Mixture of 1,2-Ethanediol + Water

Excel

1,2-Ethanediol

Name
1,2-Ethanediol
InChI
InChI=1S/C2H6O2/c3-1-2-4/h3-4H,1-2H2
InChI Key
LYCAIKOWRPUZTN-UHFFFAOYSA-N
Formula
C2H6O2
SMILES
OCCO
Mol. Weight (g/mol)
62.07
CAS
107-21-1

Water

Name
Water
InChI
InChI=1S/H2O/h1H2
InChI Key
XLYOFNOQVPJJNP-UHFFFAOYSA-N
Formula
H2O
SMILES
O
Mol. Weight (g/mol)
18.02
CAS
7732-18-5
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Datasets

  1. Mole fraction (4)
  2. Cp,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. Pvap - Vapor or sublimation pressure, kPa (6)
  6. n0 - Refractive index (Na D-line) (2)
  7. ρl - Mass density, kg/m3 (28)
  8. csound,fluid - Speed of Sound, m/s (14)
  9. γ - Surface tension liquid-gas, N/m (8)
  10. Tboil - 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. vspec - 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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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:

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

Sources