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 | 0.0046 |
298.15 | 0.0843 | 0.0028 |
298.15 | 0.1622 | 0.0020 |
298.15 | 0.2428 | 0.0015 |
298.15 | 0.3505 | 0.0011 |
298.15 | 0.4415 | 0.0009 |
298.15 | 0.5584 | 0.0007 |
298.15 | 0.6526 | 0.0006 |
298.15 | 0.7399 | 0.0005 |
298.15 | 0.8540 | 0.0004 |
298.15 | 0.9383 | 0.0004 |
298.15 | 1.0000 | 0.0004 |
308.15 | 0.0000 | 0.0029 |
308.15 | 0.0843 | 0.0020 |
308.15 | 0.1622 | 0.0015 |
308.15 | 0.2428 | 0.0012 |
308.15 | 0.3505 | 0.0009 |
308.15 | 0.4415 | 0.0007 |
308.15 | 0.5584 | 0.0006 |
308.15 | 0.6526 | 0.0005 |
308.15 | 0.7399 | 0.0004 |
308.15 | 0.8540 | 0.0004 |
308.15 | 0.9383 | 0.0004 |
308.15 | 1.0000 | 0.0004 |
318.15 | 0.0000 | 0.0019 |
318.15 | 0.0843 | 0.0014 |
318.15 | 0.1622 | 0.0010 |
318.15 | 0.2428 | 0.0007 |
318.15 | 0.3505 | 0.0005 |
318.15 | 0.4415 | 0.0004 |
318.15 | 0.5584 | 0.0003 |
318.15 | 0.6526 | 0.0003 |
318.15 | 0.7399 | 0.0003 |
318.15 | 0.8540 | 0.0003 |
318.15 | 0.9383 | 0.0003 |
318.15 | 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 | 0.0046 |
298.15 | 0.0843 | 0.0028 |
298.15 | 0.1622 | 0.0020 |
298.15 | 0.2428 | 0.0015 |
298.15 | 0.3505 | 0.0011 |
298.15 | 0.4415 | 0.0009 |
298.15 | 0.5584 | 0.0007 |
298.15 | 0.6526 | 0.0006 |
298.15 | 0.7399 | 0.0005 |
298.15 | 0.8540 | 0.0004 |
298.15 | 0.9383 | 0.0004 |
298.15 | 1.0000 | 0.0004 |
308.15 | 0.0000 | 0.0029 |
308.15 | 0.0843 | 0.0020 |
308.15 | 0.1622 | 0.0015 |
308.15 | 0.2428 | 0.0012 |
308.15 | 0.3505 | 0.0009 |
308.15 | 0.4415 | 0.0007 |
308.15 | 0.5584 | 0.0006 |
308.15 | 0.6526 | 0.0005 |
308.15 | 0.7399 | 0.0004 |
308.15 | 0.8540 | 0.0004 |
308.15 | 0.9383 | 0.0004 |
308.15 | 1.0000 | 0.0004 |
318.15 | 0.0000 | 0.0019 |
318.15 | 0.0843 | 0.0014 |
318.15 | 0.1622 | 0.0010 |
318.15 | 0.2428 | 0.0007 |
318.15 | 0.3505 | 0.0005 |
318.15 | 0.4415 | 0.0004 |
318.15 | 0.5584 | 0.0003 |
318.15 | 0.6526 | 0.0003 |
318.15 | 0.7399 | 0.0003 |
318.15 | 0.8540 | 0.0003 |
318.15 | 0.9383 | 0.0003 |
318.15 | 1.0000 | 0.0003 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 2-Butanone (1) - Liquid | Refractive index (Na D-line) - Liquid |
298.15 | 0.0000 | 1.4047 |
298.15 | 0.0843 | 1.4032 |
298.15 | 0.1622 | 1.4016 |
298.15 | 0.2428 | 1.3999 |
298.15 | 0.3505 | 1.3971 |
298.15 | 0.4415 | 1.3945 |
298.15 | 0.5584 | 1.3908 |
298.15 | 0.6526 | 1.3876 |
298.15 | 0.7399 | 1.3846 |
298.15 | 0.8540 | 1.3803 |
298.15 | 0.9383 | 1.3773 |
298.15 | 1.0000 | 1.375 |
308.15 | 0.0000 | 1.4029 |
308.15 | 0.0843 | 1.4012 |
308.15 | 0.1622 | 1.3995 |
308.15 | 0.2428 | 1.3975 |
308.15 | 0.3505 | 1.3944 |
308.15 | 0.4415 | 1.3916 |
308.15 | 0.5584 | 1.3876 |
308.15 | 0.6526 | 1.3841 |
308.15 | 0.7399 | 1.3806 |
308.15 | 0.8540 | 1.376 |
308.15 | 0.9383 | 1.3725 |
308.15 | 1.0000 | 1.37 |
318.15 | 0.0000 | 1.3981 |
318.15 | 0.0843 | 1.3965 |
318.15 | 0.1622 | 1.3949 |
318.15 | 0.2428 | 1.3929 |
318.15 | 0.3505 | 1.3901 |
318.15 | 0.4415 | 1.3873 |
318.15 | 0.5584 | 1.3835 |
318.15 | 0.6526 | 1.38 |
318.15 | 0.7399 | 1.3767 |
318.15 | 0.8540 | 1.372 |
318.15 | 0.9383 | 1.3684 |
318.15 | 1.0000 | 1.3657 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 2-Butanone (1) - Liquid | Refractive index (Na D-line) - Liquid |
298.15 | 0.0000 | 1.4047 |
298.15 | 0.0843 | 1.4032 |
298.15 | 0.1622 | 1.4016 |
298.15 | 0.2428 | 1.3999 |
298.15 | 0.3505 | 1.3971 |
298.15 | 0.4415 | 1.3945 |
298.15 | 0.5584 | 1.3908 |
298.15 | 0.6526 | 1.3876 |
298.15 | 0.7399 | 1.3846 |
298.15 | 0.8540 | 1.3803 |
298.15 | 0.9383 | 1.3773 |
298.15 | 1.0000 | 1.375 |
308.15 | 0.0000 | 1.4029 |
308.15 | 0.0843 | 1.4012 |
308.15 | 0.1622 | 1.3995 |
308.15 | 0.2428 | 1.3975 |
308.15 | 0.3505 | 1.3944 |
308.15 | 0.4415 | 1.3916 |
308.15 | 0.5584 | 1.3876 |
308.15 | 0.6526 | 1.3841 |
308.15 | 0.7399 | 1.3806 |
308.15 | 0.8540 | 1.376 |
308.15 | 0.9383 | 1.3725 |
308.15 | 1.0000 | 1.37 |
318.15 | 0.0000 | 1.3981 |
318.15 | 0.0843 | 1.3965 |
318.15 | 0.1622 | 1.3949 |
318.15 | 0.2428 | 1.3929 |
318.15 | 0.3505 | 1.3901 |
318.15 | 0.4415 | 1.3873 |
318.15 | 0.5584 | 1.3835 |
318.15 | 0.6526 | 1.38 |
318.15 | 0.7399 | 1.3767 |
318.15 | 0.8540 | 1.372 |
318.15 | 0.9383 | 1.3684 |
318.15 | 1.0000 | 1.3657 |
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 | 815.79 |
298.15 | 0.0843 | 813.43 |
298.15 | 0.1622 | 811.5 |
298.15 | 0.2428 | 809.72 |
298.15 | 0.3505 | 807.45 |
298.15 | 0.4415 | 805.82 |
298.15 | 0.5584 | 803.92 |
298.15 | 0.6526 | 802.64 |
298.15 | 0.7399 | 801.72 |
298.15 | 0.8540 | 800.8 |
298.15 | 0.9383 | 800.16 |
298.15 | 1.0000 | 799.76 |
308.15 | 0.0000 | 806.91 |
308.15 | 0.0843 | 804.58 |
308.15 | 0.1622 | 802.6 |
308.15 | 0.2428 | 800.57 |
308.15 | 0.3505 | 798.07 |
308.15 | 0.4415 | 796.23 |
308.15 | 0.5584 | 794.1 |
308.15 | 0.6526 | 792.64 |
308.15 | 0.7399 | 791.55 |
308.15 | 0.8540 | 790.31 |
308.15 | 0.9383 | 789.7 |
308.15 | 1.0000 | 789.21 |
318.15 | 0.0000 | 797.66 |
318.15 | 0.0843 | 795.034 |
318.15 | 0.1622 | 792.888 |
318.15 | 0.2428 | 790.723 |
318.15 | 0.3505 | 788.175 |
318.15 | 0.4415 | 786.285 |
318.15 | 0.5584 | 784.161 |
318.15 | 0.6526 | 782.699 |
318.15 | 0.7399 | 781.619 |
318.15 | 0.8540 | 780.165 |
318.15 | 0.9383 | 779.212 |
318.15 | 1.0000 | 778.52 |
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 | 815.79 |
298.15 | 0.0843 | 813.43 |
298.15 | 0.1622 | 811.5 |
298.15 | 0.2428 | 809.72 |
298.15 | 0.3505 | 807.45 |
298.15 | 0.4415 | 805.82 |
298.15 | 0.5584 | 803.92 |
298.15 | 0.6526 | 802.64 |
298.15 | 0.7399 | 801.72 |
298.15 | 0.8540 | 800.8 |
298.15 | 0.9383 | 800.16 |
298.15 | 1.0000 | 799.76 |
308.15 | 0.0000 | 806.91 |
308.15 | 0.0843 | 804.58 |
308.15 | 0.1622 | 802.6 |
308.15 | 0.2428 | 800.57 |
308.15 | 0.3505 | 798.07 |
308.15 | 0.4415 | 796.23 |
308.15 | 0.5584 | 794.1 |
308.15 | 0.6526 | 792.64 |
308.15 | 0.7399 | 791.55 |
308.15 | 0.8540 | 790.31 |
308.15 | 0.9383 | 789.7 |
308.15 | 1.0000 | 789.21 |
318.15 | 0.0000 | 797.66 |
318.15 | 0.0843 | 795.034 |
318.15 | 0.1622 | 792.888 |
318.15 | 0.2428 | 790.723 |
318.15 | 0.3505 | 788.175 |
318.15 | 0.4415 | 786.285 |
318.15 | 0.5584 | 784.161 |
318.15 | 0.6526 | 782.699 |
318.15 | 0.7399 | 781.619 |
318.15 | 0.8540 | 780.165 |
318.15 | 0.9383 | 779.212 |
318.15 | 1.0000 | 778.52 |