Datasets
-
η - Viscosity, Pa*s (4)
-
Excess molar enthalpy (molar enthalpy (2)
-
n0 - Refractive index (Na D-line) (4)
-
ρl - Mass density, kg/m3 (4)
-
γ - Surface tension liquid-gas, N/m (2)
Viscosity, Pa*s
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 81.5 (Liquid)
Mole fraction of Benzyl alcohol (1) - Liquid |
Viscosity, Pa*s - Liquid |
0.0000 |
0.0011 |
0.0815 |
0.0013 |
0.1604 |
0.0015 |
0.2408 |
0.0018 |
0.3194 |
0.0020 |
0.3989 |
0.0023 |
0.4800 |
0.0027 |
0.5598 |
0.0030 |
0.6392 |
0.0034 |
0.7105 |
0.0038 |
0.7995 |
0.0043 |
0.8795 |
0.0047 |
0.9583 |
0.0052 |
1.0000 |
0.0054 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
100.8 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (2) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.0000 |
0.0063 |
293.15 |
0.0500 |
0.0059 |
293.15 |
0.1000 |
0.0055 |
293.15 |
0.1504 |
0.0052 |
293.15 |
0.1999 |
0.0049 |
293.15 |
0.2502 |
0.0046 |
293.15 |
0.3003 |
0.0042 |
293.15 |
0.3499 |
0.0039 |
293.15 |
0.3998 |
0.0037 |
293.15 |
0.4500 |
0.0034 |
293.15 |
0.5001 |
0.0031 |
293.15 |
0.5500 |
0.0029 |
293.15 |
0.5999 |
0.0026 |
293.15 |
0.6500 |
0.0024 |
293.15 |
0.6997 |
0.0022 |
293.15 |
0.7500 |
0.0020 |
293.15 |
0.7999 |
0.0018 |
293.15 |
0.8496 |
0.0016 |
293.15 |
0.8998 |
0.0015 |
293.15 |
0.9500 |
0.0013 |
293.15 |
1.0000 |
0.0012 |
303.15 |
0.0000 |
0.0046 |
303.15 |
0.0500 |
0.0043 |
303.15 |
0.1000 |
0.0040 |
303.15 |
0.1504 |
0.0038 |
303.15 |
0.1999 |
0.0035 |
303.15 |
0.2502 |
0.0033 |
303.15 |
0.3003 |
0.0031 |
303.15 |
0.3499 |
0.0029 |
303.15 |
0.3998 |
0.0027 |
303.15 |
0.4500 |
0.0025 |
303.15 |
0.5001 |
0.0024 |
303.15 |
0.5500 |
0.0022 |
303.15 |
0.5999 |
0.0020 |
303.15 |
0.6500 |
0.0019 |
303.15 |
0.6997 |
0.0017 |
303.15 |
0.7500 |
0.0016 |
303.15 |
0.7999 |
0.0014 |
303.15 |
0.8496 |
0.0013 |
303.15 |
0.8998 |
0.0012 |
303.15 |
0.9500 |
0.0011 |
303.15 |
1.0000 |
0.0010 |
313.15 |
0.0000 |
0.0033 |
313.15 |
0.0500 |
0.0032 |
313.15 |
0.1000 |
0.0030 |
313.15 |
0.1504 |
0.0028 |
313.15 |
0.1999 |
0.0027 |
313.15 |
0.2502 |
0.0025 |
313.15 |
0.3003 |
0.0024 |
313.15 |
0.3499 |
0.0022 |
313.15 |
0.3998 |
0.0021 |
313.15 |
0.4500 |
0.0020 |
313.15 |
0.5001 |
0.0018 |
313.15 |
0.5500 |
0.0017 |
313.15 |
0.5999 |
0.0016 |
313.15 |
0.6500 |
0.0014 |
313.15 |
0.6997 |
0.0013 |
313.15 |
0.7500 |
0.0012 |
313.15 |
0.7999 |
0.0011 |
313.15 |
0.8496 |
0.0010 |
313.15 |
0.8998 |
0.0010 |
313.15 |
0.9500 |
0.0009 |
313.15 |
1.0000 |
0.0008 |
323.15 |
0.0000 |
0.0025 |
323.15 |
0.0500 |
0.0024 |
323.15 |
0.1000 |
0.0023 |
323.15 |
0.1504 |
0.0022 |
323.15 |
0.1999 |
0.0021 |
323.15 |
0.2502 |
0.0020 |
323.15 |
0.3003 |
0.0019 |
323.15 |
0.3499 |
0.0018 |
323.15 |
0.3998 |
0.0017 |
323.15 |
0.4500 |
0.0016 |
323.15 |
0.5001 |
0.0016 |
323.15 |
0.5500 |
0.0015 |
323.15 |
0.5999 |
0.0014 |
323.15 |
0.6500 |
0.0013 |
323.15 |
0.6997 |
0.0012 |
323.15 |
0.7500 |
0.0011 |
323.15 |
0.7999 |
0.0010 |
323.15 |
0.8496 |
0.0009 |
323.15 |
0.8998 |
0.0009 |
323.15 |
0.9500 |
0.0008 |
323.15 |
1.0000 |
0.0007 |
Viscosity, Pa*s
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 81.5 (Liquid)
Mole fraction of Benzyl alcohol (1) - Liquid |
Viscosity, Pa*s - Liquid |
0.0000 |
0.0011 |
0.0815 |
0.0013 |
0.1604 |
0.0015 |
0.2408 |
0.0018 |
0.3194 |
0.0020 |
0.3989 |
0.0023 |
0.4800 |
0.0027 |
0.5598 |
0.0030 |
0.6392 |
0.0034 |
0.7105 |
0.0038 |
0.7995 |
0.0043 |
0.8795 |
0.0047 |
0.9583 |
0.0052 |
1.0000 |
0.0054 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
100.8 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (2) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.0000 |
0.0063 |
293.15 |
0.0500 |
0.0059 |
293.15 |
0.1000 |
0.0055 |
293.15 |
0.1504 |
0.0052 |
293.15 |
0.1999 |
0.0049 |
293.15 |
0.2502 |
0.0046 |
293.15 |
0.3003 |
0.0042 |
293.15 |
0.3499 |
0.0039 |
293.15 |
0.3998 |
0.0037 |
293.15 |
0.4500 |
0.0034 |
293.15 |
0.5001 |
0.0031 |
293.15 |
0.5500 |
0.0029 |
293.15 |
0.5999 |
0.0026 |
293.15 |
0.6500 |
0.0024 |
293.15 |
0.6997 |
0.0022 |
293.15 |
0.7500 |
0.0020 |
293.15 |
0.7999 |
0.0018 |
293.15 |
0.8496 |
0.0016 |
293.15 |
0.8998 |
0.0015 |
293.15 |
0.9500 |
0.0013 |
293.15 |
1.0000 |
0.0012 |
303.15 |
0.0000 |
0.0046 |
303.15 |
0.0500 |
0.0043 |
303.15 |
0.1000 |
0.0040 |
303.15 |
0.1504 |
0.0038 |
303.15 |
0.1999 |
0.0035 |
303.15 |
0.2502 |
0.0033 |
303.15 |
0.3003 |
0.0031 |
303.15 |
0.3499 |
0.0029 |
303.15 |
0.3998 |
0.0027 |
303.15 |
0.4500 |
0.0025 |
303.15 |
0.5001 |
0.0024 |
303.15 |
0.5500 |
0.0022 |
303.15 |
0.5999 |
0.0020 |
303.15 |
0.6500 |
0.0019 |
303.15 |
0.6997 |
0.0017 |
303.15 |
0.7500 |
0.0016 |
303.15 |
0.7999 |
0.0014 |
303.15 |
0.8496 |
0.0013 |
303.15 |
0.8998 |
0.0012 |
303.15 |
0.9500 |
0.0011 |
303.15 |
1.0000 |
0.0010 |
313.15 |
0.0000 |
0.0033 |
313.15 |
0.0500 |
0.0032 |
313.15 |
0.1000 |
0.0030 |
313.15 |
0.1504 |
0.0028 |
313.15 |
0.1999 |
0.0027 |
313.15 |
0.2502 |
0.0025 |
313.15 |
0.3003 |
0.0024 |
313.15 |
0.3499 |
0.0022 |
313.15 |
0.3998 |
0.0021 |
313.15 |
0.4500 |
0.0020 |
313.15 |
0.5001 |
0.0018 |
313.15 |
0.5500 |
0.0017 |
313.15 |
0.5999 |
0.0016 |
313.15 |
0.6500 |
0.0014 |
313.15 |
0.6997 |
0.0013 |
313.15 |
0.7500 |
0.0012 |
313.15 |
0.7999 |
0.0011 |
313.15 |
0.8496 |
0.0010 |
313.15 |
0.8998 |
0.0010 |
313.15 |
0.9500 |
0.0009 |
313.15 |
1.0000 |
0.0008 |
323.15 |
0.0000 |
0.0025 |
323.15 |
0.0500 |
0.0024 |
323.15 |
0.1000 |
0.0023 |
323.15 |
0.1504 |
0.0022 |
323.15 |
0.1999 |
0.0021 |
323.15 |
0.2502 |
0.0020 |
323.15 |
0.3003 |
0.0019 |
323.15 |
0.3499 |
0.0018 |
323.15 |
0.3998 |
0.0017 |
323.15 |
0.4500 |
0.0016 |
323.15 |
0.5001 |
0.0016 |
323.15 |
0.5500 |
0.0015 |
323.15 |
0.5999 |
0.0014 |
323.15 |
0.6500 |
0.0013 |
323.15 |
0.6997 |
0.0012 |
323.15 |
0.7500 |
0.0011 |
323.15 |
0.7999 |
0.0010 |
323.15 |
0.8496 |
0.0009 |
323.15 |
0.8998 |
0.0009 |
323.15 |
0.9500 |
0.0008 |
323.15 |
1.0000 |
0.0007 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Benzyl alcohol (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0746 |
0.0734 |
0.1514 |
0.1306 |
0.2275 |
0.1714 |
0.3029 |
0.1984 |
0.3785 |
0.2144 |
0.4855 |
0.2232 |
0.5857 |
0.2079 |
0.6883 |
0.1767 |
0.7915 |
0.1293 |
0.8949 |
0.0717 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Mole fraction of Benzyl alcohol (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0746 |
0.0734 |
0.1514 |
0.1306 |
0.2275 |
0.1714 |
0.3029 |
0.1984 |
0.3785 |
0.2144 |
0.4855 |
0.2232 |
0.5857 |
0.2079 |
0.6883 |
0.1767 |
0.7915 |
0.1293 |
0.8949 |
0.0717 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 81.5 (Liquid)
Mole fraction of Benzyl alcohol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
0.0000 |
1.3594 |
0.0815 |
1.3852 |
0.1604 |
1.4073 |
0.2408 |
1.4272 |
0.3194 |
1.4457 |
0.3989 |
1.4616 |
0.4800 |
1.476 |
0.5598 |
1.489 |
0.6392 |
1.5 |
0.7105 |
1.5083 |
0.7995 |
1.5182 |
0.8795 |
1.5266 |
0.9583 |
1.5344 |
1.0000 |
1.5381 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
100.8 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (2) - Liquid |
Refractive index (Na D-line) - Liquid |
293.15 |
0.0000 |
1.5405 |
293.15 |
0.0500 |
1.5361 |
293.15 |
0.1000 |
1.5312 |
293.15 |
0.1504 |
1.5258 |
293.15 |
0.1999 |
1.5204 |
293.15 |
0.2502 |
1.5144 |
293.15 |
0.3003 |
1.508 |
293.15 |
0.3499 |
1.5015 |
293.15 |
0.3998 |
1.4945 |
293.15 |
0.4500 |
1.4871 |
293.15 |
0.5001 |
1.4791 |
293.15 |
0.5500 |
1.4707 |
293.15 |
0.5999 |
1.4618 |
293.15 |
0.6500 |
1.4522 |
293.15 |
0.6997 |
1.442 |
293.15 |
0.7500 |
1.4309 |
293.15 |
0.7999 |
1.4192 |
293.15 |
0.8496 |
1.4066 |
293.15 |
0.8998 |
1.3927 |
293.15 |
0.9500 |
1.3778 |
293.15 |
1.0000 |
1.3614 |
303.15 |
0.0000 |
1.5364 |
303.15 |
0.0500 |
1.5317 |
303.15 |
0.1000 |
1.5268 |
303.15 |
0.1504 |
1.5215 |
303.15 |
0.1999 |
1.5159 |
303.15 |
0.2502 |
1.51 |
303.15 |
0.3003 |
1.5037 |
303.15 |
0.3499 |
1.4972 |
303.15 |
0.3998 |
1.4901 |
303.15 |
0.4500 |
1.4826 |
303.15 |
0.5001 |
1.4747 |
303.15 |
0.5500 |
1.4663 |
303.15 |
0.5999 |
1.4573 |
303.15 |
0.6500 |
1.4477 |
303.15 |
0.6997 |
1.4375 |
303.15 |
0.7500 |
1.4265 |
303.15 |
0.7999 |
1.4148 |
303.15 |
0.8496 |
1.402 |
303.15 |
0.8998 |
1.3882 |
303.15 |
0.9500 |
1.3733 |
303.15 |
1.0000 |
1.3571 |
313.15 |
0.0000 |
1.5321 |
313.15 |
0.0500 |
1.5274 |
313.15 |
0.1000 |
1.5225 |
313.15 |
0.1504 |
1.5172 |
313.15 |
0.1999 |
1.5116 |
313.15 |
0.2502 |
1.5056 |
313.15 |
0.3003 |
1.4993 |
313.15 |
0.3499 |
1.4927 |
313.15 |
0.3998 |
1.4857 |
313.15 |
0.4500 |
1.4782 |
313.15 |
0.5001 |
1.4703 |
313.15 |
0.5500 |
1.4619 |
313.15 |
0.5999 |
1.453 |
313.15 |
0.6500 |
1.4433 |
313.15 |
0.6997 |
1.4331 |
313.15 |
0.7500 |
1.4221 |
313.15 |
0.7999 |
1.4104 |
313.15 |
0.8496 |
1.3976 |
313.15 |
0.8998 |
1.3839 |
313.15 |
0.9500 |
1.3691 |
313.15 |
1.0000 |
1.3529 |
323.15 |
0.0000 |
1.528 |
323.15 |
0.0500 |
1.5231 |
323.15 |
0.1000 |
1.5181 |
323.15 |
0.1504 |
1.5127 |
323.15 |
0.1999 |
1.5072 |
323.15 |
0.2502 |
1.5012 |
323.15 |
0.3003 |
1.4949 |
323.15 |
0.3499 |
1.4883 |
323.15 |
0.3998 |
1.4813 |
323.15 |
0.4500 |
1.4738 |
323.15 |
0.5001 |
1.4659 |
323.15 |
0.5500 |
1.4575 |
323.15 |
0.5999 |
1.4486 |
323.15 |
0.6500 |
1.4389 |
323.15 |
0.6997 |
1.4287 |
323.15 |
0.7500 |
1.4178 |
323.15 |
0.7999 |
1.4061 |
323.15 |
0.8496 |
1.3933 |
323.15 |
0.8998 |
1.3796 |
323.15 |
0.9500 |
1.3647 |
323.15 |
1.0000 |
1.3487 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 81.5 (Liquid)
Mole fraction of Benzyl alcohol (1) - Liquid |
Refractive index (Na D-line) - Liquid |
0.0000 |
1.3594 |
0.0815 |
1.3852 |
0.1604 |
1.4073 |
0.2408 |
1.4272 |
0.3194 |
1.4457 |
0.3989 |
1.4616 |
0.4800 |
1.476 |
0.5598 |
1.489 |
0.6392 |
1.5 |
0.7105 |
1.5083 |
0.7995 |
1.5182 |
0.8795 |
1.5266 |
0.9583 |
1.5344 |
1.0000 |
1.5381 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
100.8 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (2) - Liquid |
Refractive index (Na D-line) - Liquid |
293.15 |
0.0000 |
1.5405 |
293.15 |
0.0500 |
1.5361 |
293.15 |
0.1000 |
1.5312 |
293.15 |
0.1504 |
1.5258 |
293.15 |
0.1999 |
1.5204 |
293.15 |
0.2502 |
1.5144 |
293.15 |
0.3003 |
1.508 |
293.15 |
0.3499 |
1.5015 |
293.15 |
0.3998 |
1.4945 |
293.15 |
0.4500 |
1.4871 |
293.15 |
0.5001 |
1.4791 |
293.15 |
0.5500 |
1.4707 |
293.15 |
0.5999 |
1.4618 |
293.15 |
0.6500 |
1.4522 |
293.15 |
0.6997 |
1.442 |
293.15 |
0.7500 |
1.4309 |
293.15 |
0.7999 |
1.4192 |
293.15 |
0.8496 |
1.4066 |
293.15 |
0.8998 |
1.3927 |
293.15 |
0.9500 |
1.3778 |
293.15 |
1.0000 |
1.3614 |
303.15 |
0.0000 |
1.5364 |
303.15 |
0.0500 |
1.5317 |
303.15 |
0.1000 |
1.5268 |
303.15 |
0.1504 |
1.5215 |
303.15 |
0.1999 |
1.5159 |
303.15 |
0.2502 |
1.51 |
303.15 |
0.3003 |
1.5037 |
303.15 |
0.3499 |
1.4972 |
303.15 |
0.3998 |
1.4901 |
303.15 |
0.4500 |
1.4826 |
303.15 |
0.5001 |
1.4747 |
303.15 |
0.5500 |
1.4663 |
303.15 |
0.5999 |
1.4573 |
303.15 |
0.6500 |
1.4477 |
303.15 |
0.6997 |
1.4375 |
303.15 |
0.7500 |
1.4265 |
303.15 |
0.7999 |
1.4148 |
303.15 |
0.8496 |
1.402 |
303.15 |
0.8998 |
1.3882 |
303.15 |
0.9500 |
1.3733 |
303.15 |
1.0000 |
1.3571 |
313.15 |
0.0000 |
1.5321 |
313.15 |
0.0500 |
1.5274 |
313.15 |
0.1000 |
1.5225 |
313.15 |
0.1504 |
1.5172 |
313.15 |
0.1999 |
1.5116 |
313.15 |
0.2502 |
1.5056 |
313.15 |
0.3003 |
1.4993 |
313.15 |
0.3499 |
1.4927 |
313.15 |
0.3998 |
1.4857 |
313.15 |
0.4500 |
1.4782 |
313.15 |
0.5001 |
1.4703 |
313.15 |
0.5500 |
1.4619 |
313.15 |
0.5999 |
1.453 |
313.15 |
0.6500 |
1.4433 |
313.15 |
0.6997 |
1.4331 |
313.15 |
0.7500 |
1.4221 |
313.15 |
0.7999 |
1.4104 |
313.15 |
0.8496 |
1.3976 |
313.15 |
0.8998 |
1.3839 |
313.15 |
0.9500 |
1.3691 |
313.15 |
1.0000 |
1.3529 |
323.15 |
0.0000 |
1.528 |
323.15 |
0.0500 |
1.5231 |
323.15 |
0.1000 |
1.5181 |
323.15 |
0.1504 |
1.5127 |
323.15 |
0.1999 |
1.5072 |
323.15 |
0.2502 |
1.5012 |
323.15 |
0.3003 |
1.4949 |
323.15 |
0.3499 |
1.4883 |
323.15 |
0.3998 |
1.4813 |
323.15 |
0.4500 |
1.4738 |
323.15 |
0.5001 |
1.4659 |
323.15 |
0.5500 |
1.4575 |
323.15 |
0.5999 |
1.4486 |
323.15 |
0.6500 |
1.4389 |
323.15 |
0.6997 |
1.4287 |
323.15 |
0.7500 |
1.4178 |
323.15 |
0.7999 |
1.4061 |
323.15 |
0.8496 |
1.3933 |
323.15 |
0.8998 |
1.3796 |
323.15 |
0.9500 |
1.3647 |
323.15 |
1.0000 |
1.3487 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 81.5 (Liquid)
Mole fraction of Benzyl alcohol (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
785.12 |
0.0807 |
823.11 |
0.1619 |
855.6 |
0.2423 |
884.57 |
0.3212 |
909.77 |
0.3998 |
931.73 |
0.4808 |
951.84 |
0.5542 |
968.38 |
0.6358 |
984.93 |
0.7217 |
1000.67 |
0.7985 |
1013.39 |
0.8782 |
1025.49 |
0.9540 |
1036.86 |
1.0000 |
1042.1 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100.8 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (2) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.0000 |
1045.44 |
293.15 |
0.0500 |
1038.93 |
293.15 |
0.1000 |
1032.01 |
293.15 |
0.1504 |
1024.72 |
293.15 |
0.1999 |
1017.09 |
293.15 |
0.2502 |
1008.95 |
293.15 |
0.3003 |
1000.31 |
293.15 |
0.3499 |
991.24 |
293.15 |
0.3998 |
981.52 |
293.15 |
0.4500 |
971.12 |
293.15 |
0.5001 |
960.01 |
293.15 |
0.5500 |
948.23 |
293.15 |
0.5999 |
935.57 |
293.15 |
0.6500 |
921.93 |
293.15 |
0.6997 |
907.34 |
293.15 |
0.7500 |
891.49 |
293.15 |
0.7999 |
874.42 |
293.15 |
0.8496 |
855.94 |
293.15 |
0.8998 |
835.44 |
293.15 |
0.9500 |
813.26 |
293.15 |
1.0000 |
789.1 |
303.15 |
0.0000 |
1037.45 |
303.15 |
0.0500 |
1030.91 |
303.15 |
0.1000 |
1024.02 |
303.15 |
0.1504 |
1016.76 |
303.15 |
0.1999 |
1009.06 |
303.15 |
0.2502 |
1000.9 |
303.15 |
0.3003 |
992.29 |
303.15 |
0.3499 |
983.16 |
303.15 |
0.3998 |
973.34 |
303.15 |
0.4500 |
962.91 |
303.15 |
0.5001 |
951.76 |
303.15 |
0.5500 |
939.95 |
303.15 |
0.5999 |
927.33 |
303.15 |
0.6500 |
913.64 |
303.15 |
0.6997 |
898.99 |
303.15 |
0.7500 |
883.14 |
303.15 |
0.7999 |
865.99 |
303.15 |
0.8496 |
847.51 |
303.15 |
0.8998 |
827.13 |
303.15 |
0.9500 |
805.04 |
303.15 |
1.0000 |
780.76 |
313.15 |
0.0000 |
1029.61 |
313.15 |
0.0500 |
1023.04 |
313.15 |
0.1000 |
1016.21 |
313.15 |
0.1504 |
1008.86 |
313.15 |
0.1999 |
1001.16 |
313.15 |
0.2502 |
992.96 |
313.15 |
0.3003 |
984.28 |
313.15 |
0.3499 |
975.05 |
313.15 |
0.3998 |
965.24 |
313.15 |
0.4500 |
954.84 |
313.15 |
0.5001 |
943.67 |
313.15 |
0.5500 |
931.78 |
313.15 |
0.5999 |
919.04 |
313.15 |
0.6500 |
905.41 |
313.15 |
0.6997 |
890.69 |
313.15 |
0.7500 |
874.75 |
313.15 |
0.7999 |
857.51 |
313.15 |
0.8496 |
838.83 |
313.15 |
0.8998 |
818.48 |
313.15 |
0.9500 |
796.32 |
313.15 |
1.0000 |
771.99 |
323.15 |
0.0000 |
1021.5 |
323.15 |
0.0500 |
1014.86 |
323.15 |
0.1000 |
1007.98 |
323.15 |
0.1504 |
1000.57 |
323.15 |
0.1999 |
992.89 |
323.15 |
0.2502 |
984.67 |
323.15 |
0.3003 |
975.99 |
323.15 |
0.3499 |
966.71 |
323.15 |
0.3998 |
956.84 |
323.15 |
0.4500 |
946.37 |
323.15 |
0.5001 |
935.23 |
323.15 |
0.5500 |
923.28 |
323.15 |
0.5999 |
910.48 |
323.15 |
0.6500 |
896.61 |
323.15 |
0.6997 |
881.89 |
323.15 |
0.7500 |
865.88 |
323.15 |
0.7999 |
848.64 |
323.15 |
0.8496 |
830.07 |
323.15 |
0.8998 |
809.62 |
323.15 |
0.9500 |
787.41 |
323.15 |
1.0000 |
763.03 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 81.5 (Liquid)
Mole fraction of Benzyl alcohol (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
785.12 |
0.0807 |
823.11 |
0.1619 |
855.6 |
0.2423 |
884.57 |
0.3212 |
909.77 |
0.3998 |
931.73 |
0.4808 |
951.84 |
0.5542 |
968.38 |
0.6358 |
984.93 |
0.7217 |
1000.67 |
0.7985 |
1013.39 |
0.8782 |
1025.49 |
0.9540 |
1036.86 |
1.0000 |
1042.1 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100.8 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (2) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.0000 |
1045.44 |
293.15 |
0.0500 |
1038.93 |
293.15 |
0.1000 |
1032.01 |
293.15 |
0.1504 |
1024.72 |
293.15 |
0.1999 |
1017.09 |
293.15 |
0.2502 |
1008.95 |
293.15 |
0.3003 |
1000.31 |
293.15 |
0.3499 |
991.24 |
293.15 |
0.3998 |
981.52 |
293.15 |
0.4500 |
971.12 |
293.15 |
0.5001 |
960.01 |
293.15 |
0.5500 |
948.23 |
293.15 |
0.5999 |
935.57 |
293.15 |
0.6500 |
921.93 |
293.15 |
0.6997 |
907.34 |
293.15 |
0.7500 |
891.49 |
293.15 |
0.7999 |
874.42 |
293.15 |
0.8496 |
855.94 |
293.15 |
0.8998 |
835.44 |
293.15 |
0.9500 |
813.26 |
293.15 |
1.0000 |
789.1 |
303.15 |
0.0000 |
1037.45 |
303.15 |
0.0500 |
1030.91 |
303.15 |
0.1000 |
1024.02 |
303.15 |
0.1504 |
1016.76 |
303.15 |
0.1999 |
1009.06 |
303.15 |
0.2502 |
1000.9 |
303.15 |
0.3003 |
992.29 |
303.15 |
0.3499 |
983.16 |
303.15 |
0.3998 |
973.34 |
303.15 |
0.4500 |
962.91 |
303.15 |
0.5001 |
951.76 |
303.15 |
0.5500 |
939.95 |
303.15 |
0.5999 |
927.33 |
303.15 |
0.6500 |
913.64 |
303.15 |
0.6997 |
898.99 |
303.15 |
0.7500 |
883.14 |
303.15 |
0.7999 |
865.99 |
303.15 |
0.8496 |
847.51 |
303.15 |
0.8998 |
827.13 |
303.15 |
0.9500 |
805.04 |
303.15 |
1.0000 |
780.76 |
313.15 |
0.0000 |
1029.61 |
313.15 |
0.0500 |
1023.04 |
313.15 |
0.1000 |
1016.21 |
313.15 |
0.1504 |
1008.86 |
313.15 |
0.1999 |
1001.16 |
313.15 |
0.2502 |
992.96 |
313.15 |
0.3003 |
984.28 |
313.15 |
0.3499 |
975.05 |
313.15 |
0.3998 |
965.24 |
313.15 |
0.4500 |
954.84 |
313.15 |
0.5001 |
943.67 |
313.15 |
0.5500 |
931.78 |
313.15 |
0.5999 |
919.04 |
313.15 |
0.6500 |
905.41 |
313.15 |
0.6997 |
890.69 |
313.15 |
0.7500 |
874.75 |
313.15 |
0.7999 |
857.51 |
313.15 |
0.8496 |
838.83 |
313.15 |
0.8998 |
818.48 |
313.15 |
0.9500 |
796.32 |
313.15 |
1.0000 |
771.99 |
323.15 |
0.0000 |
1021.5 |
323.15 |
0.0500 |
1014.86 |
323.15 |
0.1000 |
1007.98 |
323.15 |
0.1504 |
1000.57 |
323.15 |
0.1999 |
992.89 |
323.15 |
0.2502 |
984.67 |
323.15 |
0.3003 |
975.99 |
323.15 |
0.3499 |
966.71 |
323.15 |
0.3998 |
956.84 |
323.15 |
0.4500 |
946.37 |
323.15 |
0.5001 |
935.23 |
323.15 |
0.5500 |
923.28 |
323.15 |
0.5999 |
910.48 |
323.15 |
0.6500 |
896.61 |
323.15 |
0.6997 |
881.89 |
323.15 |
0.7500 |
865.88 |
323.15 |
0.7999 |
848.64 |
323.15 |
0.8496 |
830.07 |
323.15 |
0.8998 |
809.62 |
323.15 |
0.9500 |
787.41 |
323.15 |
1.0000 |
763.03 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
293.15 |
0.0000 |
0.0392 |
293.15 |
0.0500 |
0.0387 |
293.15 |
0.1000 |
0.0381 |
293.15 |
0.1504 |
0.0375 |
293.15 |
0.1999 |
0.0368 |
293.15 |
0.2502 |
0.0361 |
293.15 |
0.3003 |
0.0353 |
293.15 |
0.3499 |
0.0345 |
293.15 |
0.3998 |
0.0336 |
293.15 |
0.4500 |
0.0327 |
293.15 |
0.5001 |
0.0318 |
293.15 |
0.5500 |
0.0309 |
293.15 |
0.5999 |
0.0299 |
293.15 |
0.6500 |
0.0289 |
293.15 |
0.6997 |
0.0280 |
293.15 |
0.7500 |
0.0271 |
293.15 |
0.7999 |
0.0261 |
293.15 |
0.8496 |
0.0252 |
293.15 |
0.8998 |
0.0243 |
293.15 |
0.9500 |
0.0233 |
293.15 |
1.0000 |
0.0223 |
303.15 |
0.0000 |
0.0381 |
303.15 |
0.0500 |
0.0375 |
303.15 |
0.1000 |
0.0369 |
303.15 |
0.1504 |
0.0362 |
303.15 |
0.1999 |
0.0355 |
303.15 |
0.2502 |
0.0348 |
303.15 |
0.3003 |
0.0341 |
303.15 |
0.3499 |
0.0333 |
303.15 |
0.3998 |
0.0325 |
303.15 |
0.4500 |
0.0316 |
303.15 |
0.5001 |
0.0307 |
303.15 |
0.5500 |
0.0298 |
303.15 |
0.5999 |
0.0288 |
303.15 |
0.6500 |
0.0278 |
303.15 |
0.6997 |
0.0269 |
303.15 |
0.7500 |
0.0260 |
303.15 |
0.7999 |
0.0251 |
303.15 |
0.8496 |
0.0242 |
303.15 |
0.8998 |
0.0233 |
303.15 |
0.9500 |
0.0223 |
303.15 |
1.0000 |
0.0214 |
313.15 |
0.0000 |
0.0372 |
313.15 |
0.0500 |
0.0366 |
313.15 |
0.1000 |
0.0359 |
313.15 |
0.1504 |
0.0353 |
313.15 |
0.1999 |
0.0346 |
313.15 |
0.2502 |
0.0339 |
313.15 |
0.3003 |
0.0332 |
313.15 |
0.3499 |
0.0324 |
313.15 |
0.3998 |
0.0316 |
313.15 |
0.4500 |
0.0307 |
313.15 |
0.5001 |
0.0298 |
313.15 |
0.5500 |
0.0289 |
313.15 |
0.5999 |
0.0279 |
313.15 |
0.6500 |
0.0269 |
313.15 |
0.6997 |
0.0260 |
313.15 |
0.7500 |
0.0251 |
313.15 |
0.7999 |
0.0242 |
313.15 |
0.8496 |
0.0233 |
313.15 |
0.8998 |
0.0224 |
313.15 |
0.9500 |
0.0215 |
313.15 |
1.0000 |
0.0206 |
323.15 |
0.0000 |
0.0363 |
323.15 |
0.0500 |
0.0356 |
323.15 |
0.1000 |
0.0349 |
323.15 |
0.1504 |
0.0342 |
323.15 |
0.1999 |
0.0335 |
323.15 |
0.2502 |
0.0328 |
323.15 |
0.3003 |
0.0321 |
323.15 |
0.3499 |
0.0313 |
323.15 |
0.3998 |
0.0305 |
323.15 |
0.4500 |
0.0296 |
323.15 |
0.5001 |
0.0287 |
323.15 |
0.5500 |
0.0278 |
323.15 |
0.5999 |
0.0268 |
323.15 |
0.6500 |
0.0258 |
323.15 |
0.6997 |
0.0248 |
323.15 |
0.7500 |
0.0239 |
323.15 |
0.7999 |
0.0230 |
323.15 |
0.8496 |
0.0221 |
323.15 |
0.8998 |
0.0212 |
323.15 |
0.9500 |
0.0203 |
323.15 |
1.0000 |
0.0194 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Ethanol (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
293.15 |
0.0000 |
0.0392 |
293.15 |
0.0500 |
0.0387 |
293.15 |
0.1000 |
0.0381 |
293.15 |
0.1504 |
0.0375 |
293.15 |
0.1999 |
0.0368 |
293.15 |
0.2502 |
0.0361 |
293.15 |
0.3003 |
0.0353 |
293.15 |
0.3499 |
0.0345 |
293.15 |
0.3998 |
0.0336 |
293.15 |
0.4500 |
0.0327 |
293.15 |
0.5001 |
0.0318 |
293.15 |
0.5500 |
0.0309 |
293.15 |
0.5999 |
0.0299 |
293.15 |
0.6500 |
0.0289 |
293.15 |
0.6997 |
0.0280 |
293.15 |
0.7500 |
0.0271 |
293.15 |
0.7999 |
0.0261 |
293.15 |
0.8496 |
0.0252 |
293.15 |
0.8998 |
0.0243 |
293.15 |
0.9500 |
0.0233 |
293.15 |
1.0000 |
0.0223 |
303.15 |
0.0000 |
0.0381 |
303.15 |
0.0500 |
0.0375 |
303.15 |
0.1000 |
0.0369 |
303.15 |
0.1504 |
0.0362 |
303.15 |
0.1999 |
0.0355 |
303.15 |
0.2502 |
0.0348 |
303.15 |
0.3003 |
0.0341 |
303.15 |
0.3499 |
0.0333 |
303.15 |
0.3998 |
0.0325 |
303.15 |
0.4500 |
0.0316 |
303.15 |
0.5001 |
0.0307 |
303.15 |
0.5500 |
0.0298 |
303.15 |
0.5999 |
0.0288 |
303.15 |
0.6500 |
0.0278 |
303.15 |
0.6997 |
0.0269 |
303.15 |
0.7500 |
0.0260 |
303.15 |
0.7999 |
0.0251 |
303.15 |
0.8496 |
0.0242 |
303.15 |
0.8998 |
0.0233 |
303.15 |
0.9500 |
0.0223 |
303.15 |
1.0000 |
0.0214 |
313.15 |
0.0000 |
0.0372 |
313.15 |
0.0500 |
0.0366 |
313.15 |
0.1000 |
0.0359 |
313.15 |
0.1504 |
0.0353 |
313.15 |
0.1999 |
0.0346 |
313.15 |
0.2502 |
0.0339 |
313.15 |
0.3003 |
0.0332 |
313.15 |
0.3499 |
0.0324 |
313.15 |
0.3998 |
0.0316 |
313.15 |
0.4500 |
0.0307 |
313.15 |
0.5001 |
0.0298 |
313.15 |
0.5500 |
0.0289 |
313.15 |
0.5999 |
0.0279 |
313.15 |
0.6500 |
0.0269 |
313.15 |
0.6997 |
0.0260 |
313.15 |
0.7500 |
0.0251 |
313.15 |
0.7999 |
0.0242 |
313.15 |
0.8496 |
0.0233 |
313.15 |
0.8998 |
0.0224 |
313.15 |
0.9500 |
0.0215 |
313.15 |
1.0000 |
0.0206 |
323.15 |
0.0000 |
0.0363 |
323.15 |
0.0500 |
0.0356 |
323.15 |
0.1000 |
0.0349 |
323.15 |
0.1504 |
0.0342 |
323.15 |
0.1999 |
0.0335 |
323.15 |
0.2502 |
0.0328 |
323.15 |
0.3003 |
0.0321 |
323.15 |
0.3499 |
0.0313 |
323.15 |
0.3998 |
0.0305 |
323.15 |
0.4500 |
0.0296 |
323.15 |
0.5001 |
0.0287 |
323.15 |
0.5500 |
0.0278 |
323.15 |
0.5999 |
0.0268 |
323.15 |
0.6500 |
0.0258 |
323.15 |
0.6997 |
0.0248 |
323.15 |
0.7500 |
0.0239 |
323.15 |
0.7999 |
0.0230 |
323.15 |
0.8496 |
0.0221 |
323.15 |
0.8998 |
0.0212 |
323.15 |
0.9500 |
0.0203 |
323.15 |
1.0000 |
0.0194 |
Sources