Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Butanone (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0000 | 0.0050 |
| 298.15 | 0.0834 | 0.0039 |
| 298.15 | 0.1619 | 0.0031 |
| 298.15 | 0.2426 | 0.0024 |
| 298.15 | 0.3491 | 0.0018 |
| 298.15 | 0.4375 | 0.0014 |
| 298.15 | 0.5661 | 0.0009 |
| 298.15 | 0.6502 | 0.0007 |
| 298.15 | 0.7371 | 0.0006 |
| 298.15 | 0.8498 | 0.0005 |
| 298.15 | 0.9401 | 0.0004 |
| 298.15 | 1.0000 | 0.0004 |
| 303.15 | 0.0000 | 0.0042 |
| 303.15 | 0.0834 | 0.0033 |
| 303.15 | 0.1619 | 0.0026 |
| 303.15 | 0.2426 | 0.0021 |
| 303.15 | 0.3491 | 0.0015 |
| 303.15 | 0.4375 | 0.0012 |
| 303.15 | 0.5661 | 0.0008 |
| 303.15 | 0.6502 | 0.0007 |
| 303.15 | 0.7371 | 0.0006 |
| 303.15 | 0.8498 | 0.0004 |
| 303.15 | 0.9401 | 0.0004 |
| 303.15 | 1.0000 | 0.0004 |
| 308.15 | 0.0000 | 0.0035 |
| 308.15 | 0.0834 | 0.0027 |
| 308.15 | 0.1619 | 0.0022 |
| 308.15 | 0.2426 | 0.0018 |
| 308.15 | 0.3491 | 0.0013 |
| 308.15 | 0.4375 | 0.0010 |
| 308.15 | 0.5661 | 0.0007 |
| 308.15 | 0.6502 | 0.0006 |
| 308.15 | 0.7371 | 0.0005 |
| 308.15 | 0.8498 | 0.0004 |
| 308.15 | 0.9401 | 0.0004 |
| 308.15 | 1.0000 | 0.0004 |
| 313.15 | 0.0000 | 0.0029 |
| 313.15 | 0.0834 | 0.0023 |
| 313.15 | 0.1619 | 0.0018 |
| 313.15 | 0.2426 | 0.0015 |
| 313.15 | 0.3491 | 0.0011 |
| 313.15 | 0.4375 | 0.0009 |
| 313.15 | 0.5661 | 0.0007 |
| 313.15 | 0.6502 | 0.0006 |
| 313.15 | 0.7371 | 0.0005 |
| 313.15 | 0.8498 | 0.0004 |
| 313.15 | 0.9401 | 0.0004 |
| 313.15 | 1.0000 | 0.0003 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Butanone (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0000 | 0.0050 |
| 298.15 | 0.0834 | 0.0039 |
| 298.15 | 0.1619 | 0.0031 |
| 298.15 | 0.2426 | 0.0024 |
| 298.15 | 0.3491 | 0.0018 |
| 298.15 | 0.4375 | 0.0014 |
| 298.15 | 0.5661 | 0.0009 |
| 298.15 | 0.6502 | 0.0007 |
| 298.15 | 0.7371 | 0.0006 |
| 298.15 | 0.8498 | 0.0005 |
| 298.15 | 0.9401 | 0.0004 |
| 298.15 | 1.0000 | 0.0004 |
| 303.15 | 0.0000 | 0.0042 |
| 303.15 | 0.0834 | 0.0033 |
| 303.15 | 0.1619 | 0.0026 |
| 303.15 | 0.2426 | 0.0021 |
| 303.15 | 0.3491 | 0.0015 |
| 303.15 | 0.4375 | 0.0012 |
| 303.15 | 0.5661 | 0.0008 |
| 303.15 | 0.6502 | 0.0007 |
| 303.15 | 0.7371 | 0.0006 |
| 303.15 | 0.8498 | 0.0004 |
| 303.15 | 0.9401 | 0.0004 |
| 303.15 | 1.0000 | 0.0004 |
| 308.15 | 0.0000 | 0.0035 |
| 308.15 | 0.0834 | 0.0027 |
| 308.15 | 0.1619 | 0.0022 |
| 308.15 | 0.2426 | 0.0018 |
| 308.15 | 0.3491 | 0.0013 |
| 308.15 | 0.4375 | 0.0010 |
| 308.15 | 0.5661 | 0.0007 |
| 308.15 | 0.6502 | 0.0006 |
| 308.15 | 0.7371 | 0.0005 |
| 308.15 | 0.8498 | 0.0004 |
| 308.15 | 0.9401 | 0.0004 |
| 308.15 | 1.0000 | 0.0004 |
| 313.15 | 0.0000 | 0.0029 |
| 313.15 | 0.0834 | 0.0023 |
| 313.15 | 0.1619 | 0.0018 |
| 313.15 | 0.2426 | 0.0015 |
| 313.15 | 0.3491 | 0.0011 |
| 313.15 | 0.4375 | 0.0009 |
| 313.15 | 0.5661 | 0.0007 |
| 313.15 | 0.6502 | 0.0006 |
| 313.15 | 0.7371 | 0.0005 |
| 313.15 | 0.8498 | 0.0004 |
| 313.15 | 0.9401 | 0.0004 |
| 313.15 | 1.0000 | 0.0003 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Butanone (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 813.18 |
| 298.15 | 0.0834 | 811.4 |
| 298.15 | 0.1619 | 809.92 |
| 298.15 | 0.2426 | 808.4 |
| 298.15 | 0.3491 | 806.63 |
| 298.15 | 0.4375 | 805.3 |
| 298.15 | 0.5661 | 803.5 |
| 298.15 | 0.6502 | 802.41 |
| 298.15 | 0.7371 | 801.4 |
| 298.15 | 0.8498 | 800.4 |
| 298.15 | 0.9401 | 799.73 |
| 298.15 | 1.0000 | 799.48 |
| 303.15 | 0.0000 | 809.26 |
| 303.15 | 0.0834 | 807.5 |
| 303.15 | 0.1619 | 805.97 |
| 303.15 | 0.2426 | 804.47 |
| 303.15 | 0.3491 | 802.53 |
| 303.15 | 0.4375 | 801.03 |
| 303.15 | 0.5661 | 799.1 |
| 303.15 | 0.6502 | 797.92 |
| 303.15 | 0.7371 | 796.84 |
| 303.15 | 0.8498 | 795.59 |
| 303.15 | 0.9401 | 794.95 |
| 303.15 | 1.0000 | 794.63 |
| 308.15 | 0.0000 | 805.01 |
| 308.15 | 0.0834 | 803.22 |
| 308.15 | 0.1619 | 801.7 |
| 308.15 | 0.2426 | 800.16 |
| 308.15 | 0.3491 | 798.16 |
| 308.15 | 0.4375 | 796.6 |
| 308.15 | 0.5661 | 794.57 |
| 308.15 | 0.6502 | 793.35 |
| 308.15 | 0.7371 | 792.26 |
| 308.15 | 0.8498 | 790.95 |
| 308.15 | 0.9401 | 790.35 |
| 308.15 | 1.0000 | 789.9 |
| 313.15 | 0.0000 | 801.14 |
| 313.15 | 0.0834 | 799.4 |
| 313.15 | 0.1619 | 797.73 |
| 313.15 | 0.2426 | 796.12 |
| 313.15 | 0.3491 | 794.11 |
| 313.15 | 0.4375 | 792.53 |
| 313.15 | 0.5661 | 790.44 |
| 313.15 | 0.6502 | 789.19 |
| 313.15 | 0.7371 | 788.05 |
| 313.15 | 0.8498 | 786.69 |
| 313.15 | 0.9401 | 786.0 |
| 313.15 | 1.0000 | 785.52 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Butanone (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0000 | 813.18 |
| 298.15 | 0.0834 | 811.4 |
| 298.15 | 0.1619 | 809.92 |
| 298.15 | 0.2426 | 808.4 |
| 298.15 | 0.3491 | 806.63 |
| 298.15 | 0.4375 | 805.3 |
| 298.15 | 0.5661 | 803.5 |
| 298.15 | 0.6502 | 802.41 |
| 298.15 | 0.7371 | 801.4 |
| 298.15 | 0.8498 | 800.4 |
| 298.15 | 0.9401 | 799.73 |
| 298.15 | 1.0000 | 799.48 |
| 303.15 | 0.0000 | 809.26 |
| 303.15 | 0.0834 | 807.5 |
| 303.15 | 0.1619 | 805.97 |
| 303.15 | 0.2426 | 804.47 |
| 303.15 | 0.3491 | 802.53 |
| 303.15 | 0.4375 | 801.03 |
| 303.15 | 0.5661 | 799.1 |
| 303.15 | 0.6502 | 797.92 |
| 303.15 | 0.7371 | 796.84 |
| 303.15 | 0.8498 | 795.59 |
| 303.15 | 0.9401 | 794.95 |
| 303.15 | 1.0000 | 794.63 |
| 308.15 | 0.0000 | 805.01 |
| 308.15 | 0.0834 | 803.22 |
| 308.15 | 0.1619 | 801.7 |
| 308.15 | 0.2426 | 800.16 |
| 308.15 | 0.3491 | 798.16 |
| 308.15 | 0.4375 | 796.6 |
| 308.15 | 0.5661 | 794.57 |
| 308.15 | 0.6502 | 793.35 |
| 308.15 | 0.7371 | 792.26 |
| 308.15 | 0.8498 | 790.95 |
| 308.15 | 0.9401 | 790.35 |
| 308.15 | 1.0000 | 789.9 |
| 313.15 | 0.0000 | 801.14 |
| 313.15 | 0.0834 | 799.4 |
| 313.15 | 0.1619 | 797.73 |
| 313.15 | 0.2426 | 796.12 |
| 313.15 | 0.3491 | 794.11 |
| 313.15 | 0.4375 | 792.53 |
| 313.15 | 0.5661 | 790.44 |
| 313.15 | 0.6502 | 789.19 |
| 313.15 | 0.7371 | 788.05 |
| 313.15 | 0.8498 | 786.69 |
| 313.15 | 0.9401 | 786.0 |
| 313.15 | 1.0000 | 785.52 |