Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Butanone (1) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0000 | 0.0051 |
| 293.15 | 0.0803 | 0.0038 |
| 293.15 | 0.1583 | 0.0029 |
| 293.15 | 0.2341 | 0.0021 |
| 293.15 | 0.3077 | 0.0016 |
| 293.15 | 0.3794 | 0.0012 |
| 293.15 | 0.4490 | 0.0008 |
| 293.15 | 0.5168 | 0.0007 |
| 293.15 | 0.5828 | 0.0006 |
| 293.15 | 0.6471 | 0.0005 |
| 293.15 | 0.7097 | 0.0005 |
| 293.15 | 0.7707 | 0.0004 |
| 293.15 | 0.8302 | 0.0004 |
| 293.15 | 0.8882 | 0.0004 |
| 293.15 | 0.9448 | 0.0004 |
| 293.15 | 1.0000 | 0.0004 |
| 298.15 | 0.0000 | 0.0045 |
| 298.15 | 0.0803 | 0.0034 |
| 298.15 | 0.1583 | 0.0025 |
| 298.15 | 0.2341 | 0.0019 |
| 298.15 | 0.3077 | 0.0014 |
| 298.15 | 0.3794 | 0.0011 |
| 298.15 | 0.4490 | 0.0008 |
| 298.15 | 0.5168 | 0.0007 |
| 298.15 | 0.5828 | 0.0006 |
| 298.15 | 0.6471 | 0.0005 |
| 298.15 | 0.7097 | 0.0005 |
| 298.15 | 0.7707 | 0.0004 |
| 298.15 | 0.8302 | 0.0004 |
| 298.15 | 0.8882 | 0.0004 |
| 298.15 | 0.9448 | 0.0003 |
| 298.15 | 1.0000 | 0.0003 |
| 303.15 | 0.0000 | 0.0039 |
| 303.15 | 0.0803 | 0.0029 |
| 303.15 | 0.1583 | 0.0021 |
| 303.15 | 0.2341 | 0.0015 |
| 303.15 | 0.3077 | 0.0011 |
| 303.15 | 0.3794 | 0.0009 |
| 303.15 | 0.4490 | 0.0007 |
| 303.15 | 0.5168 | 0.0006 |
| 303.15 | 0.5828 | 0.0005 |
| 303.15 | 0.6471 | 0.0005 |
| 303.15 | 0.7097 | 0.0005 |
| 303.15 | 0.7707 | 0.0005 |
| 303.15 | 0.8302 | 0.0005 |
| 303.15 | 0.8882 | 0.0004 |
| 303.15 | 0.9448 | 0.0004 |
| 303.15 | 1.0000 | 0.0003 |
| 308.15 | 0.0000 | 0.0034 |
| 308.15 | 0.0803 | 0.0025 |
| 308.15 | 0.1583 | 0.0019 |
| 308.15 | 0.2341 | 0.0014 |
| 308.15 | 0.3077 | 0.0011 |
| 308.15 | 0.3794 | 0.0008 |
| 308.15 | 0.4490 | 0.0007 |
| 308.15 | 0.5168 | 0.0006 |
| 308.15 | 0.5828 | 0.0005 |
| 308.15 | 0.6471 | 0.0005 |
| 308.15 | 0.7097 | 0.0005 |
| 308.15 | 0.7707 | 0.0005 |
| 308.15 | 0.8302 | 0.0005 |
| 308.15 | 0.8882 | 0.0004 |
| 308.15 | 0.9448 | 0.0003 |
| 308.15 | 1.0000 | 0.0003 |
| 313.15 | 0.0000 | 0.0029 |
| 313.15 | 0.0803 | 0.0023 |
| 313.15 | 0.1583 | 0.0017 |
| 313.15 | 0.2341 | 0.0013 |
| 313.15 | 0.3077 | 0.0010 |
| 313.15 | 0.3794 | 0.0007 |
| 313.15 | 0.4490 | 0.0006 |
| 313.15 | 0.5168 | 0.0005 |
| 313.15 | 0.5828 | 0.0004 |
| 313.15 | 0.6471 | 0.0004 |
| 313.15 | 0.7097 | 0.0003 |
| 313.15 | 0.7707 | 0.0003 |
| 313.15 | 0.8302 | 0.0003 |
| 313.15 | 0.8882 | 0.0003 |
| 313.15 | 0.9448 | 0.0003 |
| 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 |
| 293.15 | 0.0000 | 0.0051 |
| 293.15 | 0.0803 | 0.0038 |
| 293.15 | 0.1583 | 0.0029 |
| 293.15 | 0.2341 | 0.0021 |
| 293.15 | 0.3077 | 0.0016 |
| 293.15 | 0.3794 | 0.0012 |
| 293.15 | 0.4490 | 0.0008 |
| 293.15 | 0.5168 | 0.0007 |
| 293.15 | 0.5828 | 0.0006 |
| 293.15 | 0.6471 | 0.0005 |
| 293.15 | 0.7097 | 0.0005 |
| 293.15 | 0.7707 | 0.0004 |
| 293.15 | 0.8302 | 0.0004 |
| 293.15 | 0.8882 | 0.0004 |
| 293.15 | 0.9448 | 0.0004 |
| 293.15 | 1.0000 | 0.0004 |
| 298.15 | 0.0000 | 0.0045 |
| 298.15 | 0.0803 | 0.0034 |
| 298.15 | 0.1583 | 0.0025 |
| 298.15 | 0.2341 | 0.0019 |
| 298.15 | 0.3077 | 0.0014 |
| 298.15 | 0.3794 | 0.0011 |
| 298.15 | 0.4490 | 0.0008 |
| 298.15 | 0.5168 | 0.0007 |
| 298.15 | 0.5828 | 0.0006 |
| 298.15 | 0.6471 | 0.0005 |
| 298.15 | 0.7097 | 0.0005 |
| 298.15 | 0.7707 | 0.0004 |
| 298.15 | 0.8302 | 0.0004 |
| 298.15 | 0.8882 | 0.0004 |
| 298.15 | 0.9448 | 0.0003 |
| 298.15 | 1.0000 | 0.0003 |
| 303.15 | 0.0000 | 0.0039 |
| 303.15 | 0.0803 | 0.0029 |
| 303.15 | 0.1583 | 0.0021 |
| 303.15 | 0.2341 | 0.0015 |
| 303.15 | 0.3077 | 0.0011 |
| 303.15 | 0.3794 | 0.0009 |
| 303.15 | 0.4490 | 0.0007 |
| 303.15 | 0.5168 | 0.0006 |
| 303.15 | 0.5828 | 0.0005 |
| 303.15 | 0.6471 | 0.0005 |
| 303.15 | 0.7097 | 0.0005 |
| 303.15 | 0.7707 | 0.0005 |
| 303.15 | 0.8302 | 0.0005 |
| 303.15 | 0.8882 | 0.0004 |
| 303.15 | 0.9448 | 0.0004 |
| 303.15 | 1.0000 | 0.0003 |
| 308.15 | 0.0000 | 0.0034 |
| 308.15 | 0.0803 | 0.0025 |
| 308.15 | 0.1583 | 0.0019 |
| 308.15 | 0.2341 | 0.0014 |
| 308.15 | 0.3077 | 0.0011 |
| 308.15 | 0.3794 | 0.0008 |
| 308.15 | 0.4490 | 0.0007 |
| 308.15 | 0.5168 | 0.0006 |
| 308.15 | 0.5828 | 0.0005 |
| 308.15 | 0.6471 | 0.0005 |
| 308.15 | 0.7097 | 0.0005 |
| 308.15 | 0.7707 | 0.0005 |
| 308.15 | 0.8302 | 0.0005 |
| 308.15 | 0.8882 | 0.0004 |
| 308.15 | 0.9448 | 0.0003 |
| 308.15 | 1.0000 | 0.0003 |
| 313.15 | 0.0000 | 0.0029 |
| 313.15 | 0.0803 | 0.0023 |
| 313.15 | 0.1583 | 0.0017 |
| 313.15 | 0.2341 | 0.0013 |
| 313.15 | 0.3077 | 0.0010 |
| 313.15 | 0.3794 | 0.0007 |
| 313.15 | 0.4490 | 0.0006 |
| 313.15 | 0.5168 | 0.0005 |
| 313.15 | 0.5828 | 0.0004 |
| 313.15 | 0.6471 | 0.0004 |
| 313.15 | 0.7097 | 0.0003 |
| 313.15 | 0.7707 | 0.0003 |
| 313.15 | 0.8302 | 0.0003 |
| 313.15 | 0.8882 | 0.0003 |
| 313.15 | 0.9448 | 0.0003 |
| 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 |
| 293.15 | 0.0000 | 809.61 |
| 293.15 | 0.0803 | 809.22 |
| 293.15 | 0.1583 | 808.84 |
| 293.15 | 0.2341 | 808.48 |
| 293.15 | 0.3077 | 808.13 |
| 293.15 | 0.3794 | 807.79 |
| 293.15 | 0.4490 | 807.47 |
| 293.15 | 0.5168 | 807.16 |
| 293.15 | 0.5828 | 806.85 |
| 293.15 | 0.6471 | 806.56 |
| 293.15 | 0.7097 | 806.27 |
| 293.15 | 0.7707 | 805.99 |
| 293.15 | 0.8302 | 805.71 |
| 293.15 | 0.8882 | 805.45 |
| 293.15 | 0.9448 | 805.18 |
| 293.15 | 1.0000 | 804.92 |
| 298.15 | 0.0000 | 805.01 |
| 298.15 | 0.0803 | 804.57 |
| 298.15 | 0.1583 | 804.15 |
| 298.15 | 0.2341 | 803.74 |
| 298.15 | 0.3077 | 803.35 |
| 298.15 | 0.3794 | 802.97 |
| 298.15 | 0.4490 | 802.6 |
| 298.15 | 0.5168 | 802.24 |
| 298.15 | 0.5828 | 801.89 |
| 298.15 | 0.6471 | 801.56 |
| 298.15 | 0.7097 | 801.23 |
| 298.15 | 0.7707 | 800.91 |
| 298.15 | 0.8302 | 800.6 |
| 298.15 | 0.8882 | 800.29 |
| 298.15 | 0.9448 | 799.99 |
| 298.15 | 1.0000 | 799.7 |
| 303.15 | 0.0000 | 800.41 |
| 303.15 | 0.0803 | 799.94 |
| 303.15 | 0.1583 | 799.49 |
| 303.15 | 0.2341 | 799.06 |
| 303.15 | 0.3077 | 798.85 |
| 303.15 | 0.3794 | 798.25 |
| 303.15 | 0.4490 | 797.86 |
| 303.15 | 0.5168 | 797.48 |
| 303.15 | 0.5828 | 796.12 |
| 303.15 | 0.6471 | 796.77 |
| 303.15 | 0.7097 | 796.43 |
| 303.15 | 0.7707 | 796.08 |
| 303.15 | 0.8302 | 795.75 |
| 303.15 | 0.8882 | 795.42 |
| 303.15 | 0.9448 | 795.11 |
| 303.15 | 1.0000 | 794.81 |
| 308.15 | 0.0000 | 795.81 |
| 308.15 | 0.0803 | 795.3 |
| 308.15 | 0.1583 | 794.82 |
| 308.15 | 0.2341 | 794.36 |
| 308.15 | 0.3077 | 793.92 |
| 308.15 | 0.3794 | 793.49 |
| 308.15 | 0.4490 | 793.07 |
| 308.15 | 0.5168 | 792.67 |
| 308.15 | 0.5828 | 792.27 |
| 308.15 | 0.6471 | 791.89 |
| 308.15 | 0.7097 | 791.52 |
| 308.15 | 0.7707 | 791.15 |
| 308.15 | 0.8302 | 790.79 |
| 308.15 | 0.8882 | 790.44 |
| 308.15 | 0.9448 | 790.1 |
| 308.15 | 1.0000 | 789.78 |
| 313.15 | 0.0000 | 791.21 |
| 313.15 | 0.0803 | 790.63 |
| 313.15 | 0.1583 | 790.09 |
| 313.15 | 0.2341 | 789.57 |
| 313.15 | 0.3077 | 789.06 |
| 313.15 | 0.3794 | 788.57 |
| 313.15 | 0.4490 | 788.09 |
| 313.15 | 0.5168 | 787.63 |
| 313.15 | 0.5828 | 787.18 |
| 313.15 | 0.6471 | 786.74 |
| 313.15 | 0.7097 | 786.32 |
| 313.15 | 0.7707 | 785.9 |
| 313.15 | 0.8302 | 785.49 |
| 313.15 | 0.8882 | 785.09 |
| 313.15 | 0.9448 | 784.7 |
| 313.15 | 1.0000 | 784.32 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Butanone (1) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 809.61 |
| 293.15 | 0.0803 | 809.22 |
| 293.15 | 0.1583 | 808.84 |
| 293.15 | 0.2341 | 808.48 |
| 293.15 | 0.3077 | 808.13 |
| 293.15 | 0.3794 | 807.79 |
| 293.15 | 0.4490 | 807.47 |
| 293.15 | 0.5168 | 807.16 |
| 293.15 | 0.5828 | 806.85 |
| 293.15 | 0.6471 | 806.56 |
| 293.15 | 0.7097 | 806.27 |
| 293.15 | 0.7707 | 805.99 |
| 293.15 | 0.8302 | 805.71 |
| 293.15 | 0.8882 | 805.45 |
| 293.15 | 0.9448 | 805.18 |
| 293.15 | 1.0000 | 804.92 |
| 298.15 | 0.0000 | 805.01 |
| 298.15 | 0.0803 | 804.57 |
| 298.15 | 0.1583 | 804.15 |
| 298.15 | 0.2341 | 803.74 |
| 298.15 | 0.3077 | 803.35 |
| 298.15 | 0.3794 | 802.97 |
| 298.15 | 0.4490 | 802.6 |
| 298.15 | 0.5168 | 802.24 |
| 298.15 | 0.5828 | 801.89 |
| 298.15 | 0.6471 | 801.56 |
| 298.15 | 0.7097 | 801.23 |
| 298.15 | 0.7707 | 800.91 |
| 298.15 | 0.8302 | 800.6 |
| 298.15 | 0.8882 | 800.29 |
| 298.15 | 0.9448 | 799.99 |
| 298.15 | 1.0000 | 799.7 |
| 303.15 | 0.0000 | 800.41 |
| 303.15 | 0.0803 | 799.94 |
| 303.15 | 0.1583 | 799.49 |
| 303.15 | 0.2341 | 799.06 |
| 303.15 | 0.3077 | 798.85 |
| 303.15 | 0.3794 | 798.25 |
| 303.15 | 0.4490 | 797.86 |
| 303.15 | 0.5168 | 797.48 |
| 303.15 | 0.5828 | 796.12 |
| 303.15 | 0.6471 | 796.77 |
| 303.15 | 0.7097 | 796.43 |
| 303.15 | 0.7707 | 796.08 |
| 303.15 | 0.8302 | 795.75 |
| 303.15 | 0.8882 | 795.42 |
| 303.15 | 0.9448 | 795.11 |
| 303.15 | 1.0000 | 794.81 |
| 308.15 | 0.0000 | 795.81 |
| 308.15 | 0.0803 | 795.3 |
| 308.15 | 0.1583 | 794.82 |
| 308.15 | 0.2341 | 794.36 |
| 308.15 | 0.3077 | 793.92 |
| 308.15 | 0.3794 | 793.49 |
| 308.15 | 0.4490 | 793.07 |
| 308.15 | 0.5168 | 792.67 |
| 308.15 | 0.5828 | 792.27 |
| 308.15 | 0.6471 | 791.89 |
| 308.15 | 0.7097 | 791.52 |
| 308.15 | 0.7707 | 791.15 |
| 308.15 | 0.8302 | 790.79 |
| 308.15 | 0.8882 | 790.44 |
| 308.15 | 0.9448 | 790.1 |
| 308.15 | 1.0000 | 789.78 |
| 313.15 | 0.0000 | 791.21 |
| 313.15 | 0.0803 | 790.63 |
| 313.15 | 0.1583 | 790.09 |
| 313.15 | 0.2341 | 789.57 |
| 313.15 | 0.3077 | 789.06 |
| 313.15 | 0.3794 | 788.57 |
| 313.15 | 0.4490 | 788.09 |
| 313.15 | 0.5168 | 787.63 |
| 313.15 | 0.5828 | 787.18 |
| 313.15 | 0.6471 | 786.74 |
| 313.15 | 0.7097 | 786.32 |
| 313.15 | 0.7707 | 785.9 |
| 313.15 | 0.8302 | 785.49 |
| 313.15 | 0.8882 | 785.09 |
| 313.15 | 0.9448 | 784.7 |
| 313.15 | 1.0000 | 784.32 |