Operational condition: Pressure, kPa = 101.8 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Undecanol (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.1050 | 0.0167 |
| 298.15 | 0.3165 | 0.0161 |
| 298.15 | 0.5196 | 0.0155 |
| 298.15 | 0.7165 | 0.0150 |
| 298.15 | 0.9076 | 0.0145 |
| 308.15 | 0.1050 | 0.0113 |
| 308.15 | 0.3165 | 0.0109 |
| 308.15 | 0.5196 | 0.0106 |
| 308.15 | 0.7165 | 0.0102 |
| 308.15 | 0.9076 | 0.0099 |
| 318.15 | 0.1050 | 0.0079 |
| 318.15 | 0.3165 | 0.0076 |
| 318.15 | 0.5196 | 0.0074 |
| 318.15 | 0.7165 | 0.0072 |
| 318.15 | 0.9076 | 0.0070 |
| 328.15 | 0.1050 | 0.0057 |
| 328.15 | 0.3165 | 0.0055 |
| 328.15 | 0.5196 | 0.0054 |
| 328.15 | 0.7165 | 0.0052 |
| 328.15 | 0.9076 | 0.0051 |
| 338.15 | 0.1050 | 0.0042 |
| 338.15 | 0.3165 | 0.0041 |
| 338.15 | 0.5196 | 0.0040 |
| 338.15 | 0.7165 | 0.0039 |
| 338.15 | 0.9076 | 0.0038 |
Operational condition: Pressure, kPa = 101.8 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Undecanol (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.1050 | 0.0167 |
| 298.15 | 0.3165 | 0.0161 |
| 298.15 | 0.5196 | 0.0155 |
| 298.15 | 0.7165 | 0.0150 |
| 298.15 | 0.9076 | 0.0145 |
| 308.15 | 0.1050 | 0.0113 |
| 308.15 | 0.3165 | 0.0109 |
| 308.15 | 0.5196 | 0.0106 |
| 308.15 | 0.7165 | 0.0102 |
| 308.15 | 0.9076 | 0.0099 |
| 318.15 | 0.1050 | 0.0079 |
| 318.15 | 0.3165 | 0.0076 |
| 318.15 | 0.5196 | 0.0074 |
| 318.15 | 0.7165 | 0.0072 |
| 318.15 | 0.9076 | 0.0070 |
| 328.15 | 0.1050 | 0.0057 |
| 328.15 | 0.3165 | 0.0055 |
| 328.15 | 0.5196 | 0.0054 |
| 328.15 | 0.7165 | 0.0052 |
| 328.15 | 0.9076 | 0.0051 |
| 338.15 | 0.1050 | 0.0042 |
| 338.15 | 0.3165 | 0.0041 |
| 338.15 | 0.5196 | 0.0040 |
| 338.15 | 0.7165 | 0.0039 |
| 338.15 | 0.9076 | 0.0038 |
Operational condition: Pressure, kPa = 101.8 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Undecanol (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.1050 | 829.4 |
| 298.15 | 0.3165 | 829.2 |
| 298.15 | 0.5196 | 828.9 |
| 298.15 | 0.7165 | 828.4 |
| 298.15 | 0.9076 | 828.0 |
| 308.15 | 0.1050 | 822.6 |
| 308.15 | 0.3165 | 822.3 |
| 308.15 | 0.5196 | 822.0 |
| 308.15 | 0.7165 | 821.6 |
| 308.15 | 0.9076 | 821.2 |
| 318.15 | 0.1050 | 815.8 |
| 318.15 | 0.3165 | 815.5 |
| 318.15 | 0.5196 | 815.2 |
| 318.15 | 0.7165 | 814.8 |
| 318.15 | 0.9076 | 814.4 |
| 328.15 | 0.1050 | 808.9 |
| 328.15 | 0.3165 | 808.6 |
| 328.15 | 0.5196 | 808.3 |
| 328.15 | 0.7165 | 807.9 |
| 328.15 | 0.9076 | 807.4 |
| 338.15 | 0.1050 | 801.9 |
| 338.15 | 0.3165 | 801.6 |
| 338.15 | 0.5196 | 801.3 |
| 338.15 | 0.7165 | 800.9 |
| 338.15 | 0.9076 | 800.4 |
Operational condition: Pressure, kPa = 101.8 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 1-Undecanol (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.1050 | 829.4 |
| 298.15 | 0.3165 | 829.2 |
| 298.15 | 0.5196 | 828.9 |
| 298.15 | 0.7165 | 828.4 |
| 298.15 | 0.9076 | 828.0 |
| 308.15 | 0.1050 | 822.6 |
| 308.15 | 0.3165 | 822.3 |
| 308.15 | 0.5196 | 822.0 |
| 308.15 | 0.7165 | 821.6 |
| 308.15 | 0.9076 | 821.2 |
| 318.15 | 0.1050 | 815.8 |
| 318.15 | 0.3165 | 815.5 |
| 318.15 | 0.5196 | 815.2 |
| 318.15 | 0.7165 | 814.8 |
| 318.15 | 0.9076 | 814.4 |
| 328.15 | 0.1050 | 808.9 |
| 328.15 | 0.3165 | 808.6 |
| 328.15 | 0.5196 | 808.3 |
| 328.15 | 0.7165 | 807.9 |
| 328.15 | 0.9076 | 807.4 |
| 338.15 | 0.1050 | 801.9 |
| 338.15 | 0.3165 | 801.6 |
| 338.15 | 0.5196 | 801.3 |
| 338.15 | 0.7165 | 800.9 |
| 338.15 | 0.9076 | 800.4 |