
0.3031	333.15	102.38
0.3031	343.15	103.64
0.3031	353.15	104.99
0.3031	363.15	106.52
0.3031	373.15	107.47
0.4036	293.15	104.66
0.4036	303.15	105.99
0.4036	313.15	108.06
0.4036	323.15	109.53
0.4036	333.15	111.00
0.4036	343.15	111.93
0.4036	353.15	113.83
0.4036	363.15	115.04
0.4036	373.15	116.01
0.5370	293.15	114.30
0.5370	303.15	115.72
0.5370	313.15	117.68
0.5370	323.15	119.76
0.5370	333.15	121.18
0.5370	343.15	122.85
0.5370	353.15	124.97
0.5370	363.15	126.81
0.5370	373.15	128.22
0.7230	293.15	127.90
0.7230	303.15	129.45
0.7230	313.15	131.20
0.7230	323.15	133.39
0.7230	333.15	135.38
0.7230	343.15	138.08
0.7230	353.15	140.57
0.7230	363.15	142.17
0.7230	373.15	144.36
1.0000	293.15	147.47
1.0000	303.15	149.71
1.0000	313.15	152.00
1.0000	323.15	153.80
1.0000	333.15	156.22
1.0000	343.15	159.70
1.0000	353.15	161.00
1.0000	363.15	164.98
1.0000	373.15	168.45
0.0000	293.15	75.29
0.0000	303.15	75.38
0.0000	313.15	75.21
0.0000	323.15	75.23
0.0000	333.15	75.21
0.0000	343.15	75.32
0.0000	353.15	75.48
0.0312	293.15	88.03
0.0312	303.15	87.89
0.0312	313.15	88.36
0.0312	323.15	88.63
0.0312	333.15	88.80
0.0312	343.15	88.88
0.0312	353.15	89.15
0.0312	363.15	89.25
0.0676	293.15	87.60
0.0676	303.15	87.81
0.0676	313.15	88.19
0.0676	323.15	88.59
0.0676	333.15	88.99
0.0676	343.15	89.10
0.0676	353.15	89.47
0.0676	363.15	89.60

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
0.1105	293.15	86.70
0.1105	303.15	87.05
0.1105	313.15	87.48
0.1105	323.15	87.53
0.1105	333.15	87.76
0.1105	343.15	88.31
0.1105	353.15	88.97
0.1105	363.15	89.27
0.1105	373.15	89.52
0.1620	293.15	89.39
0.1620	303.15	89.67
0.1620	313.15	90.47
0.1620	323.15	91.00
0.1620	333.15	91.50
0.1620	343.15	92.56
0.1620	353.15	92.31
0.1620	363.15	93.51
0.1620	373.15	93.89
0.2248	293.15	93.61
0.2248	303.15	94.42
0.2248	313.15	94.89
0.2248	323.15	95.93
0.2248	333.15	96.60
0.2248	343.15	97.46
0.2248	353.15	98.61
0.2248	363.15	99.61
0.2248	373.15	100.23
0.3031	293.15	98.37
0.3031	303.15	99.15
0.3031	313.15	100.31
0.3031	323.15	101.88
0.3031	333.15	102.38
0.3031	343.15	103.64
0.3031	353.15	104.99
0.3031	363.15	106.52
0.3031	373.15	107.47
0.4036	293.15	104.66
0.4036	303.15	105.99
0.4036	313.15	108.06
0.4036	323.15	109.53
0.4036	333.15	111.00
0.4036	343.15	111.93
0.4036	353.15	113.83
0.4036	363.15	115.04
0.4036	373.15	116.01
0.5370	293.15	114.30
0.5370	303.15	115.72
0.5370	313.15	117.68
0.5370	323.15	119.76
0.5370	333.15	121.18
0.5370	343.15	122.85
0.5370	353.15	124.97
0.5370	363.15	126.81
0.5370	373.15	128.22
0.7230	293.15	127.90
0.7230	303.15	129.45
0.7230	313.15	131.20
0.7230	323.15	133.39
0.7230	333.15	135.38
0.7230	343.15	138.08
0.7230	353.15	140.57
0.7230	363.15	142.17
0.7230	373.15	144.36
1.0000	293.15	147.47
1.0000	303.15	149.71
1.0000	313.15	152.00
1.0000	323.15	153.80
1.0000	333.15	156.22
1.0000	343.15	159.70
1.0000	353.15	161.00
1.0000	363.15	164.98
1.0000	373.15	168.45
0.0000	293.15	75.29
0.0000	303.15	75.38
0.0000	313.15	75.21
0.0000	323.15	75.23
0.0000	333.15	75.21
0.0000	343.15	75.32
0.0000	353.15	75.48
0.0312	293.15	88.03
0.0312	303.15	87.89
0.0312	313.15	88.36
0.0312	323.15	88.63
0.0312	333.15	88.80
0.0312	343.15	88.88
0.0312	353.15	89.15
0.0312	363.15	89.25
0.0676	293.15	87.60
0.0676	303.15	87.81
0.0676	313.15	88.19
0.0676	323.15	88.59
0.0676	333.15	88.99
0.0676	343.15	89.10
0.0676	353.15	89.47
0.0676	363.15	89.60

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 293.15 (Liquid)
• Pressure, kPa = 101.325 (Liquid)

Mass fraction of 1,2-Ethanediol (1) - Liquid	Viscosity, Pa*s - Liquid
0.0000	0.0010
0.1000	0.0013
0.2000	0.0017
0.3000	0.0022
0.4000	0.0028
0.5000	0.0036
0.6000	0.0047
0.7000	0.0064
0.8000	0.0080
0.9000	0.0140

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 92.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0494	0.0015
293.15	0.0986	0.0021
293.15	0.1483	0.0027
293.15	0.2072	0.0035
293.15	0.2466	0.0041
293.15	0.2980	0.0049
293.15	0.3399	0.0057
293.15	0.3921	0.0066
293.15	0.4446	0.0076
293.15	0.5007	0.0088
293.15	0.5485	0.0098
293.15	0.6004	0.0109
293.15	0.6451	0.0120
293.15	0.7012	0.0133
293.15	0.7435	0.0143
293.15	0.7907	0.0155
293.15	0.8505	0.0169
293.15	0.8900	0.0179
293.15	0.9532	0.0195
298.15	0.0494	0.0013
298.15	0.0986	0.0017
298.15	0.1483	0.0022
298.15	0.2072	0.0028
298.15	0.2466	0.0033
298.15	0.2980	0.0039
298.15	0.3399	0.0045
298.15	0.3921	0.0053
298.15	0.4446	0.0061
298.15	0.5007	0.0070
298.15	0.5485	0.0078
298.15	0.6004	0.0087
298.15	0.6451	0.0095
298.15	0.7012	0.0105
298.15	0.7435	0.0113
298.15	0.7907	0.0122
298.15	0.8505	0.0133
298.15	0.8900	0.0141
298.15	0.9532	0.0154
303.15	0.0494	0.0012
303.15	0.0986	0.0016
303.15	0.1483	0.0020
303.15	0.2072	0.0026
303.15	0.2466	0.0030
303.15	0.2980	0.0035
303.15	0.3399	0.0040
303.15	0.3921	0.0047
303.15	0.4446	0.0053
303.15	0.5007	0.0061
303.15	0.5485	0.0068
303.15	0.6004	0.0075
303.15	0.6451	0.0082
303.15	0.7012	0.0091
303.15	0.7435	0.0098
303.15	0.7907	0.0105
303.15	0.8505	0.0115
303.15	0.8900	0.0121
303.15	0.9532	0.0131
308.15	0.0494	0.0011
308.15	0.0986	0.0014
308.15	0.1483	0.0017
308.15	0.2072	0.0022
308.15	0.2466	0.0026
308.15	0.2980	0.0031
308.15	0.3399	0.0035
308.15	0.3921	0.0040
308.15	0.4446	0.0046
308.15	0.5007	0.0052
308.15	0.5485	0.0058
308.15	0.6004	0.0064
308.15	0.6451	0.0070
308.15	0.7012	0.0077
308.15	0.7435	0.0083
308.15	0.7907	0.0089
308.15	0.8505	0.0096
308.15	0.8900	0.0101
308.15	0.9532	0.0109
293.15	0.0000	0.0011
298.15	0.0000	0.0009
303.15	0.0000	0.0008
308.15	0.0000	0.0008
293.15	1.0000	0.0206
298.15	1.0000	0.0162
303.15	1.0000	0.0139
308.15	1.0000	0.0115

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.0000	293.15	0.0010
0.0000	303.15	0.0008
0.0000	313.15	0.0007
0.0000	323.15	0.0005
0.0000	333.15	0.0005
0.0000	343.15	0.0004
0.0000	353.15	0.0004
0.0312	293.15	0.0013
0.0312	303.15	0.0010
0.0312	313.15	0.0008
0.0312	323.15	0.0007
0.0312	333.15	0.0006
0.0312	343.15	0.0005
0.0312	353.15	0.0004
0.0676	293.15	0.0018
0.0676	303.15	0.0013
0.0676	313.15	0.0010
0.0676	323.15	0.0009
0.0676	333.15	0.0007
0.0676	343.15	0.0006
0.0676	353.15	0.0005
0.1105	293.15	0.0023
0.1105	303.15	0.0017
0.1105	313.15	0.0013
0.1105	323.15	0.0011
0.1105	333.15	0.0009
0.1105	343.15	0.0007
0.1105	353.15	0.0006
0.1620	293.15	0.0030
0.1620	303.15	0.0022
0.1620	313.15	0.0017
0.1620	323.15	0.0013
0.1620	333.15	0.0011
0.1620	343.15	0.0009
0.1620	353.15	0.0008
0.2248	293.15	0.0039
0.2248	303.15	0.0028
0.2248	313.15	0.0021
0.2248	323.15	0.0017
0.2248	333.15	0.0013
0.2248	343.15	0.0011
0.2248	353.15	0.0009
0.3031	293.15	0.0051
0.3031	303.15	0.0037
0.3031	313.15	0.0028
0.3031	323.15	0.0021
0.3031	333.15	0.0016
0.3031	343.15	0.0013
0.3031	353.15	0.0011
0.4036	293.15	0.0069
0.4036	303.15	0.0050
0.4036	313.15	0.0036
0.4036	323.15	0.0027
0.4036	333.15	0.0021
0.4036	343.15	0.0016
0.4036	353.15	0.0014
0.5370	293.15	0.0097
0.5370	303.15	0.0067
0.5370	313.15	0.0048
0.5370	323.15	0.0036
0.5370	333.15	0.0027
0.5370	343.15	0.0021
0.5370	353.15	0.0017
0.7230	293.15	0.0140
0.7230	303.15	0.0094
0.7230	313.15	0.0064
0.7230	323.15	0.0048
0.7230	333.15	0.0035
0.7230	343.15	0.0028
0.7230	353.15	0.0023
1.0000	293.15	0.0208
1.0000	303.15	0.0136
1.0000	313.15	0.0094
1.0000	323.15	0.0070
1.0000	333.15	0.0051
1.0000	343.15	0.0040
1.0000	353.15	0.0030

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Mole fraction of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.2500	296.45	0.0037
0.2500	313.05	0.0023
0.2500	333.05	0.0015
0.2500	353.05	0.0010
0.2500	378.85	0.0007
0.2500	400.95	0.0005
0.2500	421.15	0.0004
0.2500	435.55	0.0004
0.5000	297.05	0.0076
0.5000	313.05	0.0045
0.5000	333.10	0.0026
0.5000	353.05	0.0017
0.5000	380.05	0.0011
0.5000	394.25	0.0009
0.5000	410.05	0.0007
0.5000	427.55	0.0006
0.5000	440.65	0.0005
0.7500	297.35	0.0123
0.7500	313.05	0.0070
0.7500	333.10	0.0039
0.7500	353.05	0.0024
0.7500	373.45	0.0016
0.7500	383.35	0.0014
0.7500	393.20	0.0012
0.7500	403.15	0.0010
0.7500	407.75	0.0010
0.7500	413.15	0.0009
0.7500	422.35	0.0008
0.7500	435.95	0.0007
0.7500	449.85	0.0006

Viscosity, Pa*s [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Viscosity, Pa*s - Liquid
308.15	0.0000	0.0007
308.15	0.0145	0.0008
308.15	0.0312	0.0008
308.15	0.0484	0.0009
308.15	0.0686	0.0010
308.15	0.0883	0.0011
308.15	0.1107	0.0013
308.15	0.1621	0.0016
308.15	0.2247	0.0020
308.15	0.3032	0.0027
308.15	0.4035	0.0035
308.15	0.5366	0.0047
308.15	1.0000	0.0092
313.15	0.0000	0.0007
313.15	0.0145	0.0007
313.15	0.0312	0.0008
313.15	0.0484	0.0008
313.15	0.0686	0.0009
313.15	0.0883	0.0010
313.15	0.1107	0.0011
313.15	0.1621	0.0014
313.15	0.2247	0.0018
313.15	0.3032	0.0023
313.15	0.4035	0.0030
313.15	0.5366	0.0041
313.15	1.0000	0.0080
318.15	0.0000	0.0006
318.15	0.0145	0.0006
318.15	0.0312	0.0007
318.15	0.0484	0.0007
318.15	0.0686	0.0008
318.15	0.0883	0.0009
318.15	0.1107	0.0010
318.15	0.1621	0.0012
318.15	0.2247	0.0015
318.15	0.3032	0.0019
318.15	0.4035	0.0025
318.15	0.5366	0.0033
318.15	1.0000	0.0063
323.15	0.0000	0.0006
323.15	0.0145	0.0006
323.15	0.0312	0.0006
323.15	0.0484	0.0007
323.15	0.0686	0.0007
323.15	0.0883	0.0008
323.15	0.1107	0.0009
323.15	0.1621	0.0011
323.15	0.2247	0.0013
323.15	0.3032	0.0017
323.15	0.4035	0.0022
323.15	0.5366	0.0029
323.15	1.0000	0.0054

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mass fraction of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.1000	298.15	0.0012
0.1000	303.15	0.0010
0.1000	308.15	0.0009
0.1000	318.15	0.0007
0.2000	298.15	0.0015
0.2000	303.15	0.0013
0.2000	308.15	0.0011
0.2000	318.15	0.0009
0.3000	298.15	0.0019
0.3000	303.15	0.0017
0.3000	308.15	0.0015
0.3000	318.15	0.0012
1.0000	298.15	0.0186
1.0000	303.15	0.0139
1.0000	308.15	0.0117
1.0000	318.15	0.0075

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 293.15 (Liquid)
• Pressure, kPa = 101.325 (Liquid)

Mass fraction of 1,2-Ethanediol (1) - Liquid	Viscosity, Pa*s - Liquid
0.0000	0.0010
0.1000	0.0013
0.2000	0.0017
0.3000	0.0022
0.4000	0.0028
0.5000	0.0036
0.6000	0.0047
0.7000	0.0064
0.8000	0.0080
0.9000	0.0140

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 92.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0494	0.0015
293.15	0.0986	0.0021
293.15	0.1483	0.0027
293.15	0.2072	0.0035
293.15	0.2466	0.0041
293.15	0.2980	0.0049
293.15	0.3399	0.0057
293.15	0.3921	0.0066
293.15	0.4446	0.0076
293.15	0.5007	0.0088
293.15	0.5485	0.0098
293.15	0.6004	0.0109
293.15	0.6451	0.0120
293.15	0.7012	0.0133
293.15	0.7435	0.0143
293.15	0.7907	0.0155
293.15	0.8505	0.0169
293.15	0.8900	0.0179
293.15	0.9532	0.0195
298.15	0.0494	0.0013
298.15	0.0986	0.0017
298.15	0.1483	0.0022
298.15	0.2072	0.0028
298.15	0.2466	0.0033
298.15	0.2980	0.0039
298.15	0.3399	0.0045
298.15	0.3921	0.0053
298.15	0.4446	0.0061
298.15	0.5007	0.0070
298.15	0.5485	0.0078
298.15	0.6004	0.0087
298.15	0.6451	0.0095
298.15	0.7012	0.0105
298.15	0.7435	0.0113
298.15	0.7907	0.0122
298.15	0.8505	0.0133
298.15	0.8900	0.0141
298.15	0.9532	0.0154
303.15	0.0494	0.0012
303.15	0.0986	0.0016
303.15	0.1483	0.0020
303.15	0.2072	0.0026
303.15	0.2466	0.0030
303.15	0.2980	0.0035
303.15	0.3399	0.0040
303.15	0.3921	0.0047
303.15	0.4446	0.0053
303.15	0.5007	0.0061
303.15	0.5485	0.0068
303.15	0.6004	0.0075
303.15	0.6451	0.0082
303.15	0.7012	0.0091
303.15	0.7435	0.0098
303.15	0.7907	0.0105
303.15	0.8505	0.0115
303.15	0.8900	0.0121
303.15	0.9532	0.0131
308.15	0.0494	0.0011
308.15	0.0986	0.0014
308.15	0.1483	0.0017
308.15	0.2072	0.0022
308.15	0.2466	0.0026
308.15	0.2980	0.0031
308.15	0.3399	0.0035
308.15	0.3921	0.0040
308.15	0.4446	0.0046
308.15	0.5007	0.0052
308.15	0.5485	0.0058
308.15	0.6004	0.0064
308.15	0.6451	0.0070
308.15	0.7012	0.0077
308.15	0.7435	0.0083
308.15	0.7907	0.0089
308.15	0.8505	0.0096
308.15	0.8900	0.0101
308.15	0.9532	0.0109
293.15	0.0000	0.0011
298.15	0.0000	0.0009
303.15	0.0000	0.0008
308.15	0.0000	0.0008
293.15	1.0000	0.0206
298.15	1.0000	0.0162
303.15	1.0000	0.0139
308.15	1.0000	0.0115

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.0000	293.15	0.0010
0.0000	303.15	0.0008
0.0000	313.15	0.0007
0.0000	323.15	0.0005
0.0000	333.15	0.0005
0.0000	343.15	0.0004
0.0000	353.15	0.0004
0.0312	293.15	0.0013
0.0312	303.15	0.0010
0.0312	313.15	0.0008
0.0312	323.15	0.0007
0.0312	333.15	0.0006
0.0312	343.15	0.0005
0.0312	353.15	0.0004
0.0676	293.15	0.0018
0.0676	303.15	0.0013
0.0676	313.15	0.0010
0.0676	323.15	0.0009
0.0676	333.15	0.0007
0.0676	343.15	0.0006
0.0676	353.15	0.0005
0.1105	293.15	0.0023
0.1105	303.15	0.0017
0.1105	313.15	0.0013
0.1105	323.15	0.0011
0.1105	333.15	0.0009
0.1105	343.15	0.0007
0.1105	353.15	0.0006
0.1620	293.15	0.0030
0.1620	303.15	0.0022
0.1620	313.15	0.0017
0.1620	323.15	0.0013
0.1620	333.15	0.0011
0.1620	343.15	0.0009
0.1620	353.15	0.0008
0.2248	293.15	0.0039
0.2248	303.15	0.0028
0.2248	313.15	0.0021
0.2248	323.15	0.0017
0.2248	333.15	0.0013
0.2248	343.15	0.0011
0.2248	353.15	0.0009
0.3031	293.15	0.0051
0.3031	303.15	0.0037
0.3031	313.15	0.0028
0.3031	323.15	0.0021
0.3031	333.15	0.0016
0.3031	343.15	0.0013
0.3031	353.15	0.0011
0.4036	293.15	0.0069
0.4036	303.15	0.0050
0.4036	313.15	0.0036
0.4036	323.15	0.0027
0.4036	333.15	0.0021
0.4036	343.15	0.0016
0.4036	353.15	0.0014
0.5370	293.15	0.0097
0.5370	303.15	0.0067
0.5370	313.15	0.0048
0.5370	323.15	0.0036
0.5370	333.15	0.0027
0.5370	343.15	0.0021
0.5370	353.15	0.0017
0.7230	293.15	0.0140
0.7230	303.15	0.0094
0.7230	313.15	0.0064
0.7230	323.15	0.0048
0.7230	333.15	0.0035
0.7230	343.15	0.0028
0.7230	353.15	0.0023
1.0000	293.15	0.0208
1.0000	303.15	0.0136
1.0000	313.15	0.0094
1.0000	323.15	0.0070
1.0000	333.15	0.0051
1.0000	343.15	0.0040
1.0000	353.15	0.0030

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Mole fraction of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.2500	296.45	0.0037
0.2500	313.05	0.0023
0.2500	333.05	0.0015
0.2500	353.05	0.0010
0.2500	378.85	0.0007
0.2500	400.95	0.0005
0.2500	421.15	0.0004
0.2500	435.55	0.0004
0.5000	297.05	0.0076
0.5000	313.05	0.0045
0.5000	333.10	0.0026
0.5000	353.05	0.0017
0.5000	380.05	0.0011
0.5000	394.25	0.0009
0.5000	410.05	0.0007
0.5000	427.55	0.0006
0.5000	440.65	0.0005
0.7500	297.35	0.0123
0.7500	313.05	0.0070
0.7500	333.10	0.0039
0.7500	353.05	0.0024
0.7500	373.45	0.0016
0.7500	383.35	0.0014
0.7500	393.20	0.0012
0.7500	403.15	0.0010
0.7500	407.75	0.0010
0.7500	413.15	0.0009
0.7500	422.35	0.0008
0.7500	435.95	0.0007
0.7500	449.85	0.0006

Viscosity, Pa*s [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Viscosity, Pa*s - Liquid
308.15	0.0000	0.0007
308.15	0.0145	0.0008
308.15	0.0312	0.0008
308.15	0.0484	0.0009
308.15	0.0686	0.0010
308.15	0.0883	0.0011
308.15	0.1107	0.0013
308.15	0.1621	0.0016
308.15	0.2247	0.0020
308.15	0.3032	0.0027
308.15	0.4035	0.0035
308.15	0.5366	0.0047
308.15	1.0000	0.0092
313.15	0.0000	0.0007
313.15	0.0145	0.0007
313.15	0.0312	0.0008
313.15	0.0484	0.0008
313.15	0.0686	0.0009
313.15	0.0883	0.0010
313.15	0.1107	0.0011
313.15	0.1621	0.0014
313.15	0.2247	0.0018
313.15	0.3032	0.0023
313.15	0.4035	0.0030
313.15	0.5366	0.0041
313.15	1.0000	0.0080
318.15	0.0000	0.0006
318.15	0.0145	0.0006
318.15	0.0312	0.0007
318.15	0.0484	0.0007
318.15	0.0686	0.0008
318.15	0.0883	0.0009
318.15	0.1107	0.0010
318.15	0.1621	0.0012
318.15	0.2247	0.0015
318.15	0.3032	0.0019
318.15	0.4035	0.0025
318.15	0.5366	0.0033
318.15	1.0000	0.0063
323.15	0.0000	0.0006
323.15	0.0145	0.0006
323.15	0.0312	0.0006
323.15	0.0484	0.0007
323.15	0.0686	0.0007
323.15	0.0883	0.0008
323.15	0.1107	0.0009
323.15	0.1621	0.0011
323.15	0.2247	0.0013
323.15	0.3032	0.0017
323.15	0.4035	0.0022
323.15	0.5366	0.0029
323.15	1.0000	0.0054

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mass fraction of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.1000	298.15	0.0012
0.1000	303.15	0.0010
0.1000	308.15	0.0009
0.1000	318.15	0.0007
0.2000	298.15	0.0015
0.2000	303.15	0.0013
0.2000	308.15	0.0011
0.2000	318.15	0.0009
0.3000	298.15	0.0019
0.3000	303.15	0.0017
0.3000	308.15	0.0015
0.3000	318.15	0.0012
1.0000	298.15	0.0186
1.0000	303.15	0.0139
1.0000	308.15	0.0117
1.0000	318.15	0.0075

Excess molar heat capacity, J/K/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Excess molar heat capacity, J/K/mol - Liquid
283.15	0.0099	0.4300
283.15	0.0262	0.8700
283.15	0.0464	1.03
283.15	0.0752	1.32
283.15	0.1016	1.26
283.15	0.1245	1.16
283.15	0.1491	0.9400
283.15	0.1731	0.7600
283.15	0.2903	-0.7200
283.15	0.4076	-1.26
283.15	0.4641	-1.33
283.15	0.6066	-1.31
283.15	0.6959	-1.2
283.15	0.8040	-0.9300
283.15	0.8463	-0.7500
283.15	0.9395	-0.4200
293.15	0.0099	0.3000
293.15	0.0262	0.7900
293.15	0.0464	1.25
293.15	0.0752	1.72
293.15	0.1245	1.91
293.15	0.1491	1.76
293.15	0.1731	1.68
293.15	0.2903	0.6100
293.15	0.4076	0.0500
293.15	0.4641	-0.1200
293.15	0.6066	-0.3500
293.15	0.6959	-0.4300
293.15	0.8040	-0.3600
293.15	0.8463	-0.3600
293.15	0.9395	-0.1900
298.15	0.0099	0.2600
298.15	0.0262	0.7600
298.15	0.0464	1.33
298.15	0.0752	1.85
298.15	0.0951	1.99
298.15	0.1245	2.17
298.15	0.1491	2.08
298.15	0.1731	2.01
298.15	0.2903	1.14
298.15	0.4076	0.5400
298.15	0.4641	0.3500
298.15	0.6066	0.0200
298.15	0.6959	-0.1200
298.15	0.8040	-0.2000
298.15	0.8463	-0.2200
298.15	0.9395	-0.1900
303.15	0.0099	0.2600
303.15	0.0262	0.7500
303.15	0.0464	1.39
303.15	0.0752	1.96
303.15	0.0951	2.2
303.15	0.1245	2.38
303.15	0.1491	2.35
303.15	0.1731	2.29
303.15	0.2903	1.6
303.15	0.4076	0.9800
303.15	0.4641	0.7800
303.15	0.6066	0.0350
303.15	0.6959	0.1500
303.15	0.8040	-0.0700
303.15	0.8864	-0.3000
303.15	0.9395	-0.2100
313.15	0.0099	0.3700
313.15	0.0262	0.7400
313.15	0.0464	1.5
313.15	0.0752	2.17
313.15	0.0951	2.5
313.15	0.1245	2.76
313.15	0.1491	2.82
313.15	0.2203	2.62
313.15	0.2903	2.42
313.15	0.4076	1.82
313.15	0.4641	1.58
313.15	0.6066	0.9600
313.15	0.6959	0.6300
313.15	0.8040	0.1800
313.15	0.8864	-0.1400
313.15	0.9395	-0.0900

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Water (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1014	-0.1740
0.1994	-0.3370
0.2091	-0.3470
0.3051	-0.4800
0.3674	-0.5590
0.3995	-0.5900
0.4807	-0.6400
0.5455	-0.6660
0.6144	-0.6980
0.6690	-0.7150
0.7949	-0.6810
0.8656	-0.5700
0.9150	-0.4230

Excess molar heat capacity, J/K/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Excess molar heat capacity, J/K/mol - Liquid
283.15	0.0099	0.4300
283.15	0.0262	0.8700
283.15	0.0464	1.03
283.15	0.0752	1.32
283.15	0.1016	1.26
283.15	0.1245	1.16
283.15	0.1491	0.9400
283.15	0.1731	0.7600
283.15	0.2903	-0.7200
283.15	0.4076	-1.26
283.15	0.4641	-1.33
283.15	0.6066	-1.31
283.15	0.6959	-1.2
283.15	0.8040	-0.9300
283.15	0.8463	-0.7500
283.15	0.9395	-0.4200
293.15	0.0099	0.3000
293.15	0.0262	0.7900
293.15	0.0464	1.25
293.15	0.0752	1.72
293.15	0.1245	1.91
293.15	0.1491	1.76
293.15	0.1731	1.68
293.15	0.2903	0.6100
293.15	0.4076	0.0500
293.15	0.4641	-0.1200
293.15	0.6066	-0.3500
293.15	0.6959	-0.4300
293.15	0.8040	-0.3600
293.15	0.8463	-0.3600
293.15	0.9395	-0.1900
298.15	0.0099	0.2600
298.15	0.0262	0.7600
298.15	0.0464	1.33
298.15	0.0752	1.85
298.15	0.0951	1.99
298.15	0.1245	2.17
298.15	0.1491	2.08
298.15	0.1731	2.01
298.15	0.2903	1.14
298.15	0.4076	0.5400
298.15	0.4641	0.3500
298.15	0.6066	0.0200
298.15	0.6959	-0.1200
298.15	0.8040	-0.2000
298.15	0.8463	-0.2200
298.15	0.9395	-0.1900
303.15	0.0099	0.2600
303.15	0.0262	0.7500
303.15	0.0464	1.39
303.15	0.0752	1.96
303.15	0.0951	2.2
303.15	0.1245	2.38
303.15	0.1491	2.35
303.15	0.1731	2.29
303.15	0.2903	1.6
303.15	0.4076	0.9800
303.15	0.4641	0.7800
303.15	0.6066	0.0350
303.15	0.6959	0.1500
303.15	0.8040	-0.0700
303.15	0.8864	-0.3000
303.15	0.9395	-0.2100
313.15	0.0099	0.3700
313.15	0.0262	0.7400
313.15	0.0464	1.5
313.15	0.0752	2.17
313.15	0.0951	2.5
313.15	0.1245	2.76
313.15	0.1491	2.82
313.15	0.2203	2.62
313.15	0.2903	2.42
313.15	0.4076	1.82
313.15	0.4641	1.58
313.15	0.6066	0.9600
313.15	0.6959	0.6300
313.15	0.8040	0.1800
313.15	0.8864	-0.1400
313.15	0.9395	-0.0900

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Water (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1014	-0.1740
0.1994	-0.3370
0.2091	-0.3470
0.3051	-0.4800
0.3674	-0.5590
0.3995	-0.5900
0.4807	-0.6400
0.5455	-0.6660
0.6144	-0.6980
0.6690	-0.7150
0.7949	-0.6810
0.8656	-0.5700
0.9150	-0.4230

Vapor or sublimation pressure, kPa [ref]

Operational condition: Mass fraction = 0.365 (Liquid)

Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
258.32	0.19
263.19	0.29
268.23	0.41
273.34	0.58
283.00	1.14
292.77	2.13

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 333.15 (Liquid)

Mole fraction of Water (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	0.22
0.0033	0.28
0.0095	0.39
0.0163	0.51
0.0272	0.71
0.0414	0.96
0.0634	1.35
0.0928	1.87
0.1322	2.58
0.1783	3.43
0.2310	4.42
0.2889	5.52
0.3488	6.69
0.4145	7.99
0.4777	9.27
0.5378	10.49
0.5926	11.61
0.6420	12.64
0.6863	13.55
0.7254	14.37
0.7594	15.09
0.7892	15.72
0.7898	15.81
0.8200	16.42
0.8482	16.99
0.8739	17.50
0.8972	17.94
0.9180	18.38
0.9360	18.74
0.9515	19.04
0.9633	19.22
0.9730	19.43
0.9808	19.58
0.9867	19.70
0.9911	19.78
0.9940	19.83
0.9960	19.87
0.9974	19.92
0.9984	19.89
0.9991	19.88
0.9997	19.92
1.0000	19.93

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 353.15 (Liquid)

Mole fraction of Water (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	0.77
0.0059	1.02
0.0115	1.28
0.0217	1.72
0.0331	2.22
0.0454	2.76
0.0668	3.70
0.0963	4.99
0.1358	6.71
0.1816	8.76
0.2346	11.15
0.2919	13.81
0.3516	16.60
0.4170	19.70
0.4797	22.70
0.5393	25.58
0.5936	28.22
0.6428	30.61
0.6868	32.75
0.7248	34.59
0.7258	34.65
0.7580	36.16
0.7898	37.66
0.8200	39.10
0.8481	40.40
0.8738	41.61
0.8971	42.69
0.9179	43.67
0.9358	44.50
0.9513	45.15
0.9631	45.72
0.9728	46.20
0.9804	46.56
0.9862	46.78
0.9909	47.02
0.9938	47.16
0.9958	47.26
0.9972	47.32
0.9982	47.36
0.9991	47.40
0.9997	47.41
1.0000	47.44

Vapor or sublimation pressure, kPa [ref]

Operational condition: Mass fraction = 0.365 (Liquid)

Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
258.32	0.19
263.19	0.29
268.23	0.41
273.34	0.58
283.00	1.14
292.77	2.13

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 333.15 (Liquid)

Mole fraction of Water (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	0.22
0.0033	0.28
0.0095	0.39
0.0163	0.51
0.0272	0.71
0.0414	0.96
0.0634	1.35
0.0928	1.87
0.1322	2.58
0.1783	3.43
0.2310	4.42
0.2889	5.52
0.3488	6.69
0.4145	7.99
0.4777	9.27
0.5378	10.49
0.5926	11.61
0.6420	12.64
0.6863	13.55
0.7254	14.37
0.7594	15.09
0.7892	15.72
0.7898	15.81
0.8200	16.42
0.8482	16.99
0.8739	17.50
0.8972	17.94
0.9180	18.38
0.9360	18.74
0.9515	19.04
0.9633	19.22
0.9730	19.43
0.9808	19.58
0.9867	19.70
0.9911	19.78
0.9940	19.83
0.9960	19.87
0.9974	19.92
0.9984	19.89
0.9991	19.88
0.9997	19.92
1.0000	19.93

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 353.15 (Liquid)

Mole fraction of Water (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	0.77
0.0059	1.02
0.0115	1.28
0.0217	1.72
0.0331	2.22
0.0454	2.76
0.0668	3.70
0.0963	4.99
0.1358	6.71
0.1816	8.76
0.2346	11.15
0.2919	13.81
0.3516	16.60
0.4170	19.70
0.4797	22.70
0.5393	25.58
0.5936	28.22
0.6428	30.61
0.6868	32.75
0.7248	34.59
0.7258	34.65
0.7580	36.16
0.7898	37.66
0.8200	39.10
0.8481	40.40
0.8738	41.61
0.8971	42.69
0.9179	43.67
0.9358	44.50
0.9513	45.15
0.9631	45.72
0.9728	46.20
0.9804	46.56
0.9862	46.78
0.9909	47.02
0.9938	47.16
0.9958	47.26
0.9972	47.32
0.9982	47.36
0.9991	47.40
0.9997	47.41
1.0000	47.44

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 303 (Liquid)
• Pressure, kPa = 100 (Liquid)

Mass fraction of Water (2) - Liquid	Refractive index (Na D-line) - Liquid
0.1000	1.4196
0.2000	1.4101
0.3000	1.4008
0.4100	1.3899
0.5000	1.3811
0.6000	1.3713
0.7000	1.3607
0.8000	1.3512
0.8900	1.3417
1.0000	1.3318

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 303 (Liquid)
• Pressure, kPa = 100 (Liquid)

Mass fraction of Water (2) - Liquid	Refractive index (Na D-line) - Liquid
0.1000	1.4196
0.2000	1.4101
0.3000	1.4008
0.4100	1.3899
0.5000	1.3811
0.6000	1.3713
0.7000	1.3607
0.8000	1.3512
0.8900	1.3417
1.0000	1.3318

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Mass density, kg/m3 - Liquid
278.15	0.0000	999.96
288.15	0.0000	999.09
298.15	0.0000	997.04
308.15	0.0000	994.03
323.15	0.0000	988.03
278.15	0.0228	1010.24
288.15	0.0228	1008.82
298.15	0.0228	1006.33
308.15	0.0228	1002.99
323.15	0.0228	996.6
278.15	0.0549	1023.85
288.15	0.0549	1021.56
298.15	0.0549	1018.45
308.15	0.0549	1014.58
323.15	0.0549	1007.61
278.15	0.0783	1032.87
288.15	0.0783	1030.01
298.15	0.0783	1026.44
308.15	0.0783	1022.21
323.15	0.0783	1014.78
278.15	0.1012	1040.89
288.15	0.1012	1037.48
298.15	0.1012	1033.52
308.15	0.1012	1028.99
323.15	0.1012	1021.16
278.15	0.1580	1057.7
288.15	0.1580	1053.26
298.15	0.1580	1048.42
308.15	0.1580	1043.17
323.15	0.1580	1034.52
278.15	0.2000	1067.88
288.15	0.2000	1062.86
298.15	0.2000	1057.55
308.15	0.2000	1051.92
323.15	0.2000	1042.75
278.15	0.2990	1085.43
288.15	0.2990	1079.59
298.15	0.2990	1073.54
308.15	0.2990	1067.25
323.15	0.2990	1057.39
278.15	0.3917	1096.56
288.15	0.3917	1090.28
298.15	0.3917	1083.85
308.15	0.3917	1077.24
323.15	0.3917	1067.02
278.15	0.5006	1105.57
288.15	0.5006	1098.99
298.15	0.5006	1092.32
308.15	0.5006	1085.51
323.15	0.5006	1075.02
278.15	0.6041	1111.55
288.15	0.6041	1104.81
298.15	0.6041	1098.0
308.15	0.6041	1091.09
323.15	0.6041	1080.49
278.15	0.7063	1115.93
288.15	0.7063	1109.12
298.15	0.7063	1102.24
308.15	0.7063	1095.28
323.15	0.7063	1084.61
278.15	0.8049	1119.14
288.15	0.8049	1112.26
298.15	0.8049	1105.34
308.15	0.8049	1098.34
323.15	0.8049	1087.65
278.15	0.9034	1121.73
288.15	0.9034	1114.79
298.15	0.9034	1107.84
308.15	0.9034	1100.82
323.15	0.9034	1090.14
278.15	0.9535	1122.81
288.15	0.9535	1115.88
298.15	0.9535	1108.92
308.15	0.9535	1101.89
323.15	0.9535	1091.19
278.15	0.9826	1123.42
288.15	0.9826	1116.49
298.15	0.9826	1109.51
308.15	0.9826	1102.48
323.15	0.9826	1091.78
278.15	1.0000	1123.8
288.15	1.0000	1116.85
298.15	1.0000	1109.88
308.15	1.0000	1102.84
323.15	1.0000	1092.14

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Mass fraction = 0.365 (Liquid)

Temperature, K - Liquid	Mass density, kg/m3 - Liquid
283.15	1059.35
293.15	1054.78
303.15	1049.78
313.15	1044.38
323.15	1038.57
333.15	1032.23

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 293.15 (Liquid)
• Pressure, kPa = 101.325 (Liquid)

Mass fraction of 1,2-Ethanediol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	998.2
0.1000	1011.1
0.2000	1024.49
0.3000	1011.53
0.4000	1049.89
0.5000	1062.42
0.6000	1062.42
0.7000	1085.2
0.8000	1095.34
0.9000	1103.7

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Molality, mol/kg of Water (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	1109.41
0.1028	1109.35
0.2175	1109.25
0.3155	1109.22
0.3759	1109.06
0.7031	1108.82
0.8080	1108.62
0.9282	1108.2
1.035	1108.14
1.1315	1108.1

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 92.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0101	1002.829
293.15	0.0201	1006.956
293.15	0.0302	1011.025
293.15	0.0407	1015.066
293.15	0.0506	1018.749
293.15	0.0605	1022.309
293.15	0.0704	1025.778
293.15	0.0801	1029.042
293.15	0.0905	1032.343
293.15	0.0997	1035.298
293.15	0.1493	1048.743
293.15	0.1985	1059.448
293.15	0.2487	1069.199
293.15	0.2998	1076.801
293.15	0.3318	1080.901
293.15	0.3981	1087.835
293.15	0.4521	1092.39
293.15	0.4934	1095.399
293.15	0.5520	1099.003
293.15	0.5846	1100.786
293.15	0.6481	1103.654
293.15	0.6773	1104.876
293.15	0.7421	1107.157
293.15	0.7811	1108.406
293.15	0.8497	1110.31
293.15	0.9002	1111.546
293.15	0.9059	1111.665
293.15	0.9120	1111.779
293.15	0.9299	1112.182
293.15	0.9413	1112.433
293.15	0.9495	1112.623
293.15	0.9546	1112.726
293.15	0.9681	1112.988
293.15	0.9789	1113.191
293.15	0.9893	1113.396
298.15	0.0101	1001.541
298.15	0.0201	1005.567
298.15	0.0302	1009.564
298.15	0.0407	1013.505
298.15	0.0506	1017.078
298.15	0.0605	1020.555
298.15	0.0704	1023.962
298.15	0.0801	1027.147
298.15	0.0905	1030.368
298.15	0.0997	1033.238
298.15	0.1493	1046.402
298.15	0.1985	1056.961
298.15	0.2487	1066.321
298.15	0.2998	1073.788
298.15	0.3318	1077.774
298.15	0.3981	1084.61
298.15	0.4521	1089.105
298.15	0.4934	1092.048
298.15	0.5520	1095.614
298.15	0.5846	1097.376
298.15	0.6481	1100.225
298.15	0.6773	1101.431
298.15	0.7421	1103.692
298.15	0.7811	1104.938
298.15	0.8497	1106.827
298.15	0.9002	1108.058
298.15	0.9059	1108.174
298.15	0.9120	1108.286
298.15	0.9299	1108.689
298.15	0.9413	1108.94
298.15	0.9495	1109.129
298.15	0.9546	1109.231
298.15	0.9681	1109.49
298.15	0.9789	1109.691
298.15	0.9893	1109.896
303.15	0.0101	1000.037
303.15	0.0201	1004.002
303.15	0.0302	1007.879
303.15	0.0407	1011.759
303.15	0.0506	1015.244
303.15	0.0605	1018.727
303.15	0.0704	1022.118
303.15	0.0801	1025.104
303.15	0.0905	1028.308
303.15	0.0997	1031.047
303.15	0.1493	1044.063
303.15	0.1985	1054.471
303.15	0.2487	1063.376
303.15	0.2998	1070.697
303.15	0.3318	1074.592
303.15	0.3981	1081.335
303.15	0.4521	1085.692
303.15	0.4934	1088.59
303.15	0.5520	1092.191
303.15	0.5846	1093.942
303.15	0.6481	1096.768
303.15	0.6773	1097.962
303.15	0.7421	1100.208
303.15	0.7811	1101.444
303.15	0.8497	1103.327
303.15	0.9002	1104.55
303.15	0.9059	1104.669
303.15	0.9120	1104.782
303.15	0.9299	1105.186
303.15	0.9413	1105.432
303.15	0.9495	1105.622
303.15	0.9546	1105.724
303.15	0.9681	1105.98
303.15	0.9789	1106.18
303.15	0.9893	1106.387
308.15	0.0101	998.43
308.15	0.0201	1002.324
308.15	0.0302	1006.129
308.15	0.0407	1009.896
308.15	0.0506	1013.359
308.15	0.0605	1016.685
308.15	0.0704	1019.918
308.15	0.0801	1022.9
308.15	0.0905	1026.046
308.15	0.0997	1028.71
308.15	0.1493	1041.45
308.15	0.1985	1051.737
308.15	0.2487	1060.371
308.15	0.2998	1067.567
308.15	0.3318	1071.384
308.15	0.3981	1077.992
308.15	0.4521	1082.37
308.15	0.4934	1085.257
308.15	0.5520	1088.74
308.15	0.5846	1090.48
308.15	0.6481	1093.288
308.15	0.6773	1094.476
308.15	0.7421	1096.71
308.15	0.7811	1097.939
308.15	0.8497	1099.811
308.15	0.9002	1101.031
308.15	0.9059	1101.15
308.15	0.9120	1101.26
308.15	0.9299	1101.661
308.15	0.9413	1101.909
308.15	0.9495	1102.102
308.15	0.9546	1102.203
308.15	0.9681	1102.459
308.15	0.9789	1102.654
308.15	0.9893	1102.859
293.15	0.0000	998.429
298.15	0.0000	997.267
303.15	0.0000	995.867
308.15	0.0000	994.252
293.15	1.0000	1113.725
298.15	1.0000	1110.225
303.15	1.0000	1106.715
308.15	1.0000	1103.194
293.15	0.0494	1018.402
293.15	0.0986	1034.8
293.15	0.1483	1048.464
293.15	0.2072	1061.508
293.15	0.2466	1068.682
293.15	0.2980	1076.499
293.15	0.3399	1081.798
293.15	0.3921	1087.306
293.15	0.4446	1091.877
293.15	0.5007	1095.914
293.15	0.5485	1098.81
293.15	0.6004	1101.51
293.15	0.6451	1103.534
293.15	0.7012	1105.75
293.15	0.7435	1107.221
293.15	0.7907	1108.688
293.15	0.8505	1110.325
293.15	0.8900	1111.29
293.15	0.9532	1112.691
298.15	0.0494	1016.76
298.15	0.0986	1032.776
298.15	0.1483	1046.118
298.15	0.2072	1058.856
298.15	0.2466	1065.864
298.15	0.2980	1073.506
298.15	0.3399	1078.691
298.15	0.3921	1084.091
298.15	0.4446	1088.582
298.15	0.5007	1092.559
298.15	0.5485	1095.419
298.15	0.6004	1098.092
298.15	0.6451	1100.099
298.15	0.7012	1102.3
298.15	0.7435	1103.762
298.15	0.7907	1105.219
298.15	0.8505	1106.844
298.15	0.8900	1107.803
298.15	0.9532	1109.194
303.15	0.0494	1014.981
303.15	0.0986	1030.679
303.15	0.1483	1043.727
303.15	0.2072	1056.162
303.15	0.2466	1062.997
303.15	0.2980	1070.452
303.15	0.3399	1075.516
303.15	0.3921	1080.799
303.15	0.4446	1085.21
303.15	0.5007	1089.132
303.15	0.5485	1091.967
303.15	0.6004	1094.627
303.15	0.6451	1096.629
303.15	0.7012	1098.828
303.15	0.7435	1100.287
303.15	0.7907	1101.739
303.15	0.8505	1103.353
303.15	0.8900	1104.302
303.15	0.9532	1105.684
308.15	0.0494	1013.023
308.15	0.0986	1028.374
308.15	0.1483	1041.14
308.15	0.2072	1053.317
308.15	0.2466	1060.017
308.15	0.2980	1067.333
308.15	0.3399	1072.309
308.15	0.3921	1077.509
308.15	0.4446	1081.857
308.15	0.5007	1085.732
308.15	0.5485	1088.537
308.15	0.6004	1091.172
308.15	0.6451	1093.158
308.15	0.7012	1095.34
308.15	0.7435	1096.789
308.15	0.7907	1098.231
308.15	0.8505	1099.835
308.15	0.8900	1100.78
308.15	0.9532	1102.16

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of 1,2-Ethanediol (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0989	999.06
293.15	0.1989	999.88
293.15	0.2997	1000.68
293.15	0.3948	1001.41
293.15	0.5016	1002.2
303.15	0.0989	996.47
303.15	0.1989	997.26
303.15	0.2997	998.03
303.15	0.3948	998.73
303.15	0.5016	999.48
293.15	0.0000	998.21
303.15	0.0000	995.66

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Mass fraction of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	293.15	998.2
0.0000	303.15	995.6
0.0000	313.25	992.2
0.0000	323.25	988.0
0.0000	333.35	983.1
0.9500	293.45	1109.3
0.9500	303.45	1102.4
0.9500	313.15	1095.5
0.9500	323.25	1088.3
0.9500	333.35	1081.0
1.0000	293.25	1113.6
1.0000	303.15	1106.5
1.0000	313.15	1099.2
1.0000	323.25	1091.9
1.0000	333.25	1084.6

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 98.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of 1,2-Ethanediol (1) - Liquid	Mass density, kg/m3 - Liquid
278.15	0.1018	1000.805
278.15	0.2048	1001.654
278.15	0.2949	1002.39
278.15	0.4028	1003.265
278.15	0.5086	1004.115
283.15	0.1018	1000.519
283.15	0.2048	1001.344
283.15	0.2949	1002.061
283.15	0.4028	1002.908
283.15	0.5086	1003.737
288.15	0.1018	999.9
288.15	0.2048	1000.705
288.15	0.2949	1001.404
288.15	0.4028	1002.232
288.15	0.5086	1003.038
293.15	0.1018	998.99
293.15	0.2048	999.777
293.15	0.2949	1000.46
293.15	0.4028	1001.27
293.15	0.5086	1002.058
298.15	0.1018	997.817
298.15	0.2048	998.59
298.15	0.2949	999.26
298.15	0.4028	1000.053
298.15	0.5086	1000.825
303.15	0.1018	996.408
303.15	0.2048	997.167
303.15	0.2949	997.824
303.15	0.4028	998.603
303.15	0.5086	999.362
308.15	0.1018	994.781
308.15	0.2048	995.528
308.15	0.2949	996.175
308.15	0.4028	996.94
308.15	0.5086	997.687
313.15	0.1018	992.953
313.15	0.2048	993.69
313.15	0.2949	994.327
313.15	0.4028	995.08
313.15	0.5086	995.815
318.15	0.1018	990.94
318.15	0.2048	991.667
318.15	0.2949	992.296
318.15	0.4028	993.039
318.15	0.5086	993.763
323.15	0.1018	988.755
323.15	0.2048	989.472
323.15	0.2949	990.093
323.15	0.4028	990.827
323.15	0.5086	991.539
328.15	0.1018	986.404
328.15	0.2048	987.112
328.15	0.2949	987.725
328.15	0.4028	988.451
328.15	0.5086	989.155
333.15	0.1018	983.897
333.15	0.2048	984.598
333.15	0.2949	985.204
333.15	0.4028	985.921
333.15	0.5086	986.616
338.15	0.1018	981.244
338.15	0.2048	981.938
338.15	0.2949	982.538
338.15	0.4028	983.246
338.15	0.5086	983.933
343.15	0.1018	978.449
343.15	0.2048	979.137
343.15	0.2949	979.73
343.15	0.4028	980.432
343.15	0.5086	981.112

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.9886	1119.903
288.15	0.9886	1116.426
293.15	0.9886	1112.944
298.15	0.9886	1109.463
303.15	0.9886	1105.95
308.15	0.9886	1102.43
313.15	0.9886	1098.889
323.15	0.9886	1091.746
333.15	0.9886	1084.507
343.15	0.9886	1077.163
283.15	0.9943	1120.066
288.15	0.9943	1116.59
293.15	0.9943	1113.108
298.15	0.9943	1109.613
303.15	0.9943	1106.11
308.15	0.9943	1102.586
313.15	0.9943	1099.049
323.15	0.9943	1091.903
333.15	0.9943	1084.669
343.15	0.9943	1077.326
283.15	0.9959	1120.113
288.15	0.9959	1116.638
293.15	0.9959	1113.155
298.15	0.9959	1109.661
303.15	0.9959	1106.155
308.15	0.9959	1102.634
313.15	0.9959	1099.095
323.15	0.9959	1091.952
333.15	0.9959	1084.718
343.15	0.9959	1077.37

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of 1,2-Ethanediol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0989	1000.117
288.15	0.1989	1000.96
288.15	0.2997	1001.786
288.15	0.3948	1002.529
288.15	0.5016	1003.347
288.15	0.5923	1004.018
288.15	0.6964	1004.757
288.15	0.7983	1005.436
298.15	0.0989	997.877
298.15	0.1989	998.688
298.15	0.2997	999.473
298.15	0.3948	1000.184
298.15	0.5016	1000.961
298.15	0.5923	1001.596
298.15	0.6964	1002.293
298.15	0.7983	1002.952
308.15	0.0989	994.84
308.15	0.1989	995.613
308.15	0.2997	996.362
308.15	0.3948	997.038
308.15	0.5016	997.764
308.15	0.5923	998.366
308.15	0.6964	999.045
308.15	0.7983	999.679
318.15	0.0989	991.134
318.15	0.1989	991.88
318.15	0.2997	992.607
318.15	0.3948	993.261
318.15	0.5016	993.973
318.15	0.5923	994.55
318.15	0.6964	995.188
318.15	0.7983	995.805

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Molality, mol/kg of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0989	293.15	999.059
0.1989	293.15	999.884
0.2997	293.15	1000.683
0.3948	293.15	1001.405
0.5016	293.15	1002.197
0.0989	298.15	997.877
0.1989	298.15	998.688
0.2997	298.15	999.473
0.3948	298.15	1000.184
0.5016	298.15	1000.961
0.0989	303.15	996.471
0.1989	303.15	997.262
0.2997	303.15	998.033
0.3948	303.15	998.733
0.5016	303.15	999.48
0.0989	308.15	994.84
0.1989	308.15	995.613
0.2997	308.15	996.362
0.3948	308.15	997.038
0.5016	308.15	997.764

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	293.15	998.2
0.0000	303.15	995.7
0.0000	313.15	992.2
0.0000	323.15	988.1
0.0000	333.15	983.2
0.0000	343.15	977.8
0.0000	353.15	971.8
0.0312	293.15	1011.7
0.0312	303.15	1006.1
0.0312	313.15	1001.3
0.0312	323.15	994.9
0.0312	333.15	989.8
0.0312	343.15	983.7
0.0312	353.15	977.1
0.0676	293.15	1024.6
0.0676	303.15	1018.4
0.0676	313.15	1010.6
0.0676	323.15	1005.1
0.0676	333.15	997.9
0.0676	343.15	991.5
0.0676	353.15	984.7
0.1105	293.15	1037.2
0.1105	303.15	1030.0
0.1105	313.15	1021.9
0.1105	323.15	1015.1
0.1105	333.15	1007.2
0.1105	343.15	1000.4
0.1105	353.15	993.6
0.1620	293.15	1051.3
0.1620	303.15	1043.4
0.1620	313.15	1034.7
0.1620	323.15	1027.4
0.1620	333.15	1019.2
0.1620	343.15	1011.5
0.1620	353.15	1003.8
0.2248	293.15	1064.8
0.2248	303.15	1056.2
0.2248	313.15	1046.8
0.2248	323.15	1038.6
0.2248	333.15	1030.3
0.2248	343.15	1022.3
0.2248	353.15	1014.0
0.3031	293.15	1076.7
0.3031	303.15	1067.5
0.3031	313.15	1057.9
0.3031	323.15	1049.2
0.3031	333.15	1040.6
0.3031	343.15	1031.9
0.3031	353.15	1023.7
0.4036	293.15	1087.8
0.4036	303.15	1078.0
0.4036	313.15	1067.9
0.4036	323.15	1059.0
0.4036	333.15	1050.3
0.4036	343.15	1041.3
0.4036	353.15	1033.0
0.5370	293.15	1097.8
0.5370	303.15	1087.0
0.5370	313.15	1077.1
0.5370	323.15	1068.0
0.5370	333.15	1059.2
0.5370	343.15	1050.1
0.5370	353.15	1042.0
0.7230	293.15	1105.7
0.7230	303.15	1095.5
0.7230	313.15	1085.8
0.7230	323.15	1076.7
0.7230	333.15	1068.0
0.7230	343.15	1058.8
0.7230	353.15	1050.9
1.0000	293.15	1113.7
1.0000	303.15	1103.2
1.0000	313.15	1093.6
1.0000	323.15	1084.7
1.0000	333.15	1076.4
1.0000	343.15	1067.5
1.0000	353.15	1060.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Mole fraction of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.2500	296.40	1068.0
0.2500	313.05	1058.0
0.2500	333.05	1045.0
0.2500	353.05	1030.0
0.2500	374.85	1013.0
0.2500	396.95	995.5
0.2500	417.15	977.4
0.2500	431.55	964.9
0.5000	297.05	1094.0
0.5000	313.05	1083.0
0.5000	333.10	1069.0
0.5000	353.05	1054.0
0.5000	376.05	1035.0
0.5000	390.25	1023.0
0.5000	406.05	1010.0
0.5000	423.55	994.5
0.5000	436.65	982.5
0.7500	297.35	1106.0
0.7500	313.05	1094.0
0.7500	333.10	1080.0
0.7500	353.05	1065.0
0.7500	373.45	1049.0
0.7500	383.35	1041.0
0.7500	393.20	1033.0
0.7500	403.15	1025.0
0.7500	404.75	1023.0
0.7500	413.15	1016.0
0.7500	418.35	1012.0
0.7500	431.95	1000.0
0.7500	445.85	987.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mass fraction of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.1000	298.15	1009.49
0.1000	303.15	1007.62
0.1000	308.15	1005.57
0.1000	318.15	1002.73
0.2000	298.15	1022.45
0.2000	303.15	1020.98
0.2000	308.15	1018.5
0.2000	318.15	1014.28
0.3000	298.15	1035.7
0.3000	303.15	1034.05
0.3000	308.15	1031.66
0.3000	318.15	1026.73
1.0000	298.15	1110.45
1.0000	303.15	1104.47
1.0000	308.15	1100.13
1.0000	318.15	1092.15

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Mass density, kg/m3 - Liquid
278.15	0.0000	999.96
288.15	0.0000	999.09
298.15	0.0000	997.04
308.15	0.0000	994.03
323.15	0.0000	988.03
278.15	0.0228	1010.24
288.15	0.0228	1008.82
298.15	0.0228	1006.33
308.15	0.0228	1002.99
323.15	0.0228	996.6
278.15	0.0549	1023.85
288.15	0.0549	1021.56
298.15	0.0549	1018.45
308.15	0.0549	1014.58
323.15	0.0549	1007.61
278.15	0.0783	1032.87
288.15	0.0783	1030.01
298.15	0.0783	1026.44
308.15	0.0783	1022.21
323.15	0.0783	1014.78
278.15	0.1012	1040.89
288.15	0.1012	1037.48
298.15	0.1012	1033.52
308.15	0.1012	1028.99
323.15	0.1012	1021.16
278.15	0.1580	1057.7
288.15	0.1580	1053.26
298.15	0.1580	1048.42
308.15	0.1580	1043.17
323.15	0.1580	1034.52
278.15	0.2000	1067.88
288.15	0.2000	1062.86
298.15	0.2000	1057.55
308.15	0.2000	1051.92
323.15	0.2000	1042.75
278.15	0.2990	1085.43
288.15	0.2990	1079.59
298.15	0.2990	1073.54
308.15	0.2990	1067.25
323.15	0.2990	1057.39
278.15	0.3917	1096.56
288.15	0.3917	1090.28
298.15	0.3917	1083.85
308.15	0.3917	1077.24
323.15	0.3917	1067.02
278.15	0.5006	1105.57
288.15	0.5006	1098.99
298.15	0.5006	1092.32
308.15	0.5006	1085.51
323.15	0.5006	1075.02
278.15	0.6041	1111.55
288.15	0.6041	1104.81
298.15	0.6041	1098.0
308.15	0.6041	1091.09
323.15	0.6041	1080.49
278.15	0.7063	1115.93
288.15	0.7063	1109.12
298.15	0.7063	1102.24
308.15	0.7063	1095.28
323.15	0.7063	1084.61
278.15	0.8049	1119.14
288.15	0.8049	1112.26
298.15	0.8049	1105.34
308.15	0.8049	1098.34
323.15	0.8049	1087.65
278.15	0.9034	1121.73
288.15	0.9034	1114.79
298.15	0.9034	1107.84
308.15	0.9034	1100.82
323.15	0.9034	1090.14
278.15	0.9535	1122.81
288.15	0.9535	1115.88
298.15	0.9535	1108.92
308.15	0.9535	1101.89
323.15	0.9535	1091.19
278.15	0.9826	1123.42
288.15	0.9826	1116.49
298.15	0.9826	1109.51
308.15	0.9826	1102.48
323.15	0.9826	1091.78
278.15	1.0000	1123.8
288.15	1.0000	1116.85
298.15	1.0000	1109.88
308.15	1.0000	1102.84
323.15	1.0000	1092.14

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Mass fraction = 0.365 (Liquid)

Temperature, K - Liquid	Mass density, kg/m3 - Liquid
283.15	1059.35
293.15	1054.78
303.15	1049.78
313.15	1044.38
323.15	1038.57
333.15	1032.23

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 293.15 (Liquid)
• Pressure, kPa = 101.325 (Liquid)

Mass fraction of 1,2-Ethanediol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	998.2
0.1000	1011.1
0.2000	1024.49
0.3000	1011.53
0.4000	1049.89
0.5000	1062.42
0.6000	1062.42
0.7000	1085.2
0.8000	1095.34
0.9000	1103.7

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Molality, mol/kg of Water (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	1109.41
0.1028	1109.35
0.2175	1109.25
0.3155	1109.22
0.3759	1109.06
0.7031	1108.82
0.8080	1108.62
0.9282	1108.2
1.035	1108.14
1.1315	1108.1

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 92.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0101	1002.829
293.15	0.0201	1006.956
293.15	0.0302	1011.025
293.15	0.0407	1015.066
293.15	0.0506	1018.749
293.15	0.0605	1022.309
293.15	0.0704	1025.778
293.15	0.0801	1029.042
293.15	0.0905	1032.343
293.15	0.0997	1035.298
293.15	0.1493	1048.743
293.15	0.1985	1059.448
293.15	0.2487	1069.199
293.15	0.2998	1076.801
293.15	0.3318	1080.901
293.15	0.3981	1087.835
293.15	0.4521	1092.39
293.15	0.4934	1095.399
293.15	0.5520	1099.003
293.15	0.5846	1100.786
293.15	0.6481	1103.654
293.15	0.6773	1104.876
293.15	0.7421	1107.157
293.15	0.7811	1108.406
293.15	0.8497	1110.31
293.15	0.9002	1111.546
293.15	0.9059	1111.665
293.15	0.9120	1111.779
293.15	0.9299	1112.182
293.15	0.9413	1112.433
293.15	0.9495	1112.623
293.15	0.9546	1112.726
293.15	0.9681	1112.988
293.15	0.9789	1113.191
293.15	0.9893	1113.396
298.15	0.0101	1001.541
298.15	0.0201	1005.567
298.15	0.0302	1009.564
298.15	0.0407	1013.505
298.15	0.0506	1017.078
298.15	0.0605	1020.555
298.15	0.0704	1023.962
298.15	0.0801	1027.147
298.15	0.0905	1030.368
298.15	0.0997	1033.238
298.15	0.1493	1046.402
298.15	0.1985	1056.961
298.15	0.2487	1066.321
298.15	0.2998	1073.788
298.15	0.3318	1077.774
298.15	0.3981	1084.61
298.15	0.4521	1089.105
298.15	0.4934	1092.048
298.15	0.5520	1095.614
298.15	0.5846	1097.376
298.15	0.6481	1100.225
298.15	0.6773	1101.431
298.15	0.7421	1103.692
298.15	0.7811	1104.938
298.15	0.8497	1106.827
298.15	0.9002	1108.058
298.15	0.9059	1108.174
298.15	0.9120	1108.286
298.15	0.9299	1108.689
298.15	0.9413	1108.94
298.15	0.9495	1109.129
298.15	0.9546	1109.231
298.15	0.9681	1109.49
298.15	0.9789	1109.691
298.15	0.9893	1109.896
303.15	0.0101	1000.037
303.15	0.0201	1004.002
303.15	0.0302	1007.879
303.15	0.0407	1011.759
303.15	0.0506	1015.244
303.15	0.0605	1018.727
303.15	0.0704	1022.118
303.15	0.0801	1025.104
303.15	0.0905	1028.308
303.15	0.0997	1031.047
303.15	0.1493	1044.063
303.15	0.1985	1054.471
303.15	0.2487	1063.376
303.15	0.2998	1070.697
303.15	0.3318	1074.592
303.15	0.3981	1081.335
303.15	0.4521	1085.692
303.15	0.4934	1088.59
303.15	0.5520	1092.191
303.15	0.5846	1093.942
303.15	0.6481	1096.768
303.15	0.6773	1097.962
303.15	0.7421	1100.208
303.15	0.7811	1101.444
303.15	0.8497	1103.327
303.15	0.9002	1104.55
303.15	0.9059	1104.669
303.15	0.9120	1104.782
303.15	0.9299	1105.186
303.15	0.9413	1105.432
303.15	0.9495	1105.622
303.15	0.9546	1105.724
303.15	0.9681	1105.98
303.15	0.9789	1106.18
303.15	0.9893	1106.387
308.15	0.0101	998.43
308.15	0.0201	1002.324
308.15	0.0302	1006.129
308.15	0.0407	1009.896
308.15	0.0506	1013.359
308.15	0.0605	1016.685
308.15	0.0704	1019.918
308.15	0.0801	1022.9
308.15	0.0905	1026.046
308.15	0.0997	1028.71
308.15	0.1493	1041.45
308.15	0.1985	1051.737
308.15	0.2487	1060.371
308.15	0.2998	1067.567
308.15	0.3318	1071.384
308.15	0.3981	1077.992
308.15	0.4521	1082.37
308.15	0.4934	1085.257
308.15	0.5520	1088.74
308.15	0.5846	1090.48
308.15	0.6481	1093.288
308.15	0.6773	1094.476
308.15	0.7421	1096.71
308.15	0.7811	1097.939
308.15	0.8497	1099.811
308.15	0.9002	1101.031
308.15	0.9059	1101.15
308.15	0.9120	1101.26
308.15	0.9299	1101.661
308.15	0.9413	1101.909
308.15	0.9495	1102.102
308.15	0.9546	1102.203
308.15	0.9681	1102.459
308.15	0.9789	1102.654
308.15	0.9893	1102.859
293.15	0.0000	998.429
298.15	0.0000	997.267
303.15	0.0000	995.867
308.15	0.0000	994.252
293.15	1.0000	1113.725
298.15	1.0000	1110.225
303.15	1.0000	1106.715
308.15	1.0000	1103.194
293.15	0.0494	1018.402
293.15	0.0986	1034.8
293.15	0.1483	1048.464
293.15	0.2072	1061.508
293.15	0.2466	1068.682
293.15	0.2980	1076.499
293.15	0.3399	1081.798
293.15	0.3921	1087.306
293.15	0.4446	1091.877
293.15	0.5007	1095.914
293.15	0.5485	1098.81
293.15	0.6004	1101.51
293.15	0.6451	1103.534
293.15	0.7012	1105.75
293.15	0.7435	1107.221
293.15	0.7907	1108.688
293.15	0.8505	1110.325
293.15	0.8900	1111.29
293.15	0.9532	1112.691
298.15	0.0494	1016.76
298.15	0.0986	1032.776
298.15	0.1483	1046.118
298.15	0.2072	1058.856
298.15	0.2466	1065.864
298.15	0.2980	1073.506
298.15	0.3399	1078.691
298.15	0.3921	1084.091
298.15	0.4446	1088.582
298.15	0.5007	1092.559
298.15	0.5485	1095.419
298.15	0.6004	1098.092
298.15	0.6451	1100.099
298.15	0.7012	1102.3
298.15	0.7435	1103.762
298.15	0.7907	1105.219
298.15	0.8505	1106.844
298.15	0.8900	1107.803
298.15	0.9532	1109.194
303.15	0.0494	1014.981
303.15	0.0986	1030.679
303.15	0.1483	1043.727
303.15	0.2072	1056.162
303.15	0.2466	1062.997
303.15	0.2980	1070.452
303.15	0.3399	1075.516
303.15	0.3921	1080.799
303.15	0.4446	1085.21
303.15	0.5007	1089.132
303.15	0.5485	1091.967
303.15	0.6004	1094.627
303.15	0.6451	1096.629
303.15	0.7012	1098.828
303.15	0.7435	1100.287
303.15	0.7907	1101.739
303.15	0.8505	1103.353
303.15	0.8900	1104.302
303.15	0.9532	1105.684
308.15	0.0494	1013.023
308.15	0.0986	1028.374
308.15	0.1483	1041.14
308.15	0.2072	1053.317
308.15	0.2466	1060.017
308.15	0.2980	1067.333
308.15	0.3399	1072.309
308.15	0.3921	1077.509
308.15	0.4446	1081.857
308.15	0.5007	1085.732
308.15	0.5485	1088.537
308.15	0.6004	1091.172
308.15	0.6451	1093.158
308.15	0.7012	1095.34
308.15	0.7435	1096.789
308.15	0.7907	1098.231
308.15	0.8505	1099.835
308.15	0.8900	1100.78
308.15	0.9532	1102.16

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of 1,2-Ethanediol (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0989	999.06
293.15	0.1989	999.88
293.15	0.2997	1000.68
293.15	0.3948	1001.41
293.15	0.5016	1002.2
303.15	0.0989	996.47
303.15	0.1989	997.26
303.15	0.2997	998.03
303.15	0.3948	998.73
303.15	0.5016	999.48
293.15	0.0000	998.21
303.15	0.0000	995.66

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Mass fraction of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	293.15	998.2
0.0000	303.15	995.6
0.0000	313.25	992.2
0.0000	323.25	988.0
0.0000	333.35	983.1
0.9500	293.45	1109.3
0.9500	303.45	1102.4
0.9500	313.15	1095.5
0.9500	323.25	1088.3
0.9500	333.35	1081.0
1.0000	293.25	1113.6
1.0000	303.15	1106.5
1.0000	313.15	1099.2
1.0000	323.25	1091.9
1.0000	333.25	1084.6

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 98.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of 1,2-Ethanediol (1) - Liquid	Mass density, kg/m3 - Liquid
278.15	0.1018	1000.805
278.15	0.2048	1001.654
278.15	0.2949	1002.39
278.15	0.4028	1003.265
278.15	0.5086	1004.115
283.15	0.1018	1000.519
283.15	0.2048	1001.344
283.15	0.2949	1002.061
283.15	0.4028	1002.908
283.15	0.5086	1003.737
288.15	0.1018	999.9
288.15	0.2048	1000.705
288.15	0.2949	1001.404
288.15	0.4028	1002.232
288.15	0.5086	1003.038
293.15	0.1018	998.99
293.15	0.2048	999.777
293.15	0.2949	1000.46
293.15	0.4028	1001.27
293.15	0.5086	1002.058
298.15	0.1018	997.817
298.15	0.2048	998.59
298.15	0.2949	999.26
298.15	0.4028	1000.053
298.15	0.5086	1000.825
303.15	0.1018	996.408
303.15	0.2048	997.167
303.15	0.2949	997.824
303.15	0.4028	998.603
303.15	0.5086	999.362
308.15	0.1018	994.781
308.15	0.2048	995.528
308.15	0.2949	996.175
308.15	0.4028	996.94
308.15	0.5086	997.687
313.15	0.1018	992.953
313.15	0.2048	993.69
313.15	0.2949	994.327
313.15	0.4028	995.08
313.15	0.5086	995.815
318.15	0.1018	990.94
318.15	0.2048	991.667
318.15	0.2949	992.296
318.15	0.4028	993.039
318.15	0.5086	993.763
323.15	0.1018	988.755
323.15	0.2048	989.472
323.15	0.2949	990.093
323.15	0.4028	990.827
323.15	0.5086	991.539
328.15	0.1018	986.404
328.15	0.2048	987.112
328.15	0.2949	987.725
328.15	0.4028	988.451
328.15	0.5086	989.155
333.15	0.1018	983.897
333.15	0.2048	984.598
333.15	0.2949	985.204
333.15	0.4028	985.921
333.15	0.5086	986.616
338.15	0.1018	981.244
338.15	0.2048	981.938
338.15	0.2949	982.538
338.15	0.4028	983.246
338.15	0.5086	983.933
343.15	0.1018	978.449
343.15	0.2048	979.137
343.15	0.2949	979.73
343.15	0.4028	980.432
343.15	0.5086	981.112

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.9886	1119.903
288.15	0.9886	1116.426
293.15	0.9886	1112.944
298.15	0.9886	1109.463
303.15	0.9886	1105.95
308.15	0.9886	1102.43
313.15	0.9886	1098.889
323.15	0.9886	1091.746
333.15	0.9886	1084.507
343.15	0.9886	1077.163
283.15	0.9943	1120.066
288.15	0.9943	1116.59
293.15	0.9943	1113.108
298.15	0.9943	1109.613
303.15	0.9943	1106.11
308.15	0.9943	1102.586
313.15	0.9943	1099.049
323.15	0.9943	1091.903
333.15	0.9943	1084.669
343.15	0.9943	1077.326
283.15	0.9959	1120.113
288.15	0.9959	1116.638
293.15	0.9959	1113.155
298.15	0.9959	1109.661
303.15	0.9959	1106.155
308.15	0.9959	1102.634
313.15	0.9959	1099.095
323.15	0.9959	1091.952
333.15	0.9959	1084.718
343.15	0.9959	1077.37

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of 1,2-Ethanediol (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.0989	1000.117
288.15	0.1989	1000.96
288.15	0.2997	1001.786
288.15	0.3948	1002.529
288.15	0.5016	1003.347
288.15	0.5923	1004.018
288.15	0.6964	1004.757
288.15	0.7983	1005.436
298.15	0.0989	997.877
298.15	0.1989	998.688
298.15	0.2997	999.473
298.15	0.3948	1000.184
298.15	0.5016	1000.961
298.15	0.5923	1001.596
298.15	0.6964	1002.293
298.15	0.7983	1002.952
308.15	0.0989	994.84
308.15	0.1989	995.613
308.15	0.2997	996.362
308.15	0.3948	997.038
308.15	0.5016	997.764
308.15	0.5923	998.366
308.15	0.6964	999.045
308.15	0.7983	999.679
318.15	0.0989	991.134
318.15	0.1989	991.88
318.15	0.2997	992.607
318.15	0.3948	993.261
318.15	0.5016	993.973
318.15	0.5923	994.55
318.15	0.6964	995.188
318.15	0.7983	995.805

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Molality, mol/kg of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0989	293.15	999.059
0.1989	293.15	999.884
0.2997	293.15	1000.683
0.3948	293.15	1001.405
0.5016	293.15	1002.197
0.0989	298.15	997.877
0.1989	298.15	998.688
0.2997	298.15	999.473
0.3948	298.15	1000.184
0.5016	298.15	1000.961
0.0989	303.15	996.471
0.1989	303.15	997.262
0.2997	303.15	998.033
0.3948	303.15	998.733
0.5016	303.15	999.48
0.0989	308.15	994.84
0.1989	308.15	995.613
0.2997	308.15	996.362
0.3948	308.15	997.038
0.5016	308.15	997.764

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	293.15	998.2
0.0000	303.15	995.7
0.0000	313.15	992.2
0.0000	323.15	988.1
0.0000	333.15	983.2
0.0000	343.15	977.8
0.0000	353.15	971.8
0.0312	293.15	1011.7
0.0312	303.15	1006.1
0.0312	313.15	1001.3
0.0312	323.15	994.9
0.0312	333.15	989.8
0.0312	343.15	983.7
0.0312	353.15	977.1
0.0676	293.15	1024.6
0.0676	303.15	1018.4
0.0676	313.15	1010.6
0.0676	323.15	1005.1
0.0676	333.15	997.9
0.0676	343.15	991.5
0.0676	353.15	984.7
0.1105	293.15	1037.2
0.1105	303.15	1030.0
0.1105	313.15	1021.9
0.1105	323.15	1015.1
0.1105	333.15	1007.2
0.1105	343.15	1000.4
0.1105	353.15	993.6
0.1620	293.15	1051.3
0.1620	303.15	1043.4
0.1620	313.15	1034.7
0.1620	323.15	1027.4
0.1620	333.15	1019.2
0.1620	343.15	1011.5
0.1620	353.15	1003.8
0.2248	293.15	1064.8
0.2248	303.15	1056.2
0.2248	313.15	1046.8
0.2248	323.15	1038.6
0.2248	333.15	1030.3
0.2248	343.15	1022.3
0.2248	353.15	1014.0
0.3031	293.15	1076.7
0.3031	303.15	1067.5
0.3031	313.15	1057.9
0.3031	323.15	1049.2
0.3031	333.15	1040.6
0.3031	343.15	1031.9
0.3031	353.15	1023.7
0.4036	293.15	1087.8
0.4036	303.15	1078.0
0.4036	313.15	1067.9
0.4036	323.15	1059.0
0.4036	333.15	1050.3
0.4036	343.15	1041.3
0.4036	353.15	1033.0
0.5370	293.15	1097.8
0.5370	303.15	1087.0
0.5370	313.15	1077.1
0.5370	323.15	1068.0
0.5370	333.15	1059.2
0.5370	343.15	1050.1
0.5370	353.15	1042.0
0.7230	293.15	1105.7
0.7230	303.15	1095.5
0.7230	313.15	1085.8
0.7230	323.15	1076.7
0.7230	333.15	1068.0
0.7230	343.15	1058.8
0.7230	353.15	1050.9
1.0000	293.15	1113.7
1.0000	303.15	1103.2
1.0000	313.15	1093.6
1.0000	323.15	1084.7
1.0000	333.15	1076.4
1.0000	343.15	1067.5
1.0000	353.15	1060.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Mole fraction of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.2500	296.40	1068.0
0.2500	313.05	1058.0
0.2500	333.05	1045.0
0.2500	353.05	1030.0
0.2500	374.85	1013.0
0.2500	396.95	995.5
0.2500	417.15	977.4
0.2500	431.55	964.9
0.5000	297.05	1094.0
0.5000	313.05	1083.0
0.5000	333.10	1069.0
0.5000	353.05	1054.0
0.5000	376.05	1035.0
0.5000	390.25	1023.0
0.5000	406.05	1010.0
0.5000	423.55	994.5
0.5000	436.65	982.5
0.7500	297.35	1106.0
0.7500	313.05	1094.0
0.7500	333.10	1080.0
0.7500	353.05	1065.0
0.7500	373.45	1049.0
0.7500	383.35	1041.0
0.7500	393.20	1033.0
0.7500	403.15	1025.0
0.7500	404.75	1023.0
0.7500	413.15	1016.0
0.7500	418.35	1012.0
0.7500	431.95	1000.0
0.7500	445.85	987.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mass fraction of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.1000	298.15	1009.49
0.1000	303.15	1007.62
0.1000	308.15	1005.57
0.1000	318.15	1002.73
0.2000	298.15	1022.45
0.2000	303.15	1020.98
0.2000	308.15	1018.5
0.2000	318.15	1014.28
0.3000	298.15	1035.7
0.3000	303.15	1034.05
0.3000	308.15	1031.66
0.3000	318.15	1026.73
1.0000	298.15	1110.45
1.0000	303.15	1104.47
1.0000	308.15	1100.13
1.0000	318.15	1092.15

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Molality, mol/kg of Water (2) - Liquid	Speed of sound, m/s - Liquid
0.0000	1656.1
0.1028	1656.9
0.2175	1657.7
0.3155	1658.6
0.3759	1658.7
0.7031	1660.5
0.8080	1661.4
0.9282	1661.8
1.035	1662.3
1.1315	1662.7

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 92.3 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0101	1498.93
293.15	0.0201	1514.6
293.15	0.0302	1529.67
293.15	0.0407	1544.58
293.15	0.0506	1558.08
293.15	0.0605	1570.84
293.15	0.0704	1583.2
293.15	0.0801	1594.04
293.15	0.0905	1605.57
293.15	0.0997	1614.83
293.15	0.1493	1656.21
293.15	0.1985	1684.47
293.15	0.2487	1702.1
293.15	0.2998	1712.9
293.15	0.3318	1716.56
293.15	0.3981	1719.42
293.15	0.4521	1718.62
293.15	0.4934	1716.07
293.15	0.5520	1711.48
293.15	0.5846	1708.34
293.15	0.6481	1702.12
293.15	0.6773	1698.98
293.15	0.7421	1692.21
293.15	0.7811	1688.03
293.15	0.8497	1680.95
293.15	0.9002	1675.96
293.15	0.9059	1675.47
293.15	0.9120	1675.0
293.15	0.9299	1673.27
293.15	0.9413	1672.18
293.15	0.9495	1671.36
293.15	0.9546	1671.0
293.15	0.9681	1669.88
293.15	0.9789	1668.97
293.15	0.9893	1667.93
298.15	0.0101	1511.93
298.15	0.0201	1526.27
298.15	0.0302	1540.19
298.15	0.0407	1553.85
298.15	0.0506	1566.21
298.15	0.0605	1577.87
298.15	0.0704	1589.19
298.15	0.0801	1599.04
298.15	0.0905	1609.57
298.15	0.0997	1617.97
298.15	0.1493	1655.52
298.15	0.1985	1680.95
298.15	0.2487	1696.52
298.15	0.2998	1705.75
298.15	0.3318	1708.69
298.15	0.3981	1710.37
298.15	0.4521	1708.84
298.15	0.4934	1705.92
298.15	0.5520	1700.89
298.15	0.5846	1697.57
298.15	0.6481	1691.05
298.15	0.6773	1687.79
298.15	0.7421	1680.83
298.15	0.7811	1676.54
298.15	0.8497	1669.34
298.15	0.9002	1664.26
298.15	0.9059	1663.75
298.15	0.9120	1663.28
298.15	0.9299	1661.53
298.15	0.9413	1660.42
298.15	0.9495	1659.59
298.15	0.9546	1659.22
298.15	0.9681	1658.08
298.15	0.9789	1657.17
298.15	0.9893	1656.1
303.15	0.0101	1523.14
303.15	0.0201	1536.35
303.15	0.0302	1549.13
303.15	0.0407	1561.66
303.15	0.0506	1572.97
303.15	0.0605	1583.61
303.15	0.0704	1593.95
303.15	0.0801	1602.94
303.15	0.0905	1612.5
303.15	0.0997	1620.16
303.15	0.1493	1654.1
303.15	0.1985	1676.89
303.15	0.2487	1690.54
303.15	0.2998	1698.29
303.15	0.3318	1700.53
303.15	0.3981	1701.11
303.15	0.4521	1698.89
303.15	0.4934	1695.65
303.15	0.5520	1690.21
303.15	0.5846	1686.72
303.15	0.6481	1679.92
303.15	0.6773	1676.57
303.15	0.7421	1669.44
303.15	0.7811	1665.05
303.15	0.8497	1657.73
303.15	0.9002	1652.57
303.15	0.9059	1652.06
303.15	0.9120	1651.59
303.15	0.9299	1649.81
303.15	0.9413	1648.69
303.15	0.9495	1647.83
303.15	0.9546	1647.47
303.15	0.9681	1646.31
303.15	0.9789	1645.38
303.15	0.9893	1644.3
308.15	0.0101	1532.65
308.15	0.0201	1544.82
308.15	0.0302	1556.58
308.15	0.0407	1568.06
308.15	0.0506	1578.41
308.15	0.0605	1588.01
308.15	0.0704	1597.42
308.15	0.0801	1605.68
308.15	0.0905	1614.35
308.15	0.0997	1621.33
308.15	0.1493	1652.02
308.15	0.1985	1672.24
308.15	0.2487	1684.15
308.15	0.2998	1690.59
308.15	0.3318	1692.18
308.15	0.3981	1691.66
308.15	0.4521	1688.77
308.15	0.4934	1685.25
308.15	0.5520	1679.44
308.15	0.5846	1675.82
308.15	0.6481	1668.78
308.15	0.6773	1665.33
308.15	0.7421	1658.04
308.15	0.7811	1653.58
308.15	0.8497	1646.14
308.15	0.9002	1640.91
308.15	0.9059	1640.42
308.15	0.9120	1639.92
308.15	0.9299	1638.12
308.15	0.9413	1636.98
308.15	0.9495	1636.12
308.15	0.9546	1635.76
308.15	0.9681	1634.58
308.15	0.9789	1633.64
308.15	0.9893	1632.55
293.15	0.0000	1482.78
298.15	0.0000	1496.99
303.15	0.0000	1509.32
308.15	0.0000	1519.89
293.15	1.0000	1666.55
298.15	1.0000	1654.67
303.15	1.0000	1642.87
308.15	1.0000	1631.23

Speed of sound, m/s [ref]

Operational conditions:

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

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of 1,2-Ethanediol (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0989	1485.3
293.15	0.1989	1488.3
293.15	0.2997	1491.2
293.15	0.3948	1493.9
293.15	0.5016	1496.8
303.15	0.0989	1511.1
303.15	0.1989	1513.8
303.15	0.2997	1516.2
303.15	0.3948	1518.7
303.15	0.5016	1521.2
293.15	0.0000	1482.3
303.15	0.0000	1508.5

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 98.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of 1,2-Ethanediol (1) - Liquid	Speed of sound, m/s - Liquid
278.15	0.1018	1430.46
278.15	0.2048	1434.27
278.15	0.2949	1437.59
278.15	0.4028	1441.5
278.15	0.5086	1445.35
283.15	0.1018	1451.08
283.15	0.2048	1454.55
283.15	0.2949	1457.59
283.15	0.4028	1461.19
283.15	0.5086	1464.71
288.15	0.1018	1469.39
288.15	0.2048	1472.6
288.15	0.2949	1475.4
288.15	0.4028	1478.69
288.15	0.5086	1481.94
293.15	0.1018	1485.51
293.15	0.2048	1488.46
293.15	0.2949	1491.04
293.15	0.4028	1494.09
293.15	0.5086	1497.06
298.15	0.1018	1499.66
298.15	0.2048	1502.37
298.15	0.2949	1504.74
298.15	0.4028	1507.57
298.15	0.5086	1510.31
303.15	0.1018	1511.92
303.15	0.2048	1514.43
303.15	0.2949	1516.61
303.15	0.4028	1519.22
303.15	0.5086	1521.75
308.15	0.1018	1522.45
308.15	0.2048	1524.75
308.15	0.2949	1526.76
308.15	0.4028	1529.18
308.15	0.5086	1531.51
313.15	0.1018	1531.36
313.15	0.2048	1533.48
313.15	0.2949	1535.34
313.15	0.4028	1537.58
313.15	0.5086	1539.73
318.15	0.1018	1538.78
318.15	0.2048	1540.73
318.15	0.2949	1542.46
318.15	0.4028	1544.52
318.15	0.5086	1546.5
323.15	0.1018	1544.8
323.15	0.2048	1546.6
323.15	0.2949	1548.18
323.15	0.4028	1550.03
323.15	0.5086	1551.89
328.15	0.1018	1549.49
328.15	0.2048	1551.13
328.15	0.2949	1552.58
328.15	0.4028	1554.28
328.15	0.5086	1555.99
333.15	0.1018	1552.95
333.15	0.2048	1554.46
333.15	0.2949	1555.78
333.15	0.4028	1557.32
333.15	0.5086	1558.9
338.15	0.1018	1555.25
338.15	0.2048	1556.62
338.15	0.2949	1557.83
338.15	0.4028	1559.24
338.15	0.5086	1560.69
343.15	0.1018	1556.47
343.15	0.2048	1557.72
343.15	0.2949	1558.8
343.15	0.4028	1560.09
343.15	0.5086	1561.4

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Speed of sound, m/s - Liquid
283.15	0.9886	1690.2
288.15	0.9886	1678.4
293.15	0.9886	1666.6
298.15	0.9886	1654.7
303.15	0.9886	1643.0
308.15	0.9886	1631.2
313.15	0.9886	1619.5
323.15	0.9886	1595.7
333.15	0.9886	1571.7
343.15	0.9886	1547.6
283.15	0.9943	1689.0
288.15	0.9943	1678.1
293.15	0.9943	1666.3
298.15	0.9943	1654.8
303.15	0.9943	1643.0
308.15	0.9943	1631.3
313.15	0.9943	1619.4
323.15	0.9943	1595.5
333.15	0.9943	1571.5
343.15	0.9943	1547.4
283.15	0.9959	1690.6
288.15	0.9959	1678.6
293.15	0.9959	1666.6
298.15	0.9959	1654.6
303.15	0.9959	1642.7
308.15	0.9959	1630.9
313.15	0.9959	1619.1
323.15	0.9959	1595.2
333.15	0.9959	1571.2
343.15	0.9959	1547.1

Speed of sound, m/s [ref]

Operational conditions:

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

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of 1,2-Ethanediol (1) - Liquid	Speed of sound, m/s - Liquid
288.15	0.0989	1469.57
288.15	0.1989	1472.72
288.15	0.2997	1475.45
288.15	0.3948	1478.57
288.15	0.5016	1481.17
288.15	0.5923	1484.02
288.15	0.6964	1486.59
288.15	0.7983	1489.45
298.15	0.0989	1498.92
298.15	0.1989	1501.72
298.15	0.2997	1504.29
298.15	0.3948	1506.64
298.15	0.5016	1509.09
298.15	0.5923	1511.61
298.15	0.6964	1514.81
298.15	0.7983	1517.93
308.15	0.0989	1521.84
308.15	0.1989	1524.03
308.15	0.2997	1526.18
308.15	0.3948	1528.28
308.15	0.5016	1530.34
308.15	0.5923	1534.12
308.15	0.6964	1537.56
308.15	0.7983	1540.35
318.15	0.0989	1539.17
318.15	0.1989	1542.24
318.15	0.2997	1544.95
318.15	0.3948	1547.87
318.15	0.5016	1550.65
318.15	0.5923	1553.56
318.15	0.6964	1556.55
318.15	0.7983	1559.58

Speed of sound, m/s [ref]

Operational conditions:

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

Fixed		Measured
Molality, mol/kg of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
0.0989	293.15	1485.54
0.1989	293.15	1488.34
0.2997	293.15	1491.19
0.3948	293.15	1493.86
0.5016	293.15	1496.84
0.0989	298.15	1498.92
0.1989	298.15	1501.72
0.2997	298.15	1504.29
0.3948	298.15	1506.64
0.5016	298.15	1509.09
0.0989	303.15	1511.12
0.1989	303.15	1513.75
0.2997	303.15	1516.15
0.3948	303.15	1518.69
0.5016	303.15	1521.22
0.0989	308.15	1521.84
0.1989	308.15	1524.03
0.2997	308.15	1526.18
0.3948	308.15	1528.28
0.5016	308.15	1530.34

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Molality, mol/kg of Water (2) - Liquid	Speed of sound, m/s - Liquid
0.0000	1656.1
0.1028	1656.9
0.2175	1657.7
0.3155	1658.6
0.3759	1658.7
0.7031	1660.5
0.8080	1661.4
0.9282	1661.8
1.035	1662.3
1.1315	1662.7

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 92.3 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0101	1498.93
293.15	0.0201	1514.6
293.15	0.0302	1529.67
293.15	0.0407	1544.58
293.15	0.0506	1558.08
293.15	0.0605	1570.84
293.15	0.0704	1583.2
293.15	0.0801	1594.04
293.15	0.0905	1605.57
293.15	0.0997	1614.83
293.15	0.1493	1656.21
293.15	0.1985	1684.47
293.15	0.2487	1702.1
293.15	0.2998	1712.9
293.15	0.3318	1716.56
293.15	0.3981	1719.42
293.15	0.4521	1718.62
293.15	0.4934	1716.07
293.15	0.5520	1711.48
293.15	0.5846	1708.34
293.15	0.6481	1702.12
293.15	0.6773	1698.98
293.15	0.7421	1692.21
293.15	0.7811	1688.03
293.15	0.8497	1680.95
293.15	0.9002	1675.96
293.15	0.9059	1675.47
293.15	0.9120	1675.0
293.15	0.9299	1673.27
293.15	0.9413	1672.18
293.15	0.9495	1671.36
293.15	0.9546	1671.0
293.15	0.9681	1669.88
293.15	0.9789	1668.97
293.15	0.9893	1667.93
298.15	0.0101	1511.93
298.15	0.0201	1526.27
298.15	0.0302	1540.19
298.15	0.0407	1553.85
298.15	0.0506	1566.21
298.15	0.0605	1577.87
298.15	0.0704	1589.19
298.15	0.0801	1599.04
298.15	0.0905	1609.57
298.15	0.0997	1617.97
298.15	0.1493	1655.52
298.15	0.1985	1680.95
298.15	0.2487	1696.52
298.15	0.2998	1705.75
298.15	0.3318	1708.69
298.15	0.3981	1710.37
298.15	0.4521	1708.84
298.15	0.4934	1705.92
298.15	0.5520	1700.89
298.15	0.5846	1697.57
298.15	0.6481	1691.05
298.15	0.6773	1687.79
298.15	0.7421	1680.83
298.15	0.7811	1676.54
298.15	0.8497	1669.34
298.15	0.9002	1664.26
298.15	0.9059	1663.75
298.15	0.9120	1663.28
298.15	0.9299	1661.53
298.15	0.9413	1660.42
298.15	0.9495	1659.59
298.15	0.9546	1659.22
298.15	0.9681	1658.08
298.15	0.9789	1657.17
298.15	0.9893	1656.1
303.15	0.0101	1523.14
303.15	0.0201	1536.35
303.15	0.0302	1549.13
303.15	0.0407	1561.66
303.15	0.0506	1572.97
303.15	0.0605	1583.61
303.15	0.0704	1593.95
303.15	0.0801	1602.94
303.15	0.0905	1612.5
303.15	0.0997	1620.16
303.15	0.1493	1654.1
303.15	0.1985	1676.89
303.15	0.2487	1690.54
303.15	0.2998	1698.29
303.15	0.3318	1700.53
303.15	0.3981	1701.11
303.15	0.4521	1698.89
303.15	0.4934	1695.65
303.15	0.5520	1690.21
303.15	0.5846	1686.72
303.15	0.6481	1679.92
303.15	0.6773	1676.57
303.15	0.7421	1669.44
303.15	0.7811	1665.05
303.15	0.8497	1657.73
303.15	0.9002	1652.57
303.15	0.9059	1652.06
303.15	0.9120	1651.59
303.15	0.9299	1649.81
303.15	0.9413	1648.69
303.15	0.9495	1647.83
303.15	0.9546	1647.47
303.15	0.9681	1646.31
303.15	0.9789	1645.38
303.15	0.9893	1644.3
308.15	0.0101	1532.65
308.15	0.0201	1544.82
308.15	0.0302	1556.58
308.15	0.0407	1568.06
308.15	0.0506	1578.41
308.15	0.0605	1588.01
308.15	0.0704	1597.42
308.15	0.0801	1605.68
308.15	0.0905	1614.35
308.15	0.0997	1621.33
308.15	0.1493	1652.02
308.15	0.1985	1672.24
308.15	0.2487	1684.15
308.15	0.2998	1690.59
308.15	0.3318	1692.18
308.15	0.3981	1691.66
308.15	0.4521	1688.77
308.15	0.4934	1685.25
308.15	0.5520	1679.44
308.15	0.5846	1675.82
308.15	0.6481	1668.78
308.15	0.6773	1665.33
308.15	0.7421	1658.04
308.15	0.7811	1653.58
308.15	0.8497	1646.14
308.15	0.9002	1640.91
308.15	0.9059	1640.42
308.15	0.9120	1639.92
308.15	0.9299	1638.12
308.15	0.9413	1636.98
308.15	0.9495	1636.12
308.15	0.9546	1635.76
308.15	0.9681	1634.58
308.15	0.9789	1633.64
308.15	0.9893	1632.55
293.15	0.0000	1482.78
298.15	0.0000	1496.99
303.15	0.0000	1509.32
308.15	0.0000	1519.89
293.15	1.0000	1666.55
298.15	1.0000	1654.67
303.15	1.0000	1642.87
308.15	1.0000	1631.23

Speed of sound, m/s [ref]

Operational conditions:

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

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of 1,2-Ethanediol (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0989	1485.3
293.15	0.1989	1488.3
293.15	0.2997	1491.2
293.15	0.3948	1493.9
293.15	0.5016	1496.8
303.15	0.0989	1511.1
303.15	0.1989	1513.8
303.15	0.2997	1516.2
303.15	0.3948	1518.7
303.15	0.5016	1521.2
293.15	0.0000	1482.3
303.15	0.0000	1508.5

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 98.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of 1,2-Ethanediol (1) - Liquid	Speed of sound, m/s - Liquid
278.15	0.1018	1430.46
278.15	0.2048	1434.27
278.15	0.2949	1437.59
278.15	0.4028	1441.5
278.15	0.5086	1445.35
283.15	0.1018	1451.08
283.15	0.2048	1454.55
283.15	0.2949	1457.59
283.15	0.4028	1461.19
283.15	0.5086	1464.71
288.15	0.1018	1469.39
288.15	0.2048	1472.6
288.15	0.2949	1475.4
288.15	0.4028	1478.69
288.15	0.5086	1481.94
293.15	0.1018	1485.51
293.15	0.2048	1488.46
293.15	0.2949	1491.04
293.15	0.4028	1494.09
293.15	0.5086	1497.06
298.15	0.1018	1499.66
298.15	0.2048	1502.37
298.15	0.2949	1504.74
298.15	0.4028	1507.57
298.15	0.5086	1510.31
303.15	0.1018	1511.92
303.15	0.2048	1514.43
303.15	0.2949	1516.61
303.15	0.4028	1519.22
303.15	0.5086	1521.75
308.15	0.1018	1522.45
308.15	0.2048	1524.75
308.15	0.2949	1526.76
308.15	0.4028	1529.18
308.15	0.5086	1531.51
313.15	0.1018	1531.36
313.15	0.2048	1533.48
313.15	0.2949	1535.34
313.15	0.4028	1537.58
313.15	0.5086	1539.73
318.15	0.1018	1538.78
318.15	0.2048	1540.73
318.15	0.2949	1542.46
318.15	0.4028	1544.52
318.15	0.5086	1546.5
323.15	0.1018	1544.8
323.15	0.2048	1546.6
323.15	0.2949	1548.18
323.15	0.4028	1550.03
323.15	0.5086	1551.89
328.15	0.1018	1549.49
328.15	0.2048	1551.13
328.15	0.2949	1552.58
328.15	0.4028	1554.28
328.15	0.5086	1555.99
333.15	0.1018	1552.95
333.15	0.2048	1554.46
333.15	0.2949	1555.78
333.15	0.4028	1557.32
333.15	0.5086	1558.9
338.15	0.1018	1555.25
338.15	0.2048	1556.62
338.15	0.2949	1557.83
338.15	0.4028	1559.24
338.15	0.5086	1560.69
343.15	0.1018	1556.47
343.15	0.2048	1557.72
343.15	0.2949	1558.8
343.15	0.4028	1560.09
343.15	0.5086	1561.4

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Speed of sound, m/s - Liquid
283.15	0.9886	1690.2
288.15	0.9886	1678.4
293.15	0.9886	1666.6
298.15	0.9886	1654.7
303.15	0.9886	1643.0
308.15	0.9886	1631.2
313.15	0.9886	1619.5
323.15	0.9886	1595.7
333.15	0.9886	1571.7
343.15	0.9886	1547.6
283.15	0.9943	1689.0
288.15	0.9943	1678.1
293.15	0.9943	1666.3
298.15	0.9943	1654.8
303.15	0.9943	1643.0
308.15	0.9943	1631.3
313.15	0.9943	1619.4
323.15	0.9943	1595.5
333.15	0.9943	1571.5
343.15	0.9943	1547.4
283.15	0.9959	1690.6
288.15	0.9959	1678.6
293.15	0.9959	1666.6
298.15	0.9959	1654.6
303.15	0.9959	1642.7
308.15	0.9959	1630.9
313.15	0.9959	1619.1
323.15	0.9959	1595.2
333.15	0.9959	1571.2
343.15	0.9959	1547.1

Speed of sound, m/s [ref]

Operational conditions:

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

Fixed		Measured
Temperature, K - Liquid	Molality, mol/kg of 1,2-Ethanediol (1) - Liquid	Speed of sound, m/s - Liquid
288.15	0.0989	1469.57
288.15	0.1989	1472.72
288.15	0.2997	1475.45
288.15	0.3948	1478.57
288.15	0.5016	1481.17
288.15	0.5923	1484.02
288.15	0.6964	1486.59
288.15	0.7983	1489.45
298.15	0.0989	1498.92
298.15	0.1989	1501.72
298.15	0.2997	1504.29
298.15	0.3948	1506.64
298.15	0.5016	1509.09
298.15	0.5923	1511.61
298.15	0.6964	1514.81
298.15	0.7983	1517.93
308.15	0.0989	1521.84
308.15	0.1989	1524.03
308.15	0.2997	1526.18
308.15	0.3948	1528.28
308.15	0.5016	1530.34
308.15	0.5923	1534.12
308.15	0.6964	1537.56
308.15	0.7983	1540.35
318.15	0.0989	1539.17
318.15	0.1989	1542.24
318.15	0.2997	1544.95
318.15	0.3948	1547.87
318.15	0.5016	1550.65
318.15	0.5923	1553.56
318.15	0.6964	1556.55
318.15	0.7983	1559.58

Speed of sound, m/s [ref]

Operational conditions:

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

Fixed		Measured
Molality, mol/kg of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
0.0989	293.15	1485.54
0.1989	293.15	1488.34
0.2997	293.15	1491.19
0.3948	293.15	1493.86
0.5016	293.15	1496.84
0.0989	298.15	1498.92
0.1989	298.15	1501.72
0.2997	298.15	1504.29
0.3948	298.15	1506.64
0.5016	298.15	1509.09
0.0989	303.15	1511.12
0.1989	303.15	1513.75
0.2997	303.15	1516.15
0.3948	303.15	1518.69
0.5016	303.15	1521.22
0.0989	308.15	1521.84
0.1989	308.15	1524.03
0.2997	308.15	1526.18
0.3948	308.15	1528.28
0.5016	308.15	1530.34

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
283.15	0.0078	0.0735
283.15	0.0132	0.0726
283.15	0.0216	0.0712
283.15	0.0334	0.0699
283.15	0.0498	0.0686
283.15	0.0632	0.0672
283.15	0.0875	0.0650
283.15	0.1152	0.0639
283.15	0.1436	0.0622
283.15	0.1635	0.0608
283.15	0.2002	0.0593
283.15	0.2509	0.0577
283.15	0.2895	0.0565
283.15	0.4112	0.0545
283.15	0.4753	0.0532
283.15	0.6668	0.0516
283.15	0.7562	0.0508
283.15	0.8958	0.0498
298.15	0.0083	0.0712
298.15	0.0144	0.0704
298.15	0.0246	0.0693
298.15	0.0351	0.0681
298.15	0.0466	0.0669
298.15	0.0556	0.0661
298.15	0.0899	0.0637
298.15	0.1042	0.0627
298.15	0.1342	0.0612
298.15	0.1624	0.0600
298.15	0.1989	0.0585
298.15	0.2499	0.0569
298.15	0.2996	0.0556
298.15	0.4010	0.0536
298.15	0.4999	0.0522
298.15	0.6500	0.0507
298.15	0.7500	0.0498
298.15	0.8987	0.0487
308.15	0.0080	0.0691
308.15	0.0141	0.0683
308.15	0.0253	0.0668
308.15	0.0353	0.0657
308.15	0.0511	0.0641
308.15	0.0556	0.0637
308.15	0.0905	0.0611
308.15	0.1113	0.0599
308.15	0.1445	0.0583
308.15	0.1602	0.0576
308.15	0.2132	0.0558
308.15	0.2485	0.0549
308.15	0.3201	0.0534
308.15	0.4126	0.0520
308.15	0.5054	0.0508
308.15	0.6501	0.0495
308.15	0.7406	0.0488
308.15	0.8875	0.0479

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

Operational condition: Temperature, K = 298.15 (Liquid)

Volume fraction of 1,2-Ethanediol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.0000	0.0718
0.1000	0.0683
0.2000	0.0648
0.3000	0.0615

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

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of 1,2-Ethanediol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.0083	0.0708
0.0101	0.0707
0.0118	0.0704
0.0142	0.0702
0.0158	0.0697
0.0182	0.0696
0.0200	0.0694
0.0220	0.0692
0.0249	0.0688
0.0299	0.0682
0.0354	0.0677
0.0401	0.0673
0.0452	0.0666
0.1010	0.0625
0.2000	0.0579

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
308.15	0.0000	0.0710
308.15	0.0145	0.0697
308.15	0.0312	0.0678
308.15	0.0484	0.0661
308.15	0.0686	0.0646
308.15	0.0883	0.0633
308.15	0.1107	0.0621
308.15	0.1621	0.0600
308.15	0.2247	0.0575
308.15	0.3032	0.0560
308.15	0.4035	0.0540
308.15	0.5366	0.0525
308.15	1.0000	0.0501
313.15	0.0000	0.0697
313.15	0.0145	0.0666
313.15	0.0312	0.0656
313.15	0.0484	0.0641
313.15	0.0686	0.0625
313.15	0.0883	0.0613
313.15	0.1107	0.0603
313.15	0.1621	0.0581
313.15	0.2247	0.0559
313.15	0.3032	0.0544
313.15	0.4035	0.0524
313.15	0.5366	0.0507
313.15	1.0000	0.0487
318.15	0.0000	0.0677
318.15	0.0145	0.0659
318.15	0.0312	0.0639
318.15	0.0484	0.0622
318.15	0.0686	0.0606
318.15	0.0883	0.0592
318.15	0.1107	0.0584
318.15	0.1621	0.0563
318.15	0.2247	0.0544
318.15	0.3032	0.0527
318.15	0.4035	0.0506
318.15	0.5366	0.0493
318.15	1.0000	0.0473
323.15	0.0000	0.0661
323.15	0.0145	0.0632
323.15	0.0312	0.0606
323.15	0.0484	0.0596
323.15	0.0686	0.0580
323.15	0.0883	0.0568
323.15	0.1107	0.0558
323.15	0.1621	0.0542
323.15	0.2247	0.0522
323.15	0.3032	0.0505
323.15	0.4035	0.0491
323.15	0.5366	0.0479
323.15	1.0000	0.0464

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
283.15	0.0078	0.0735
283.15	0.0132	0.0726
283.15	0.0216	0.0712
283.15	0.0334	0.0699
283.15	0.0498	0.0686
283.15	0.0632	0.0672
283.15	0.0875	0.0650
283.15	0.1152	0.0639
283.15	0.1436	0.0622
283.15	0.1635	0.0608
283.15	0.2002	0.0593
283.15	0.2509	0.0577
283.15	0.2895	0.0565
283.15	0.4112	0.0545
283.15	0.4753	0.0532
283.15	0.6668	0.0516
283.15	0.7562	0.0508
283.15	0.8958	0.0498
298.15	0.0083	0.0712
298.15	0.0144	0.0704
298.15	0.0246	0.0693
298.15	0.0351	0.0681
298.15	0.0466	0.0669
298.15	0.0556	0.0661
298.15	0.0899	0.0637
298.15	0.1042	0.0627
298.15	0.1342	0.0612
298.15	0.1624	0.0600
298.15	0.1989	0.0585
298.15	0.2499	0.0569
298.15	0.2996	0.0556
298.15	0.4010	0.0536
298.15	0.4999	0.0522
298.15	0.6500	0.0507
298.15	0.7500	0.0498
298.15	0.8987	0.0487
308.15	0.0080	0.0691
308.15	0.0141	0.0683
308.15	0.0253	0.0668
308.15	0.0353	0.0657
308.15	0.0511	0.0641
308.15	0.0556	0.0637
308.15	0.0905	0.0611
308.15	0.1113	0.0599
308.15	0.1445	0.0583
308.15	0.1602	0.0576
308.15	0.2132	0.0558
308.15	0.2485	0.0549
308.15	0.3201	0.0534
308.15	0.4126	0.0520
308.15	0.5054	0.0508
308.15	0.6501	0.0495
308.15	0.7406	0.0488
308.15	0.8875	0.0479

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

Operational condition: Temperature, K = 298.15 (Liquid)

Volume fraction of 1,2-Ethanediol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.0000	0.0718
0.1000	0.0683
0.2000	0.0648
0.3000	0.0615

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

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of 1,2-Ethanediol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.0083	0.0708
0.0101	0.0707
0.0118	0.0704
0.0142	0.0702
0.0158	0.0697
0.0182	0.0696
0.0200	0.0694
0.0220	0.0692
0.0249	0.0688
0.0299	0.0682
0.0354	0.0677
0.0401	0.0673
0.0452	0.0666
0.1010	0.0625
0.2000	0.0579

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

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
308.15	0.0000	0.0710
308.15	0.0145	0.0697
308.15	0.0312	0.0678
308.15	0.0484	0.0661
308.15	0.0686	0.0646
308.15	0.0883	0.0633
308.15	0.1107	0.0621
308.15	0.1621	0.0600
308.15	0.2247	0.0575
308.15	0.3032	0.0560
308.15	0.4035	0.0540
308.15	0.5366	0.0525
308.15	1.0000	0.0501
313.15	0.0000	0.0697
313.15	0.0145	0.0666
313.15	0.0312	0.0656
313.15	0.0484	0.0641
313.15	0.0686	0.0625
313.15	0.0883	0.0613
313.15	0.1107	0.0603
313.15	0.1621	0.0581
313.15	0.2247	0.0559
313.15	0.3032	0.0544
313.15	0.4035	0.0524
313.15	0.5366	0.0507
313.15	1.0000	0.0487
318.15	0.0000	0.0677
318.15	0.0145	0.0659
318.15	0.0312	0.0639
318.15	0.0484	0.0622
318.15	0.0686	0.0606
318.15	0.0883	0.0592
318.15	0.1107	0.0584
318.15	0.1621	0.0563
318.15	0.2247	0.0544
318.15	0.3032	0.0527
318.15	0.4035	0.0506
318.15	0.5366	0.0493
318.15	1.0000	0.0473
323.15	0.0000	0.0661
323.15	0.0145	0.0632
323.15	0.0312	0.0606
323.15	0.0484	0.0596
323.15	0.0686	0.0580
323.15	0.0883	0.0568
323.15	0.1107	0.0558
323.15	0.1621	0.0542
323.15	0.2247	0.0522
323.15	0.3032	0.0505
323.15	0.4035	0.0491
323.15	0.5366	0.0479
323.15	1.0000	0.0464

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Water (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.1792	424.82
0.2468	415.59
0.3181	407.93
0.3805	402.37
0.4451	397.48
0.5845	388.93

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Pressure, kPa - Liquid	Mole fraction of Water (2) - Liquid	Boiling temperature at pressure P, K - Liquid
100.00	0.9990	372.60
100.00	0.9830	373.35
100.00	0.9660	374.11
100.00	0.9580	374.67
100.00	0.9230	375.61
100.00	0.8800	377.15
100.00	0.8290	378.61
100.00	0.7910	380.45
100.00	0.7650	380.97
100.00	0.7220	382.75
100.00	0.6930	383.75
100.00	0.6540	386.20
100.00	0.5700	389.60
100.00	0.4940	395.15
100.00	0.4550	398.72
100.00	0.4130	402.25
100.00	0.3170	410.95
70.00	0.9990	362.52
70.00	0.9620	364.60
70.00	0.8790	366.79
70.00	0.8620	367.81
70.00	0.8040	369.03
70.00	0.7790	370.15
70.00	0.7460	371.50
70.00	0.7430	371.58
70.00	0.6560	376.19
70.00	0.6040	378.50
70.00	0.5440	380.77
70.00	0.4830	385.07
70.00	0.4140	389.33
70.00	0.3530	395.81
70.00	0.2840	402.27
50.00	0.9990	353.64
50.00	0.9660	355.15
50.00	0.9280	356.65
50.00	0.9030	357.51
50.00	0.8900	357.31
50.00	0.8510	358.54
50.00	0.7610	361.70
50.00	0.7150	363.65
50.00	0.6560	366.27
50.00	0.6260	366.87
50.00	0.6160	367.49
50.00	0.6080	367.90
50.00	0.5380	371.65
50.00	0.4860	374.68
50.00	0.4270	378.67
50.00	0.3630	384.98
50.00	0.2910	392.25

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Water (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0200	462.57
0.0630	448.77
0.1040	438.69
0.1280	433.60
0.1670	426.70
0.1970	422.03
0.2500	415.27
0.2790	411.98
0.3170	408.00
0.3460	405.33
0.4090	400.18
0.4440	397.27
0.5010	393.53
0.5570	390.22
0.6740	384.51
0.7470	381.51
0.7970	379.47
0.8610	377.30
0.9000	376.05

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Water (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.1792	424.82
0.2468	415.59
0.3181	407.93
0.3805	402.37
0.4451	397.48
0.5845	388.93

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Pressure, kPa - Liquid	Mole fraction of Water (2) - Liquid	Boiling temperature at pressure P, K - Liquid
100.00	0.9990	372.60
100.00	0.9830	373.35
100.00	0.9660	374.11
100.00	0.9580	374.67
100.00	0.9230	375.61
100.00	0.8800	377.15
100.00	0.8290	378.61
100.00	0.7910	380.45
100.00	0.7650	380.97
100.00	0.7220	382.75
100.00	0.6930	383.75
100.00	0.6540	386.20
100.00	0.5700	389.60
100.00	0.4940	395.15
100.00	0.4550	398.72
100.00	0.4130	402.25
100.00	0.3170	410.95
70.00	0.9990	362.52
70.00	0.9620	364.60
70.00	0.8790	366.79
70.00	0.8620	367.81
70.00	0.8040	369.03
70.00	0.7790	370.15
70.00	0.7460	371.50
70.00	0.7430	371.58
70.00	0.6560	376.19
70.00	0.6040	378.50
70.00	0.5440	380.77
70.00	0.4830	385.07
70.00	0.4140	389.33
70.00	0.3530	395.81
70.00	0.2840	402.27
50.00	0.9990	353.64
50.00	0.9660	355.15
50.00	0.9280	356.65
50.00	0.9030	357.51
50.00	0.8900	357.31
50.00	0.8510	358.54
50.00	0.7610	361.70
50.00	0.7150	363.65
50.00	0.6560	366.27
50.00	0.6260	366.87
50.00	0.6160	367.49
50.00	0.6080	367.90
50.00	0.5380	371.65
50.00	0.4860	374.68
50.00	0.4270	378.67
50.00	0.3630	384.98
50.00	0.2910	392.25

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Water (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0200	462.57
0.0630	448.77
0.1040	438.69
0.1280	433.60
0.1670	426.70
0.1970	422.03
0.2500	415.27
0.2790	411.98
0.3170	408.00
0.3460	405.33
0.4090	400.18
0.4440	397.27
0.5010	393.53
0.5570	390.22
0.6740	384.51
0.7470	381.51
0.7970	379.47
0.8610	377.30
0.9000	376.05

Thermal conductivity, W/m/K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Mole fraction of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Thermal conductivity, W/m/K - Liquid
0.2500	303.40	0.3910
0.2500	323.60	0.4000
0.2500	348.60	0.4160
0.2500	372.00	0.4230
0.2500	395.90	0.4280
0.2500	421.00	0.4320
0.5000	312.30	0.3160
0.5000	324.40	0.3140
0.5000	347.70	0.3240
0.5000	372.80	0.3300
0.5000	397.00	0.3320
0.5000	421.70	0.3200
0.7500	298.50	0.2690
0.7500	324.20	0.2720
0.7500	347.50	0.2770
0.7500	371.90	0.2810
0.7500	396.80	0.2800
0.7500	419.90	0.2790
0.7500	441.60	0.2760

Thermal conductivity, W/m/K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Mole fraction of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Thermal conductivity, W/m/K - Liquid
0.2500	303.40	0.3910
0.2500	323.60	0.4000
0.2500	348.60	0.4160
0.2500	372.00	0.4230
0.2500	395.90	0.4280
0.2500	421.00	0.4320
0.5000	312.30	0.3160
0.5000	324.40	0.3140
0.5000	347.70	0.3240
0.5000	372.80	0.3300
0.5000	397.00	0.3320
0.5000	421.70	0.3200
0.7500	298.50	0.2690
0.7500	324.20	0.2720
0.7500	347.50	0.2770
0.7500	371.90	0.2810
0.7500	396.80	0.2800
0.7500	419.90	0.2790
0.7500	441.60	0.2760

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

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

Temperature, K - Liquid	Binary diffusion coefficient, m2/s - Liquid
303.20	0.0000
308.20	0.0000
313.20	0.0000
318.20	0.0000
323.20	0.0000

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.2 (Liquid)

Mole fraction of 1,2-Ethanediol (1) - Liquid	Binary diffusion coefficient, m2/s - Liquid
0.0000	0.0000
0.2000	0.0000
0.4000	0.0000
0.6000	0.0000
0.8000	0.0000

Binary diffusion coefficient, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Binary diffusion coefficient, m2/s - Liquid
0.2000	303.20	0.0000
0.2000	308.20	0.0000
0.2000	313.20	0.0000
0.2000	318.20	0.0000
0.2000	323.20	0.0000
0.4000	303.20	0.0000
0.4000	308.20	0.0000
0.4000	313.20	0.0000
0.4000	318.20	0.0000
0.4000	323.20	0.0000
0.6000	303.20	0.0000
0.6000	308.20	0.0000
0.6000	313.20	0.0000
0.6000	318.20	0.0000
0.6000	323.20	0.0000
0.8000	303.20	0.0000
0.8000	308.20	0.0000
0.8000	313.20	0.0000
0.8000	318.20	0.0000
0.8000	323.20	0.0000

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Mole fraction = 0.2 (Liquid)

Temperature, K - Liquid	Binary diffusion coefficient, m2/s - Liquid
303.15	0.0000
308.15	0.0000
313.15	0.0000
318.15	0.0000
323.15	0.0000

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.2 (Liquid)

Mole fraction of 1,2-Ethanediol (1) - Liquid	Binary diffusion coefficient, m2/s - Liquid
0.0323	0.0000
0.0698	0.0000
0.1140	0.0000
0.1667	0.0000
0.2420	0.0000
0.3104	0.0000
0.4119	0.0000
0.5456	0.0000
0.7298	0.0000

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

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

Temperature, K - Liquid	Binary diffusion coefficient, m2/s - Liquid
303.20	0.0000
308.20	0.0000
313.20	0.0000
318.20	0.0000
323.20	0.0000

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.2 (Liquid)

Mole fraction of 1,2-Ethanediol (1) - Liquid	Binary diffusion coefficient, m2/s - Liquid
0.0000	0.0000
0.2000	0.0000
0.4000	0.0000
0.6000	0.0000
0.8000	0.0000

Binary diffusion coefficient, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of 1,2-Ethanediol (1) - Liquid	Temperature, K - Liquid	Binary diffusion coefficient, m2/s - Liquid
0.2000	303.20	0.0000
0.2000	308.20	0.0000
0.2000	313.20	0.0000
0.2000	318.20	0.0000
0.2000	323.20	0.0000
0.4000	303.20	0.0000
0.4000	308.20	0.0000
0.4000	313.20	0.0000
0.4000	318.20	0.0000
0.4000	323.20	0.0000
0.6000	303.20	0.0000
0.6000	308.20	0.0000
0.6000	313.20	0.0000
0.6000	318.20	0.0000
0.6000	323.20	0.0000
0.8000	303.20	0.0000
0.8000	308.20	0.0000
0.8000	313.20	0.0000
0.8000	318.20	0.0000
0.8000	323.20	0.0000

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Mole fraction = 0.2 (Liquid)

Temperature, K - Liquid	Binary diffusion coefficient, m2/s - Liquid
303.15	0.0000
308.15	0.0000
313.15	0.0000
318.15	0.0000
323.15	0.0000

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.2 (Liquid)

Mole fraction of 1,2-Ethanediol (1) - Liquid	Binary diffusion coefficient, m2/s - Liquid
0.0323	0.0000
0.0698	0.0000
0.1140	0.0000
0.1667	0.0000
0.2420	0.0000
0.3104	0.0000
0.4119	0.0000
0.5456	0.0000
0.7298	0.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Water (2) - Liquid	y1[mol/mol] of Water (2) - Vapour
448.95	0.0303	0.5750
411.75	0.1198	0.9389
400.75	0.1906	0.9760
394.75	0.2305	0.9818
388.95	0.3593	0.9821
380.45	0.5689	0.9911
375.95	0.7412	0.9953
373.95	0.7979	0.9974
374.65	0.8803	0.9982
375.65	0.9239	0.9988
373.65	0.9667	0.9994

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 1.3332 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Water (2) - Liquid	y1[mol/mol] of Water (2) - Vapour
360.15	0.0080	0.3320
359.15	0.0120	0.4370
350.25	0.0280	0.6790
339.45	0.0510	0.8290
335.95	0.0740	0.8800
335.15	0.1030	0.9170
326.65	0.1450	0.9500
320.35	0.1960	0.9690
308.25	0.3190	0.9870
302.35	0.3920	0.9920
296.65	0.5170	0.9958
295.15	0.5900	0.9971
293.45	0.6480	0.9978
292.65	0.7010	0.9983
291.55	0.7560	0.9987

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 3.333 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Water (2) - Liquid	y1[mol/mol] of Water (2) - Vapour
376.65	0.0090	0.3020
366.95	0.0240	0.5630
356.15	0.0530	0.7790
347.65	0.1000	0.8960
337.15	0.1520	0.9440
330.15	0.2180	0.9700
321.25	0.3150	0.9840
315.95	0.4040	0.9905
312.15	0.5100	0.9940
309.95	0.5980	0.9960
306.15	0.7060	0.9978
303.55	0.7950	0.9987

Specific volume, m3/kg [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Volume fraction = 0.75 (Liquid)

Temperature, K - Liquid	Specific volume, m3/kg - Liquid
288.13	0.0009
273.15	0.0009
274.15	0.0009
275.15	0.0009
276.15	0.0009
277.15	0.0009
278.15	0.0009
279.15	0.0009
280.15	0.0009
281.15	0.0009
282.15	0.0009
283.16	0.0009
284.16	0.0009
285.16	0.0009
286.16	0.0009
287.16	0.0009
288.16	0.0009
289.16	0.0009
290.16	0.0009
291.16	0.0009
292.15	0.0009
293.15	0.0009
294.15	0.0009
295.16	0.0009
296.16	0.0009
297.15	0.0009
298.15	0.0009
299.15	0.0009
300.16	0.0009
301.16	0.0009
302.16	0.0009
303.16	0.0009
304.16	0.0009
305.16	0.0009
306.16	0.0009
307.15	0.0009
308.15	0.0009
309.15	0.0009
310.15	0.0009
311.15	0.0009
312.15	0.0009
313.15	0.0009
288.11	0.0009
288.09	0.0009

Specific volume, m3/kg [ref]

Operational condition: Volume fraction = 0.75 (Liquid)

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Specific volume, m3/kg - Liquid
49300.00	288.33	0.0009
49400.00	288.13	0.0009
49700.00	288.11	0.0009
98200.00	288.12	0.0009
98200.00	288.10	0.0009
100900.00	288.36	0.0009
148600.00	288.09	0.0009
149300.00	288.33	0.0009
149800.00	288.14	0.0009
199000.00	288.14	0.0009
199100.00	288.15	0.0009
199200.00	288.31	0.0009
248700.00	288.16	0.0009
250600.00	288.19	0.0009
251000.00	288.32	0.0009
299600.00	288.29	0.0008
299900.00	288.17	0.0008
300300.00	288.33	0.0008
348300.00	288.33	0.0008
349300.00	288.13	0.0008
350200.00	288.31	0.0008

Specific volume, m3/kg [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Volume fraction = 0.75 (Liquid)

Temperature, K - Liquid	Specific volume, m3/kg - Liquid
288.13	0.0009
273.15	0.0009
274.15	0.0009
275.15	0.0009
276.15	0.0009
277.15	0.0009
278.15	0.0009
279.15	0.0009
280.15	0.0009
281.15	0.0009
282.15	0.0009
283.16	0.0009
284.16	0.0009
285.16	0.0009
286.16	0.0009
287.16	0.0009
288.16	0.0009
289.16	0.0009
290.16	0.0009
291.16	0.0009
292.15	0.0009
293.15	0.0009
294.15	0.0009
295.16	0.0009
296.16	0.0009
297.15	0.0009
298.15	0.0009
299.15	0.0009
300.16	0.0009
301.16	0.0009
302.16	0.0009
303.16	0.0009
304.16	0.0009
305.16	0.0009
306.16	0.0009
307.15	0.0009
308.15	0.0009
309.15	0.0009
310.15	0.0009
311.15	0.0009
312.15	0.0009
313.15	0.0009
288.11	0.0009
288.09	0.0009

Specific volume, m3/kg [ref]

Operational condition: Volume fraction = 0.75 (Liquid)

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Specific volume, m3/kg - Liquid
49300.00	288.33	0.0009
49400.00	288.13	0.0009
49700.00	288.11	0.0009
98200.00	288.12	0.0009
98200.00	288.10	0.0009
100900.00	288.36	0.0009
148600.00	288.09	0.0009
149300.00	288.33	0.0009
149800.00	288.14	0.0009
199000.00	288.14	0.0009
199100.00	288.15	0.0009
199200.00	288.31	0.0009
248700.00	288.16	0.0009
250600.00	288.19	0.0009
251000.00	288.32	0.0009
299600.00	288.29	0.0008
299900.00	288.17	0.0008
300300.00	288.33	0.0008
348300.00	288.33	0.0008
349300.00	288.13	0.0008
350200.00	288.31	0.0008

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Excess molar volume, m3/mol - Liquid
283.15	0.0099	-1.5900e-08
283.15	0.0126	-2.0000e-08
283.15	0.0262	-4.2000e-08
283.15	0.0464	-7.7700e-08
283.15	0.0752	-1.2900e-07
283.15	0.0951	-1.6630e-07
283.15	0.1016	-1.7600e-07
283.15	0.1245	-2.1300e-07
283.15	0.1491	-2.5030e-07
283.15	0.1731	-2.8120e-07
283.15	0.2000	-3.1290e-07
283.15	0.2004	-3.1110e-07
283.15	0.2083	-3.1960e-07
283.15	0.2203	-3.2900e-07
283.15	0.2501	-3.5420e-07
283.15	0.2903	-3.7940e-07
283.15	0.4076	-4.0060e-07
283.15	0.4641	-3.9100e-07
283.15	0.6066	-3.2850e-07
283.15	0.6959	-2.6820e-07
283.15	0.7788	-2.0170e-07
283.15	0.7988	-1.8520e-07
283.15	0.8040	-1.7970e-07
283.15	0.8463	-1.4250e-07
283.15	0.8864	-1.0630e-07
283.15	0.9308	-6.4200e-08
283.15	0.9395	-5.5000e-08
293.15	0.0099	-1.3400e-08
293.15	0.0126	-1.7200e-08
293.15	0.0262	-3.7300e-08
293.15	0.0464	-6.9500e-08
293.15	0.0752	-1.1510e-07
293.15	0.0951	-1.4850e-07
293.15	0.1016	-1.5710e-07
293.15	0.1245	-1.9010e-07
293.15	0.1491	-2.2360e-07
293.15	0.1731	-2.5160e-07
293.15	0.2000	-2.8050e-07
293.15	0.2004	-2.7880e-07
293.15	0.2083	-2.8660e-07
293.15	0.2203	-2.9520e-07
293.15	0.2501	-3.1860e-07
293.15	0.2903	-3.4230e-07
293.15	0.4076	-3.6390e-07
293.15	0.4641	-3.5600e-07
293.15	0.6066	-3.0070e-07
293.15	0.6959	-2.4600e-07
293.15	0.7788	-1.8530e-07
293.15	0.7988	-1.7030e-07
293.15	0.8040	-1.6510e-07
293.15	0.8463	-1.3090e-07
293.15	0.8864	-9.7800e-08
293.15	0.9308	-5.9000e-08
293.15	0.9395	-5.0300e-08
298.15	0.0099	-1.2300e-08
298.15	0.0126	-1.6000e-08
298.15	0.0262	-3.5400e-08
298.15	0.0464	-6.6300e-08
298.15	0.0752	-1.0970e-07
298.15	0.0951	-1.4150e-07
298.15	0.1016	-1.4960e-07
298.15	0.1245	-1.8100e-07
298.15	0.1491	-2.1290e-07
298.15	0.1731	-2.3960e-07
298.15	0.2000	-2.6740e-07
298.15	0.2004	-2.6560e-07
298.15	0.2083	-2.7310e-07
298.15	0.2203	-2.8130e-07
298.15	0.2501	-3.0380e-07
298.15	0.2903	-3.2690e-07
298.15	0.4076	-3.4840e-07
298.15	0.4641	-3.4120e-07
298.15	0.6066	-2.8870e-07
298.15	0.6959	-2.3640e-07
298.15	0.7788	-1.7820e-07
298.15	0.7988	-1.6380e-07
298.15	0.8040	-1.5870e-07
298.15	0.8463	-1.2600e-07
298.15	0.8864	-9.4000e-08
298.15	0.9308	-5.6800e-08
298.15	0.9395	-4.8300e-08
303.15	0.0099	-1.1300e-08
303.15	0.0126	-1.4900e-08
303.15	0.0262	-3.3800e-08
303.15	0.0464	-6.3500e-08
303.15	0.0752	-1.0510e-07
303.15	0.0951	-1.3540e-07
303.15	0.1016	-1.4310e-07
303.15	0.1245	-1.7300e-07
303.15	0.1491	-2.0350e-07
303.15	0.1731	-2.2900e-07
303.15	0.2000	-2.5550e-07
303.15	0.2004	-2.5380e-07
303.15	0.2083	-2.6110e-07
303.15	0.2203	-2.6900e-07
303.15	0.2501	-2.9070e-07
303.15	0.2903	-3.1300e-07
303.15	0.4076	-3.3440e-07
303.15	0.4641	-3.2770e-07
303.15	0.6066	-2.7790e-07
303.15	0.6959	-2.2780e-07
303.15	0.7788	-1.7170e-07
303.15	0.7988	-1.5790e-07
303.15	0.8040	-1.5300e-07
303.15	0.8463	-1.2140e-07
303.15	0.8864	-9.0600e-08
303.15	0.9308	-5.4600e-08
303.15	0.9395	-4.6600e-08
313.15	0.0099	-0.0000
313.15	0.0126	-1.2900e-08
313.15	0.0262	-3.0700e-08
313.15	0.0464	-5.8900e-08
313.15	0.0752	-9.7200e-08
313.15	0.0951	-1.2520e-07
313.15	0.1016	-1.3220e-07
313.15	0.1245	-1.5960e-07
313.15	0.1491	-1.8750e-07
313.15	0.1731	-2.1110e-07
313.15	0.2000	-2.3560e-07
313.15	0.2004	-2.3390e-07
313.15	0.2083	-2.4050e-07
313.15	0.2203	-2.4780e-07
313.15	0.2501	-2.6800e-07
313.15	0.2903	-2.8900e-07
313.15	0.4076	-3.0990e-07
313.15	0.4641	-3.0420e-07
313.15	0.6066	-2.5890e-07
313.15	0.6959	-2.1270e-07
313.15	0.7788	-1.6050e-07
313.15	0.7988	-1.4750e-07
313.15	0.8040	-1.4310e-07
313.15	0.8463	-1.1360e-07
313.15	0.8864	-8.4800e-08
313.15	0.9308	-5.1000e-08
313.15	0.9395	-4.3500e-08

Partial molar volume, m3/mol of 1,2-Ethanediol (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Partial molar volume, m3/mol of 1,2-Ethanediol (1) - Liquid
298.21	640.00	0.0001
298.21	29790.00	0.0001
298.23	15130.00	0.0001
318.17	470.00	0.0001
318.17	14770.00	0.0001
318.17	30150.00	0.0001
338.16	440.00	0.0001
338.16	15150.00	0.0001
338.16	30360.00	0.0001
373.12	30010.00	0.0001
373.14	15170.00	0.0001
373.15	1960.00	0.0001
408.15	30070.00	0.0001
408.16	1760.00	0.0001
408.16	15000.00	0.0001
441.98	1950.00	0.0001
442.03	15670.00	0.0001
442.04	29810.00	0.0001
473.15	1900.00	0.0001
473.15	30250.00	0.0001
473.16	15750.00	0.0001
498.15	15970.00	0.0001
498.15	30110.00	0.0001
498.16	2930.00	0.0001
523.16	5030.00	0.0001
523.16	16160.00	0.0001
523.16	30260.00	0.0001
548.17	7030.00	0.0001
548.18	18020.00	0.0001
548.18	30300.00	0.0001
573.14	30090.00	0.0001
573.18	10040.00	0.0001
573.19	15080.00	0.0001
573.19	19910.00	0.0001
573.23	24730.00	0.0001

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,2-Ethanediol (1) - Liquid	Excess molar volume, m3/mol - Liquid
283.15	0.0099	-1.5900e-08
283.15	0.0126	-2.0000e-08
283.15	0.0262	-4.2000e-08
283.15	0.0464	-7.7700e-08
283.15	0.0752	-1.2900e-07
283.15	0.0951	-1.6630e-07
283.15	0.1016	-1.7600e-07
283.15	0.1245	-2.1300e-07
283.15	0.1491	-2.5030e-07
283.15	0.1731	-2.8120e-07
283.15	0.2000	-3.1290e-07
283.15	0.2004	-3.1110e-07
283.15	0.2083	-3.1960e-07
283.15	0.2203	-3.2900e-07
283.15	0.2501	-3.5420e-07
283.15	0.2903	-3.7940e-07
283.15	0.4076	-4.0060e-07
283.15	0.4641	-3.9100e-07
283.15	0.6066	-3.2850e-07
283.15	0.6959	-2.6820e-07
283.15	0.7788	-2.0170e-07
283.15	0.7988	-1.8520e-07
283.15	0.8040	-1.7970e-07
283.15	0.8463	-1.4250e-07
283.15	0.8864	-1.0630e-07
283.15	0.9308	-6.4200e-08
283.15	0.9395	-5.5000e-08
293.15	0.0099	-1.3400e-08
293.15	0.0126	-1.7200e-08
293.15	0.0262	-3.7300e-08
293.15	0.0464	-6.9500e-08
293.15	0.0752	-1.1510e-07
293.15	0.0951	-1.4850e-07
293.15	0.1016	-1.5710e-07
293.15	0.1245	-1.9010e-07
293.15	0.1491	-2.2360e-07
293.15	0.1731	-2.5160e-07
293.15	0.2000	-2.8050e-07
293.15	0.2004	-2.7880e-07
293.15	0.2083	-2.8660e-07
293.15	0.2203	-2.9520e-07
293.15	0.2501	-3.1860e-07
293.15	0.2903	-3.4230e-07
293.15	0.4076	-3.6390e-07
293.15	0.4641	-3.5600e-07
293.15	0.6066	-3.0070e-07
293.15	0.6959	-2.4600e-07
293.15	0.7788	-1.8530e-07
293.15	0.7988	-1.7030e-07
293.15	0.8040	-1.6510e-07
293.15	0.8463	-1.3090e-07
293.15	0.8864	-9.7800e-08
293.15	0.9308	-5.9000e-08
293.15	0.9395	-5.0300e-08
298.15	0.0099	-1.2300e-08
298.15	0.0126	-1.6000e-08
298.15	0.0262	-3.5400e-08
298.15	0.0464	-6.6300e-08
298.15	0.0752	-1.0970e-07
298.15	0.0951	-1.4150e-07
298.15	0.1016	-1.4960e-07
298.15	0.1245	-1.8100e-07
298.15	0.1491	-2.1290e-07
298.15	0.1731	-2.3960e-07
298.15	0.2000	-2.6740e-07
298.15	0.2004	-2.6560e-07
298.15	0.2083	-2.7310e-07
298.15	0.2203	-2.8130e-07
298.15	0.2501	-3.0380e-07
298.15	0.2903	-3.2690e-07
298.15	0.4076	-3.4840e-07
298.15	0.4641	-3.4120e-07
298.15	0.6066	-2.8870e-07
298.15	0.6959	-2.3640e-07
298.15	0.7788	-1.7820e-07
298.15	0.7988	-1.6380e-07
298.15	0.8040	-1.5870e-07
298.15	0.8463	-1.2600e-07
298.15	0.8864	-9.4000e-08
298.15	0.9308	-5.6800e-08
298.15	0.9395	-4.8300e-08
303.15	0.0099	-1.1300e-08
303.15	0.0126	-1.4900e-08
303.15	0.0262	-3.3800e-08
303.15	0.0464	-6.3500e-08
303.15	0.0752	-1.0510e-07
303.15	0.0951	-1.3540e-07
303.15	0.1016	-1.4310e-07
303.15	0.1245	-1.7300e-07
303.15	0.1491	-2.0350e-07
303.15	0.1731	-2.2900e-07
303.15	0.2000	-2.5550e-07
303.15	0.2004	-2.5380e-07
303.15	0.2083	-2.6110e-07
303.15	0.2203	-2.6900e-07
303.15	0.2501	-2.9070e-07
303.15	0.2903	-3.1300e-07
303.15	0.4076	-3.3440e-07
303.15	0.4641	-3.2770e-07
303.15	0.6066	-2.7790e-07
303.15	0.6959	-2.2780e-07
303.15	0.7788	-1.7170e-07
303.15	0.7988	-1.5790e-07
303.15	0.8040	-1.5300e-07
303.15	0.8463	-1.2140e-07
303.15	0.8864	-9.0600e-08
303.15	0.9308	-5.4600e-08
303.15	0.9395	-4.6600e-08
313.15	0.0099	-0.0000
313.15	0.0126	-1.2900e-08
313.15	0.0262	-3.0700e-08
313.15	0.0464	-5.8900e-08
313.15	0.0752	-9.7200e-08
313.15	0.0951	-1.2520e-07
313.15	0.1016	-1.3220e-07
313.15	0.1245	-1.5960e-07
313.15	0.1491	-1.8750e-07
313.15	0.1731	-2.1110e-07
313.15	0.2000	-2.3560e-07
313.15	0.2004	-2.3390e-07
313.15	0.2083	-2.4050e-07
313.15	0.2203	-2.4780e-07
313.15	0.2501	-2.6800e-07
313.15	0.2903	-2.8900e-07
313.15	0.4076	-3.0990e-07
313.15	0.4641	-3.0420e-07
313.15	0.6066	-2.5890e-07
313.15	0.6959	-2.1270e-07
313.15	0.7788	-1.6050e-07
313.15	0.7988	-1.4750e-07
313.15	0.8040	-1.4310e-07
313.15	0.8463	-1.1360e-07
313.15	0.8864	-8.4800e-08
313.15	0.9308	-5.1000e-08
313.15	0.9395	-4.3500e-08

Partial molar volume, m3/mol of 1,2-Ethanediol (1) [ref]

Operational condition: Mole fraction = 0 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Partial molar volume, m3/mol of 1,2-Ethanediol (1) - Liquid
298.21	640.00	0.0001
298.21	29790.00	0.0001
298.23	15130.00	0.0001
318.17	470.00	0.0001
318.17	14770.00	0.0001
318.17	30150.00	0.0001
338.16	440.00	0.0001
338.16	15150.00	0.0001
338.16	30360.00	0.0001
373.12	30010.00	0.0001
373.14	15170.00	0.0001
373.15	1960.00	0.0001
408.15	30070.00	0.0001
408.16	1760.00	0.0001
408.16	15000.00	0.0001
441.98	1950.00	0.0001
442.03	15670.00	0.0001
442.04	29810.00	0.0001
473.15	1900.00	0.0001
473.15	30250.00	0.0001
473.16	15750.00	0.0001
498.15	15970.00	0.0001
498.15	30110.00	0.0001
498.16	2930.00	0.0001
523.16	5030.00	0.0001
523.16	16160.00	0.0001
523.16	30260.00	0.0001
548.17	7030.00	0.0001
548.18	18020.00	0.0001
548.18	30300.00	0.0001
573.14	30090.00	0.0001
573.18	10040.00	0.0001
573.19	15080.00	0.0001
573.19	19910.00	0.0001
573.23	24730.00	0.0001

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