Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Cyclohexanone (1) - Liquid | Viscosity, Pa*s - Liquid |
| 288.15 | 0.0911 | 0.0006 |
| 288.15 | 0.1761 | 0.0007 |
| 288.15 | 0.3304 | 0.0008 |
| 288.15 | 0.4005 | 0.0008 |
| 288.15 | 0.5288 | 0.0010 |
| 288.15 | 0.5877 | 0.0011 |
| 288.15 | 0.6961 | 0.0013 |
| 288.15 | 0.7937 | 0.0016 |
| 288.15 | 0.9232 | 0.0022 |
| 293.15 | 0.0911 | 0.0006 |
| 293.15 | 0.1761 | 0.0006 |
| 293.15 | 0.3304 | 0.0007 |
| 293.15 | 0.4005 | 0.0008 |
| 293.15 | 0.5288 | 0.0009 |
| 293.15 | 0.5877 | 0.0010 |
| 293.15 | 0.6961 | 0.0012 |
| 293.15 | 0.7937 | 0.0015 |
| 293.15 | 0.9232 | 0.0019 |
| 298.15 | 0.0911 | 0.0005 |
| 298.15 | 0.1761 | 0.0006 |
| 298.15 | 0.3304 | 0.0007 |
| 298.15 | 0.4005 | 0.0007 |
| 298.15 | 0.5288 | 0.0009 |
| 298.15 | 0.5877 | 0.0010 |
| 298.15 | 0.6961 | 0.0011 |
| 298.15 | 0.7937 | 0.0014 |
| 298.15 | 0.9232 | 0.0018 |
| 303.15 | 0.0911 | 0.0005 |
| 303.15 | 0.1761 | 0.0005 |
| 303.15 | 0.3304 | 0.0006 |
| 303.15 | 0.4005 | 0.0007 |
| 303.15 | 0.5288 | 0.0008 |
| 303.15 | 0.5877 | 0.0009 |
| 303.15 | 0.6961 | 0.0010 |
| 303.15 | 0.7937 | 0.0012 |
| 303.15 | 0.9232 | 0.0016 |
| 308.15 | 0.0911 | 0.0005 |
| 308.15 | 0.1761 | 0.0005 |
| 308.15 | 0.3304 | 0.0006 |
| 308.15 | 0.4005 | 0.0006 |
| 308.15 | 0.5288 | 0.0008 |
| 308.15 | 0.5877 | 0.0008 |
| 308.15 | 0.6961 | 0.0010 |
| 308.15 | 0.7937 | 0.0012 |
| 308.15 | 0.9232 | 0.0015 |
| 313.15 | 0.0911 | 0.0004 |
| 313.15 | 0.1761 | 0.0005 |
| 313.15 | 0.3304 | 0.0006 |
| 313.15 | 0.4005 | 0.0006 |
| 313.15 | 0.5288 | 0.0007 |
| 313.15 | 0.5877 | 0.0008 |
| 313.15 | 0.6961 | 0.0009 |
| 313.15 | 0.7937 | 0.0011 |
| 313.15 | 0.9232 | 0.0014 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Cyclohexanone (1) - Liquid | Viscosity, Pa*s - Liquid |
| 288.15 | 0.0911 | 0.0006 |
| 288.15 | 0.1761 | 0.0007 |
| 288.15 | 0.3304 | 0.0008 |
| 288.15 | 0.4005 | 0.0008 |
| 288.15 | 0.5288 | 0.0010 |
| 288.15 | 0.5877 | 0.0011 |
| 288.15 | 0.6961 | 0.0013 |
| 288.15 | 0.7937 | 0.0016 |
| 288.15 | 0.9232 | 0.0022 |
| 293.15 | 0.0911 | 0.0006 |
| 293.15 | 0.1761 | 0.0006 |
| 293.15 | 0.3304 | 0.0007 |
| 293.15 | 0.4005 | 0.0008 |
| 293.15 | 0.5288 | 0.0009 |
| 293.15 | 0.5877 | 0.0010 |
| 293.15 | 0.6961 | 0.0012 |
| 293.15 | 0.7937 | 0.0015 |
| 293.15 | 0.9232 | 0.0019 |
| 298.15 | 0.0911 | 0.0005 |
| 298.15 | 0.1761 | 0.0006 |
| 298.15 | 0.3304 | 0.0007 |
| 298.15 | 0.4005 | 0.0007 |
| 298.15 | 0.5288 | 0.0009 |
| 298.15 | 0.5877 | 0.0010 |
| 298.15 | 0.6961 | 0.0011 |
| 298.15 | 0.7937 | 0.0014 |
| 298.15 | 0.9232 | 0.0018 |
| 303.15 | 0.0911 | 0.0005 |
| 303.15 | 0.1761 | 0.0005 |
| 303.15 | 0.3304 | 0.0006 |
| 303.15 | 0.4005 | 0.0007 |
| 303.15 | 0.5288 | 0.0008 |
| 303.15 | 0.5877 | 0.0009 |
| 303.15 | 0.6961 | 0.0010 |
| 303.15 | 0.7937 | 0.0012 |
| 303.15 | 0.9232 | 0.0016 |
| 308.15 | 0.0911 | 0.0005 |
| 308.15 | 0.1761 | 0.0005 |
| 308.15 | 0.3304 | 0.0006 |
| 308.15 | 0.4005 | 0.0006 |
| 308.15 | 0.5288 | 0.0008 |
| 308.15 | 0.5877 | 0.0008 |
| 308.15 | 0.6961 | 0.0010 |
| 308.15 | 0.7937 | 0.0012 |
| 308.15 | 0.9232 | 0.0015 |
| 313.15 | 0.0911 | 0.0004 |
| 313.15 | 0.1761 | 0.0005 |
| 313.15 | 0.3304 | 0.0006 |
| 313.15 | 0.4005 | 0.0006 |
| 313.15 | 0.5288 | 0.0007 |
| 313.15 | 0.5877 | 0.0008 |
| 313.15 | 0.6961 | 0.0009 |
| 313.15 | 0.7937 | 0.0011 |
| 313.15 | 0.9232 | 0.0014 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Cyclohexanone (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0911 | 714.5 |
| 288.15 | 0.1761 | 732.3 |
| 288.15 | 0.3304 | 760.9 |
| 288.15 | 0.4005 | 776.4 |
| 288.15 | 0.5288 | 805.6 |
| 288.15 | 0.5877 | 822.2 |
| 288.15 | 0.6961 | 850.8 |
| 288.15 | 0.7937 | 885.7 |
| 288.15 | 0.9232 | 925.4 |
| 293.15 | 0.0911 | 710.7 |
| 293.15 | 0.1761 | 726.5 |
| 293.15 | 0.3304 | 755.8 |
| 293.15 | 0.4005 | 772.2 |
| 293.15 | 0.5288 | 801.3 |
| 293.15 | 0.5877 | 817.8 |
| 293.15 | 0.6961 | 846.6 |
| 293.15 | 0.7937 | 881.7 |
| 293.15 | 0.9232 | 920.6 |
| 298.15 | 0.0911 | 706.4 |
| 298.15 | 0.1761 | 724.4 |
| 298.15 | 0.3304 | 750.9 |
| 298.15 | 0.4005 | 768.1 |
| 298.15 | 0.5288 | 797.2 |
| 298.15 | 0.5877 | 813.5 |
| 298.15 | 0.6961 | 842.0 |
| 298.15 | 0.7937 | 877.0 |
| 298.15 | 0.9232 | 916.3 |
| 303.15 | 0.0911 | 702.6 |
| 303.15 | 0.1761 | 719.9 |
| 303.15 | 0.3304 | 748.5 |
| 303.15 | 0.4005 | 766.9 |
| 303.15 | 0.5288 | 793.2 |
| 303.15 | 0.5877 | 809.6 |
| 303.15 | 0.6961 | 838.3 |
| 303.15 | 0.7937 | 873.2 |
| 303.15 | 0.9232 | 912.5 |
| 308.15 | 0.0911 | 697.8 |
| 308.15 | 0.1761 | 716.6 |
| 308.15 | 0.3304 | 743.9 |
| 308.15 | 0.4005 | 760.8 |
| 308.15 | 0.5288 | 788.7 |
| 308.15 | 0.5877 | 805.3 |
| 308.15 | 0.6961 | 834.0 |
| 308.15 | 0.7937 | 869.0 |
| 308.15 | 0.9232 | 908.0 |
| 313.15 | 0.0911 | 693.1 |
| 313.15 | 0.1761 | 711.7 |
| 313.15 | 0.3304 | 739.3 |
| 313.15 | 0.4005 | 754.8 |
| 313.15 | 0.5288 | 785.0 |
| 313.15 | 0.5877 | 801.2 |
| 313.15 | 0.6961 | 830.3 |
| 313.15 | 0.7937 | 865.7 |
| 313.15 | 0.9232 | 904.0 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Cyclohexanone (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0911 | 714.5 |
| 288.15 | 0.1761 | 732.3 |
| 288.15 | 0.3304 | 760.9 |
| 288.15 | 0.4005 | 776.4 |
| 288.15 | 0.5288 | 805.6 |
| 288.15 | 0.5877 | 822.2 |
| 288.15 | 0.6961 | 850.8 |
| 288.15 | 0.7937 | 885.7 |
| 288.15 | 0.9232 | 925.4 |
| 293.15 | 0.0911 | 710.7 |
| 293.15 | 0.1761 | 726.5 |
| 293.15 | 0.3304 | 755.8 |
| 293.15 | 0.4005 | 772.2 |
| 293.15 | 0.5288 | 801.3 |
| 293.15 | 0.5877 | 817.8 |
| 293.15 | 0.6961 | 846.6 |
| 293.15 | 0.7937 | 881.7 |
| 293.15 | 0.9232 | 920.6 |
| 298.15 | 0.0911 | 706.4 |
| 298.15 | 0.1761 | 724.4 |
| 298.15 | 0.3304 | 750.9 |
| 298.15 | 0.4005 | 768.1 |
| 298.15 | 0.5288 | 797.2 |
| 298.15 | 0.5877 | 813.5 |
| 298.15 | 0.6961 | 842.0 |
| 298.15 | 0.7937 | 877.0 |
| 298.15 | 0.9232 | 916.3 |
| 303.15 | 0.0911 | 702.6 |
| 303.15 | 0.1761 | 719.9 |
| 303.15 | 0.3304 | 748.5 |
| 303.15 | 0.4005 | 766.9 |
| 303.15 | 0.5288 | 793.2 |
| 303.15 | 0.5877 | 809.6 |
| 303.15 | 0.6961 | 838.3 |
| 303.15 | 0.7937 | 873.2 |
| 303.15 | 0.9232 | 912.5 |
| 308.15 | 0.0911 | 697.8 |
| 308.15 | 0.1761 | 716.6 |
| 308.15 | 0.3304 | 743.9 |
| 308.15 | 0.4005 | 760.8 |
| 308.15 | 0.5288 | 788.7 |
| 308.15 | 0.5877 | 805.3 |
| 308.15 | 0.6961 | 834.0 |
| 308.15 | 0.7937 | 869.0 |
| 308.15 | 0.9232 | 908.0 |
| 313.15 | 0.0911 | 693.1 |
| 313.15 | 0.1761 | 711.7 |
| 313.15 | 0.3304 | 739.3 |
| 313.15 | 0.4005 | 754.8 |
| 313.15 | 0.5288 | 785.0 |
| 313.15 | 0.5877 | 801.2 |
| 313.15 | 0.6961 | 830.3 |
| 313.15 | 0.7937 | 865.7 |
| 313.15 | 0.9232 | 904.0 |