Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Cyclohexane, methyl- (2) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.1014 | 0.0006 |
| 293.15 | 0.1535 | 0.0006 |
| 293.15 | 0.2607 | 0.0006 |
| 293.15 | 0.3720 | 0.0006 |
| 293.15 | 0.4293 | 0.0007 |
| 293.15 | 0.5473 | 0.0007 |
| 293.15 | 0.6080 | 0.0007 |
| 293.15 | 0.7979 | 0.0007 |
| 293.15 | 0.8639 | 0.0007 |
| 298.15 | 0.1014 | 0.0006 |
| 298.15 | 0.1535 | 0.0006 |
| 298.15 | 0.2607 | 0.0006 |
| 298.15 | 0.3720 | 0.0006 |
| 298.15 | 0.4293 | 0.0006 |
| 298.15 | 0.5473 | 0.0006 |
| 298.15 | 0.6080 | 0.0006 |
| 298.15 | 0.7979 | 0.0006 |
| 298.15 | 0.8639 | 0.0007 |
| 303.15 | 0.1014 | 0.0006 |
| 303.15 | 0.1535 | 0.0006 |
| 303.15 | 0.2607 | 0.0006 |
| 303.15 | 0.3720 | 0.0006 |
| 303.15 | 0.4293 | 0.0006 |
| 303.15 | 0.5473 | 0.0006 |
| 303.15 | 0.6080 | 0.0006 |
| 303.15 | 0.7979 | 0.0006 |
| 303.15 | 0.8639 | 0.0006 |
| 308.15 | 0.1014 | 0.0005 |
| 308.15 | 0.1535 | 0.0005 |
| 308.15 | 0.2607 | 0.0005 |
| 308.15 | 0.3720 | 0.0005 |
| 308.15 | 0.4293 | 0.0006 |
| 308.15 | 0.5473 | 0.0006 |
| 308.15 | 0.6080 | 0.0006 |
| 308.15 | 0.7979 | 0.0006 |
| 308.15 | 0.8639 | 0.0006 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Cyclohexane, methyl- (2) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.1014 | 0.0006 |
| 293.15 | 0.1535 | 0.0006 |
| 293.15 | 0.2607 | 0.0006 |
| 293.15 | 0.3720 | 0.0006 |
| 293.15 | 0.4293 | 0.0007 |
| 293.15 | 0.5473 | 0.0007 |
| 293.15 | 0.6080 | 0.0007 |
| 293.15 | 0.7979 | 0.0007 |
| 293.15 | 0.8639 | 0.0007 |
| 298.15 | 0.1014 | 0.0006 |
| 298.15 | 0.1535 | 0.0006 |
| 298.15 | 0.2607 | 0.0006 |
| 298.15 | 0.3720 | 0.0006 |
| 298.15 | 0.4293 | 0.0006 |
| 298.15 | 0.5473 | 0.0006 |
| 298.15 | 0.6080 | 0.0006 |
| 298.15 | 0.7979 | 0.0006 |
| 298.15 | 0.8639 | 0.0007 |
| 303.15 | 0.1014 | 0.0006 |
| 303.15 | 0.1535 | 0.0006 |
| 303.15 | 0.2607 | 0.0006 |
| 303.15 | 0.3720 | 0.0006 |
| 303.15 | 0.4293 | 0.0006 |
| 303.15 | 0.5473 | 0.0006 |
| 303.15 | 0.6080 | 0.0006 |
| 303.15 | 0.7979 | 0.0006 |
| 303.15 | 0.8639 | 0.0006 |
| 308.15 | 0.1014 | 0.0005 |
| 308.15 | 0.1535 | 0.0005 |
| 308.15 | 0.2607 | 0.0005 |
| 308.15 | 0.3720 | 0.0005 |
| 308.15 | 0.4293 | 0.0006 |
| 308.15 | 0.5473 | 0.0006 |
| 308.15 | 0.6080 | 0.0006 |
| 308.15 | 0.7979 | 0.0006 |
| 308.15 | 0.8639 | 0.0006 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Cyclohexane, methyl- (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.1014 | 1218.7 |
| 293.15 | 0.1535 | 1187.3 |
| 293.15 | 0.2607 | 1129.8 |
| 293.15 | 0.3720 | 1071.0 |
| 293.15 | 0.4293 | 1041.0 |
| 293.15 | 0.5473 | 978.8 |
| 293.15 | 0.6080 | 946.5 |
| 293.15 | 0.7979 | 858.3 |
| 293.15 | 0.8639 | 830.0 |
| 298.15 | 0.1014 | 1212.2 |
| 298.15 | 0.1535 | 1180.4 |
| 298.15 | 0.2607 | 1123.0 |
| 298.15 | 0.3720 | 1064.8 |
| 298.15 | 0.4293 | 1035.5 |
| 298.15 | 0.5473 | 973.2 |
| 298.15 | 0.6080 | 941.2 |
| 298.15 | 0.7979 | 853.5 |
| 298.15 | 0.8639 | 825.8 |
| 303.15 | 0.1014 | 1206.3 |
| 303.15 | 0.1535 | 1174.2 |
| 303.15 | 0.2607 | 1118.5 |
| 303.15 | 0.3720 | 1059.4 |
| 303.15 | 0.4293 | 1029.9 |
| 303.15 | 0.5473 | 967.8 |
| 303.15 | 0.6080 | 935.8 |
| 303.15 | 0.7979 | 849.0 |
| 303.15 | 0.8639 | 821.8 |
| 308.15 | 0.1014 | 1198.2 |
| 308.15 | 0.1535 | 1167.5 |
| 308.15 | 0.2607 | 1111.0 |
| 308.15 | 0.3720 | 1053.2 |
| 308.15 | 0.4293 | 1024.4 |
| 308.15 | 0.5473 | 962.5 |
| 308.15 | 0.6080 | 930.7 |
| 308.15 | 0.7979 | 843.8 |
| 308.15 | 0.8639 | 816.5 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Cyclohexane, methyl- (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.1014 | 1218.7 |
| 293.15 | 0.1535 | 1187.3 |
| 293.15 | 0.2607 | 1129.8 |
| 293.15 | 0.3720 | 1071.0 |
| 293.15 | 0.4293 | 1041.0 |
| 293.15 | 0.5473 | 978.8 |
| 293.15 | 0.6080 | 946.5 |
| 293.15 | 0.7979 | 858.3 |
| 293.15 | 0.8639 | 830.0 |
| 298.15 | 0.1014 | 1212.2 |
| 298.15 | 0.1535 | 1180.4 |
| 298.15 | 0.2607 | 1123.0 |
| 298.15 | 0.3720 | 1064.8 |
| 298.15 | 0.4293 | 1035.5 |
| 298.15 | 0.5473 | 973.2 |
| 298.15 | 0.6080 | 941.2 |
| 298.15 | 0.7979 | 853.5 |
| 298.15 | 0.8639 | 825.8 |
| 303.15 | 0.1014 | 1206.3 |
| 303.15 | 0.1535 | 1174.2 |
| 303.15 | 0.2607 | 1118.5 |
| 303.15 | 0.3720 | 1059.4 |
| 303.15 | 0.4293 | 1029.9 |
| 303.15 | 0.5473 | 967.8 |
| 303.15 | 0.6080 | 935.8 |
| 303.15 | 0.7979 | 849.0 |
| 303.15 | 0.8639 | 821.8 |
| 308.15 | 0.1014 | 1198.2 |
| 308.15 | 0.1535 | 1167.5 |
| 308.15 | 0.2607 | 1111.0 |
| 308.15 | 0.3720 | 1053.2 |
| 308.15 | 0.4293 | 1024.4 |
| 308.15 | 0.5473 | 962.5 |
| 308.15 | 0.6080 | 930.7 |
| 308.15 | 0.7979 | 843.8 |
| 308.15 | 0.8639 | 816.5 |