Operational condition: Pressure, kPa = 203 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Mesitylene (2) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0000 | 0.0020 |
| 298.15 | 0.1011 | 0.0015 |
| 298.15 | 0.2005 | 0.0012 |
| 298.15 | 0.3055 | 0.0010 |
| 298.15 | 0.4001 | 0.0009 |
| 298.15 | 0.5008 | 0.0008 |
| 298.15 | 0.6035 | 0.0007 |
| 298.15 | 0.6979 | 0.0007 |
| 298.15 | 0.8014 | 0.0007 |
| 298.15 | 0.8940 | 0.0006 |
| 298.15 | 1.0000 | 0.0006 |
| 303.15 | 0.0000 | 0.0018 |
| 303.15 | 0.1011 | 0.0013 |
| 303.15 | 0.2005 | 0.0010 |
| 303.15 | 0.3055 | 0.0009 |
| 303.15 | 0.4001 | 0.0008 |
| 303.15 | 0.5008 | 0.0007 |
| 303.15 | 0.6035 | 0.0007 |
| 303.15 | 0.6979 | 0.0006 |
| 303.15 | 0.8014 | 0.0006 |
| 303.15 | 0.8940 | 0.0006 |
| 303.15 | 1.0000 | 0.0006 |
| 308.15 | 0.0000 | 0.0015 |
| 308.15 | 0.1011 | 0.0011 |
| 308.15 | 0.2005 | 0.0009 |
| 308.15 | 0.3055 | 0.0008 |
| 308.15 | 0.4001 | 0.0007 |
| 308.15 | 0.5008 | 0.0007 |
| 308.15 | 0.6035 | 0.0006 |
| 308.15 | 0.6979 | 0.0006 |
| 308.15 | 0.8014 | 0.0006 |
| 308.15 | 0.8940 | 0.0006 |
| 308.15 | 1.0000 | 0.0006 |
Operational condition: Pressure, kPa = 203 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Mesitylene (2) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0000 | 0.0020 |
| 298.15 | 0.1011 | 0.0015 |
| 298.15 | 0.2005 | 0.0012 |
| 298.15 | 0.3055 | 0.0010 |
| 298.15 | 0.4001 | 0.0009 |
| 298.15 | 0.5008 | 0.0008 |
| 298.15 | 0.6035 | 0.0007 |
| 298.15 | 0.6979 | 0.0007 |
| 298.15 | 0.8014 | 0.0007 |
| 298.15 | 0.8940 | 0.0006 |
| 298.15 | 1.0000 | 0.0006 |
| 303.15 | 0.0000 | 0.0018 |
| 303.15 | 0.1011 | 0.0013 |
| 303.15 | 0.2005 | 0.0010 |
| 303.15 | 0.3055 | 0.0009 |
| 303.15 | 0.4001 | 0.0008 |
| 303.15 | 0.5008 | 0.0007 |
| 303.15 | 0.6035 | 0.0007 |
| 303.15 | 0.6979 | 0.0006 |
| 303.15 | 0.8014 | 0.0006 |
| 303.15 | 0.8940 | 0.0006 |
| 303.15 | 1.0000 | 0.0006 |
| 308.15 | 0.0000 | 0.0015 |
| 308.15 | 0.1011 | 0.0011 |
| 308.15 | 0.2005 | 0.0009 |
| 308.15 | 0.3055 | 0.0008 |
| 308.15 | 0.4001 | 0.0007 |
| 308.15 | 0.5008 | 0.0007 |
| 308.15 | 0.6035 | 0.0006 |
| 308.15 | 0.6979 | 0.0006 |
| 308.15 | 0.8014 | 0.0006 |
| 308.15 | 0.8940 | 0.0006 |
| 308.15 | 1.0000 | 0.0006 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Mesitylene (2) - Liquid | Refractive index (Na D-line) - Liquid |
| 298.15 | 0.0000 | 1.3745 |
| 298.15 | 0.1011 | 1.394 |
| 298.15 | 0.2005 | 1.4115 |
| 298.15 | 0.3055 | 1.4272 |
| 298.15 | 0.4001 | 1.4393 |
| 298.15 | 0.5008 | 1.4483 |
| 298.15 | 0.6035 | 1.4634 |
| 298.15 | 0.6979 | 1.4711 |
| 298.15 | 0.8014 | 1.4813 |
| 298.15 | 0.8940 | 1.4879 |
| 298.15 | 1.0000 | 1.4958 |
| 303.15 | 0.0000 | 1.3721 |
| 303.15 | 0.1011 | 1.3919 |
| 303.15 | 0.2005 | 1.4092 |
| 303.15 | 0.3055 | 1.4248 |
| 303.15 | 0.4001 | 1.437 |
| 303.15 | 0.5008 | 1.4465 |
| 303.15 | 0.6035 | 1.4607 |
| 303.15 | 0.6979 | 1.4688 |
| 303.15 | 0.8014 | 1.4779 |
| 303.15 | 0.8940 | 1.485 |
| 303.15 | 1.0000 | 1.4928 |
| 308.15 | 0.0000 | 1.3702 |
| 308.15 | 0.1011 | 1.3894 |
| 308.15 | 0.2005 | 1.4064 |
| 308.15 | 0.3055 | 1.4219 |
| 308.15 | 0.4001 | 1.4347 |
| 308.15 | 0.5008 | 1.4458 |
| 308.15 | 0.6035 | 1.4576 |
| 308.15 | 0.6979 | 1.4656 |
| 308.15 | 0.8014 | 1.4756 |
| 308.15 | 0.8940 | 1.4824 |
| 308.15 | 1.0000 | 1.4898 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Mesitylene (2) - Liquid | Refractive index (Na D-line) - Liquid |
| 298.15 | 0.0000 | 1.3745 |
| 298.15 | 0.1011 | 1.394 |
| 298.15 | 0.2005 | 1.4115 |
| 298.15 | 0.3055 | 1.4272 |
| 298.15 | 0.4001 | 1.4393 |
| 298.15 | 0.5008 | 1.4483 |
| 298.15 | 0.6035 | 1.4634 |
| 298.15 | 0.6979 | 1.4711 |
| 298.15 | 0.8014 | 1.4813 |
| 298.15 | 0.8940 | 1.4879 |
| 298.15 | 1.0000 | 1.4958 |
| 303.15 | 0.0000 | 1.3721 |
| 303.15 | 0.1011 | 1.3919 |
| 303.15 | 0.2005 | 1.4092 |
| 303.15 | 0.3055 | 1.4248 |
| 303.15 | 0.4001 | 1.437 |
| 303.15 | 0.5008 | 1.4465 |
| 303.15 | 0.6035 | 1.4607 |
| 303.15 | 0.6979 | 1.4688 |
| 303.15 | 0.8014 | 1.4779 |
| 303.15 | 0.8940 | 1.485 |
| 303.15 | 1.0000 | 1.4928 |
| 308.15 | 0.0000 | 1.3702 |
| 308.15 | 0.1011 | 1.3894 |
| 308.15 | 0.2005 | 1.4064 |
| 308.15 | 0.3055 | 1.4219 |
| 308.15 | 0.4001 | 1.4347 |
| 308.15 | 0.5008 | 1.4458 |
| 308.15 | 0.6035 | 1.4576 |
| 308.15 | 0.6979 | 1.4656 |
| 308.15 | 0.8014 | 1.4756 |
| 308.15 | 0.8940 | 1.4824 |
| 308.15 | 1.0000 | 1.4898 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Mesitylene (2) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 781.36 |
| 298.15 | 0.1011 | 793.81 |
| 298.15 | 0.2005 | 804.44 |
| 298.15 | 0.3055 | 814.27 |
| 298.15 | 0.4001 | 822.26 |
| 298.15 | 0.5008 | 829.63 |
| 298.15 | 0.6035 | 836.85 |
| 298.15 | 0.6979 | 842.79 |
| 298.15 | 0.8014 | 848.84 |
| 298.15 | 0.8940 | 854.1 |
| 298.15 | 1.0000 | 860.5 |
| 303.15 | 0.0000 | 777.09 |
| 303.15 | 0.1011 | 789.43 |
| 303.15 | 0.2005 | 800.01 |
| 303.15 | 0.3055 | 809.81 |
| 303.15 | 0.4001 | 817.79 |
| 303.15 | 0.5008 | 825.18 |
| 303.15 | 0.6035 | 832.45 |
| 303.15 | 0.6979 | 838.43 |
| 303.15 | 0.8014 | 844.55 |
| 303.15 | 0.8940 | 849.87 |
| 303.15 | 1.0000 | 856.4 |
| 308.15 | 0.0000 | 772.75 |
| 308.15 | 0.1011 | 784.98 |
| 308.15 | 0.2005 | 795.51 |
| 308.15 | 0.3055 | 805.51 |
| 308.15 | 0.4001 | 813.28 |
| 308.15 | 0.5008 | 820.69 |
| 308.15 | 0.6035 | 828.01 |
| 308.15 | 0.6979 | 834.04 |
| 308.15 | 0.8014 | 840.22 |
| 308.15 | 0.8940 | 845.62 |
| 308.15 | 1.0000 | 852.29 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Mesitylene (2) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 781.36 |
| 298.15 | 0.1011 | 793.81 |
| 298.15 | 0.2005 | 804.44 |
| 298.15 | 0.3055 | 814.27 |
| 298.15 | 0.4001 | 822.26 |
| 298.15 | 0.5008 | 829.63 |
| 298.15 | 0.6035 | 836.85 |
| 298.15 | 0.6979 | 842.79 |
| 298.15 | 0.8014 | 848.84 |
| 298.15 | 0.8940 | 854.1 |
| 298.15 | 1.0000 | 860.5 |
| 303.15 | 0.0000 | 777.09 |
| 303.15 | 0.1011 | 789.43 |
| 303.15 | 0.2005 | 800.01 |
| 303.15 | 0.3055 | 809.81 |
| 303.15 | 0.4001 | 817.79 |
| 303.15 | 0.5008 | 825.18 |
| 303.15 | 0.6035 | 832.45 |
| 303.15 | 0.6979 | 838.43 |
| 303.15 | 0.8014 | 844.55 |
| 303.15 | 0.8940 | 849.87 |
| 303.15 | 1.0000 | 856.4 |
| 308.15 | 0.0000 | 772.75 |
| 308.15 | 0.1011 | 784.98 |
| 308.15 | 0.2005 | 795.51 |
| 308.15 | 0.3055 | 805.51 |
| 308.15 | 0.4001 | 813.28 |
| 308.15 | 0.5008 | 820.69 |
| 308.15 | 0.6035 | 828.01 |
| 308.15 | 0.6979 | 834.04 |
| 308.15 | 0.8014 | 840.22 |
| 308.15 | 0.8940 | 845.62 |
| 308.15 | 1.0000 | 852.29 |