Operational conditions:
| Mole fraction of Ethanol (2) - Liquid | Viscosity, Pa*s - Liquid |
|---|---|
| 0.0738 | 0.0250 |
| 0.1285 | 0.0205 |
| 0.2099 | 0.0152 |
| 0.2725 | 0.0121 |
| 0.3701 | 0.0086 |
| 0.4389 | 0.0067 |
| 0.5193 | 0.0050 |
| 0.5871 | 0.0040 |
| 0.6780 | 0.0029 |
| 0.7554 | 0.0022 |
| 0.8185 | 0.0018 |
| 0.9171 | 0.0013 |
Operational conditions:
| Mole fraction of Ethanol (2) - Liquid | Viscosity, Pa*s - Liquid |
|---|---|
| 0.0738 | 0.0250 |
| 0.1285 | 0.0205 |
| 0.2099 | 0.0152 |
| 0.2725 | 0.0121 |
| 0.3701 | 0.0086 |
| 0.4389 | 0.0067 |
| 0.5193 | 0.0050 |
| 0.5871 | 0.0040 |
| 0.6780 | 0.0029 |
| 0.7554 | 0.0022 |
| 0.8185 | 0.0018 |
| 0.9171 | 0.0013 |
Operational conditions:
| Mole fraction of Propylene Glycol (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0997 | 0.0899 |
| 0.1948 | 0.1436 |
| 0.2875 | 0.1757 |
| 0.3810 | 0.1897 |
| 0.4756 | 0.1886 |
| 0.4952 | 0.1985 |
| 0.5972 | 0.1787 |
| 0.6991 | 0.1476 |
| 0.8005 | 0.1059 |
| 0.9004 | 0.0569 |
Operational conditions:
| Mole fraction of Propylene Glycol (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0997 | 0.0899 |
| 0.1948 | 0.1436 |
| 0.2875 | 0.1757 |
| 0.3810 | 0.1897 |
| 0.4756 | 0.1886 |
| 0.4952 | 0.1985 |
| 0.5972 | 0.1787 |
| 0.6991 | 0.1476 |
| 0.8005 | 0.1059 |
| 0.9004 | 0.0569 |
Operational conditions:
| Mole fraction of Ethanol (2) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.0738 | 1.426 |
| 0.1285 | 1.4233 |
| 0.2099 | 1.4187 |
| 0.2725 | 1.4153 |
| 0.3701 | 1.4093 |
| 0.4389 | 1.4052 |
| 0.5193 | 1.3998 |
| 0.5871 | 1.3946 |
| 0.6780 | 1.3876 |
| 0.7554 | 1.3817 |
| 0.8185 | 1.3765 |
| 0.9171 | 1.3672 |
Operational conditions:
| Mole fraction of Ethanol (2) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.0738 | 1.426 |
| 0.1285 | 1.4233 |
| 0.2099 | 1.4187 |
| 0.2725 | 1.4153 |
| 0.3701 | 1.4093 |
| 0.4389 | 1.4052 |
| 0.5193 | 1.3998 |
| 0.5871 | 1.3946 |
| 0.6780 | 1.3876 |
| 0.7554 | 1.3817 |
| 0.8185 | 1.3765 |
| 0.9171 | 1.3672 |
Operational condition: Pressure, kPa = 81.5 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol (2) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0492 | 1023.64 |
| 298.15 | 0.1220 | 1009.9 |
| 298.15 | 0.2072 | 993.05 |
| 298.15 | 0.2706 | 979.89 |
| 298.15 | 0.3633 | 959.86 |
| 298.15 | 0.4478 | 940.7 |
| 298.15 | 0.5261 | 921.85 |
| 298.15 | 0.6103 | 900.63 |
| 298.15 | 0.6770 | 882.99 |
| 298.15 | 0.7613 | 859.54 |
| 298.15 | 0.8332 | 838.49 |
| 298.15 | 0.9232 | 810.57 |
| 298.15 | 1.0000 | 785.18 |
| 303.15 | 0.0492 | 1019.91 |
| 303.15 | 0.1220 | 1006.14 |
| 303.15 | 0.2072 | 989.22 |
| 303.15 | 0.2706 | 976.03 |
| 303.15 | 0.3633 | 955.92 |
| 303.15 | 0.4478 | 936.73 |
| 303.15 | 0.5261 | 917.81 |
| 303.15 | 0.6103 | 896.55 |
| 303.15 | 0.6770 | 878.84 |
| 303.15 | 0.7613 | 855.37 |
| 303.15 | 0.8332 | 834.25 |
| 303.15 | 0.9232 | 806.3 |
| 303.15 | 1.0000 | 780.87 |
| 308.15 | 0.0492 | 1016.16 |
| 308.15 | 0.1220 | 1002.31 |
| 308.15 | 0.2072 | 985.36 |
| 308.15 | 0.2706 | 972.12 |
| 308.15 | 0.3633 | 951.97 |
| 308.15 | 0.4478 | 932.7 |
| 308.15 | 0.5261 | 913.76 |
| 308.15 | 0.6103 | 892.41 |
| 308.15 | 0.6770 | 874.69 |
| 308.15 | 0.7613 | 851.13 |
| 308.15 | 0.8332 | 829.99 |
| 308.15 | 0.9232 | 801.98 |
| 308.15 | 1.0000 | 776.52 |
Operational condition: Pressure, kPa = 81.5 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol (2) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0492 | 1023.64 |
| 298.15 | 0.1220 | 1009.9 |
| 298.15 | 0.2072 | 993.05 |
| 298.15 | 0.2706 | 979.89 |
| 298.15 | 0.3633 | 959.86 |
| 298.15 | 0.4478 | 940.7 |
| 298.15 | 0.5261 | 921.85 |
| 298.15 | 0.6103 | 900.63 |
| 298.15 | 0.6770 | 882.99 |
| 298.15 | 0.7613 | 859.54 |
| 298.15 | 0.8332 | 838.49 |
| 298.15 | 0.9232 | 810.57 |
| 298.15 | 1.0000 | 785.18 |
| 303.15 | 0.0492 | 1019.91 |
| 303.15 | 0.1220 | 1006.14 |
| 303.15 | 0.2072 | 989.22 |
| 303.15 | 0.2706 | 976.03 |
| 303.15 | 0.3633 | 955.92 |
| 303.15 | 0.4478 | 936.73 |
| 303.15 | 0.5261 | 917.81 |
| 303.15 | 0.6103 | 896.55 |
| 303.15 | 0.6770 | 878.84 |
| 303.15 | 0.7613 | 855.37 |
| 303.15 | 0.8332 | 834.25 |
| 303.15 | 0.9232 | 806.3 |
| 303.15 | 1.0000 | 780.87 |
| 308.15 | 0.0492 | 1016.16 |
| 308.15 | 0.1220 | 1002.31 |
| 308.15 | 0.2072 | 985.36 |
| 308.15 | 0.2706 | 972.12 |
| 308.15 | 0.3633 | 951.97 |
| 308.15 | 0.4478 | 932.7 |
| 308.15 | 0.5261 | 913.76 |
| 308.15 | 0.6103 | 892.41 |
| 308.15 | 0.6770 | 874.69 |
| 308.15 | 0.7613 | 851.13 |
| 308.15 | 0.8332 | 829.99 |
| 308.15 | 0.9232 | 801.98 |
| 308.15 | 1.0000 | 776.52 |