Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of 1-Propanol (2) - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
| 0.0000 | 293.15 | 0.0172 |
| 0.0000 | 298.15 | 0.0140 |
| 0.1283 | 293.15 | 0.0151 |
| 0.1283 | 298.15 | 0.0124 |
| 0.2079 | 293.15 | 0.0134 |
| 0.2079 | 298.15 | 0.0111 |
| 0.3145 | 293.15 | 0.0116 |
| 0.3145 | 298.15 | 0.0096 |
| 0.4057 | 293.15 | 0.0101 |
| 0.4057 | 298.15 | 0.0084 |
| 0.5075 | 293.15 | 0.0083 |
| 0.5075 | 298.15 | 0.0070 |
| 0.6096 | 293.15 | 0.0068 |
| 0.6096 | 298.15 | 0.0058 |
| 0.6937 | 293.15 | 0.0056 |
| 0.6937 | 298.15 | 0.0048 |
| 0.7922 | 293.15 | 0.0044 |
| 0.7922 | 298.15 | 0.0038 |
| 0.8907 | 293.15 | 0.0033 |
| 0.8907 | 298.15 | 0.0029 |
| 1.0000 | 293.15 | 0.0023 |
| 1.0000 | 298.15 | 0.0020 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of 1-Propanol (2) - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
| 0.0000 | 293.15 | 0.0172 |
| 0.0000 | 298.15 | 0.0140 |
| 0.1283 | 293.15 | 0.0151 |
| 0.1283 | 298.15 | 0.0124 |
| 0.2079 | 293.15 | 0.0134 |
| 0.2079 | 298.15 | 0.0111 |
| 0.3145 | 293.15 | 0.0116 |
| 0.3145 | 298.15 | 0.0096 |
| 0.4057 | 293.15 | 0.0101 |
| 0.4057 | 298.15 | 0.0084 |
| 0.5075 | 293.15 | 0.0083 |
| 0.5075 | 298.15 | 0.0070 |
| 0.6096 | 293.15 | 0.0068 |
| 0.6096 | 298.15 | 0.0058 |
| 0.6937 | 293.15 | 0.0056 |
| 0.6937 | 298.15 | 0.0048 |
| 0.7922 | 293.15 | 0.0044 |
| 0.7922 | 298.15 | 0.0038 |
| 0.8907 | 293.15 | 0.0033 |
| 0.8907 | 298.15 | 0.0029 |
| 1.0000 | 293.15 | 0.0023 |
| 1.0000 | 298.15 | 0.0020 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of 1-Propanol (2) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 0.0000 | 293.15 | 832.5 |
| 0.0000 | 298.15 | 829.0 |
| 0.1283 | 293.15 | 830.7 |
| 0.1283 | 298.15 | 827.3 |
| 0.2079 | 293.15 | 829.6 |
| 0.2079 | 298.15 | 826.2 |
| 0.3145 | 293.15 | 827.9 |
| 0.3145 | 298.15 | 824.4 |
| 0.4057 | 293.15 | 826.1 |
| 0.4057 | 298.15 | 822.6 |
| 0.5075 | 293.15 | 824.0 |
| 0.5075 | 298.15 | 820.5 |
| 0.6096 | 293.15 | 821.3 |
| 0.6096 | 298.15 | 817.7 |
| 0.6937 | 293.15 | 818.7 |
| 0.6937 | 298.15 | 815.1 |
| 0.7922 | 293.15 | 815.0 |
| 0.7922 | 298.15 | 811.4 |
| 0.8907 | 293.15 | 810.3 |
| 0.8907 | 298.15 | 806.5 |
| 1.0000 | 293.15 | 803.5 |
| 1.0000 | 298.15 | 799.6 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of 1-Propanol (2) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 0.0000 | 293.15 | 832.5 |
| 0.0000 | 298.15 | 829.0 |
| 0.1283 | 293.15 | 830.7 |
| 0.1283 | 298.15 | 827.3 |
| 0.2079 | 293.15 | 829.6 |
| 0.2079 | 298.15 | 826.2 |
| 0.3145 | 293.15 | 827.9 |
| 0.3145 | 298.15 | 824.4 |
| 0.4057 | 293.15 | 826.1 |
| 0.4057 | 298.15 | 822.6 |
| 0.5075 | 293.15 | 824.0 |
| 0.5075 | 298.15 | 820.5 |
| 0.6096 | 293.15 | 821.3 |
| 0.6096 | 298.15 | 817.7 |
| 0.6937 | 293.15 | 818.7 |
| 0.6937 | 298.15 | 815.1 |
| 0.7922 | 293.15 | 815.0 |
| 0.7922 | 298.15 | 811.4 |
| 0.8907 | 293.15 | 810.3 |
| 0.8907 | 298.15 | 806.5 |
| 1.0000 | 293.15 | 803.5 |
| 1.0000 | 298.15 | 799.6 |