Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Phenol, 3-methyl- (1) - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
| 0.0000 | 308.15 | 0.0005 |
| 0.0000 | 313.15 | 0.0004 |
| 0.0000 | 318.15 | 0.0004 |
| 0.0000 | 323.15 | 0.0004 |
| 0.0000 | 328.15 | 0.0004 |
| 0.0999 | 308.15 | 0.0007 |
| 0.0999 | 313.15 | 0.0007 |
| 0.0999 | 318.15 | 0.0006 |
| 0.0999 | 323.15 | 0.0006 |
| 0.0999 | 328.15 | 0.0005 |
| 0.1999 | 308.15 | 0.0010 |
| 0.1999 | 313.15 | 0.0009 |
| 0.1999 | 318.15 | 0.0008 |
| 0.1999 | 323.15 | 0.0008 |
| 0.1999 | 328.15 | 0.0007 |
| 0.2998 | 308.15 | 0.0013 |
| 0.2998 | 313.15 | 0.0012 |
| 0.2998 | 318.15 | 0.0011 |
| 0.2998 | 323.15 | 0.0010 |
| 0.2998 | 328.15 | 0.0009 |
| 0.3999 | 308.15 | 0.0018 |
| 0.3999 | 313.15 | 0.0016 |
| 0.3999 | 318.15 | 0.0014 |
| 0.3999 | 323.15 | 0.0013 |
| 0.3999 | 328.15 | 0.0012 |
| 0.4998 | 308.15 | 0.0024 |
| 0.4998 | 313.15 | 0.0021 |
| 0.4998 | 318.15 | 0.0018 |
| 0.4998 | 323.15 | 0.0016 |
| 0.4998 | 328.15 | 0.0015 |
| 0.6001 | 308.15 | 0.0030 |
| 0.6001 | 313.15 | 0.0026 |
| 0.6001 | 318.15 | 0.0022 |
| 0.6001 | 323.15 | 0.0020 |
| 0.6001 | 328.15 | 0.0018 |
| 0.6998 | 308.15 | 0.0038 |
| 0.6998 | 313.15 | 0.0032 |
| 0.6998 | 318.15 | 0.0028 |
| 0.6998 | 323.15 | 0.0024 |
| 0.6998 | 328.15 | 0.0021 |
| 0.7999 | 308.15 | 0.0048 |
| 0.7999 | 313.15 | 0.0040 |
| 0.7999 | 318.15 | 0.0034 |
| 0.7999 | 323.15 | 0.0029 |
| 0.7999 | 328.15 | 0.0026 |
| 0.8999 | 308.15 | 0.0061 |
| 0.8999 | 313.15 | 0.0050 |
| 0.8999 | 318.15 | 0.0042 |
| 0.8999 | 323.15 | 0.0035 |
| 0.8999 | 328.15 | 0.0030 |
| 1.0000 | 308.15 | 0.0077 |
| 1.0000 | 313.15 | 0.0061 |
| 1.0000 | 318.15 | 0.0050 |
| 1.0000 | 323.15 | 0.0042 |
| 1.0000 | 328.15 | 0.0035 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Phenol, 3-methyl- (1) - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
| 0.0000 | 308.15 | 0.0005 |
| 0.0000 | 313.15 | 0.0004 |
| 0.0000 | 318.15 | 0.0004 |
| 0.0000 | 323.15 | 0.0004 |
| 0.0000 | 328.15 | 0.0004 |
| 0.0999 | 308.15 | 0.0007 |
| 0.0999 | 313.15 | 0.0007 |
| 0.0999 | 318.15 | 0.0006 |
| 0.0999 | 323.15 | 0.0006 |
| 0.0999 | 328.15 | 0.0005 |
| 0.1999 | 308.15 | 0.0010 |
| 0.1999 | 313.15 | 0.0009 |
| 0.1999 | 318.15 | 0.0008 |
| 0.1999 | 323.15 | 0.0008 |
| 0.1999 | 328.15 | 0.0007 |
| 0.2998 | 308.15 | 0.0013 |
| 0.2998 | 313.15 | 0.0012 |
| 0.2998 | 318.15 | 0.0011 |
| 0.2998 | 323.15 | 0.0010 |
| 0.2998 | 328.15 | 0.0009 |
| 0.3999 | 308.15 | 0.0018 |
| 0.3999 | 313.15 | 0.0016 |
| 0.3999 | 318.15 | 0.0014 |
| 0.3999 | 323.15 | 0.0013 |
| 0.3999 | 328.15 | 0.0012 |
| 0.4998 | 308.15 | 0.0024 |
| 0.4998 | 313.15 | 0.0021 |
| 0.4998 | 318.15 | 0.0018 |
| 0.4998 | 323.15 | 0.0016 |
| 0.4998 | 328.15 | 0.0015 |
| 0.6001 | 308.15 | 0.0030 |
| 0.6001 | 313.15 | 0.0026 |
| 0.6001 | 318.15 | 0.0022 |
| 0.6001 | 323.15 | 0.0020 |
| 0.6001 | 328.15 | 0.0018 |
| 0.6998 | 308.15 | 0.0038 |
| 0.6998 | 313.15 | 0.0032 |
| 0.6998 | 318.15 | 0.0028 |
| 0.6998 | 323.15 | 0.0024 |
| 0.6998 | 328.15 | 0.0021 |
| 0.7999 | 308.15 | 0.0048 |
| 0.7999 | 313.15 | 0.0040 |
| 0.7999 | 318.15 | 0.0034 |
| 0.7999 | 323.15 | 0.0029 |
| 0.7999 | 328.15 | 0.0026 |
| 0.8999 | 308.15 | 0.0061 |
| 0.8999 | 313.15 | 0.0050 |
| 0.8999 | 318.15 | 0.0042 |
| 0.8999 | 323.15 | 0.0035 |
| 0.8999 | 328.15 | 0.0030 |
| 1.0000 | 308.15 | 0.0077 |
| 1.0000 | 313.15 | 0.0061 |
| 1.0000 | 318.15 | 0.0050 |
| 1.0000 | 323.15 | 0.0042 |
| 1.0000 | 328.15 | 0.0035 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Phenol, 3-methyl- (1) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 0.0000 | 308.15 | 776.92 |
| 0.0000 | 313.15 | 772.13 |
| 0.0000 | 318.15 | 767.31 |
| 0.0000 | 323.15 | 762.46 |
| 0.0000 | 328.15 | 757.85 |
| 0.0999 | 308.15 | 838.66 |
| 0.0999 | 313.15 | 834.09 |
| 0.0999 | 318.15 | 829.48 |
| 0.0999 | 323.15 | 824.84 |
| 0.0999 | 328.15 | 820.44 |
| 0.1999 | 308.15 | 880.62 |
| 0.1999 | 313.15 | 876.22 |
| 0.1999 | 318.15 | 871.78 |
| 0.1999 | 323.15 | 867.32 |
| 0.1999 | 328.15 | 863.14 |
| 0.2998 | 308.15 | 914.11 |
| 0.2998 | 313.15 | 909.92 |
| 0.2998 | 318.15 | 905.55 |
| 0.2998 | 323.15 | 901.14 |
| 0.2998 | 328.15 | 897.17 |
| 0.3999 | 308.15 | 939.8 |
| 0.3999 | 313.15 | 935.58 |
| 0.3999 | 318.15 | 931.38 |
| 0.3999 | 323.15 | 927.14 |
| 0.3999 | 328.15 | 923.28 |
| 0.4998 | 308.15 | 960.97 |
| 0.4998 | 313.15 | 956.82 |
| 0.4998 | 318.15 | 952.74 |
| 0.4998 | 323.15 | 948.57 |
| 0.4998 | 328.15 | 944.75 |
| 0.6001 | 308.15 | 977.35 |
| 0.6001 | 313.15 | 973.31 |
| 0.6001 | 318.15 | 969.31 |
| 0.6001 | 323.15 | 965.28 |
| 0.6001 | 328.15 | 961.59 |
| 0.6998 | 308.15 | 991.84 |
| 0.6998 | 313.15 | 987.87 |
| 0.6998 | 318.15 | 983.92 |
| 0.6998 | 323.15 | 979.59 |
| 0.6998 | 328.15 | 976.07 |
| 0.7999 | 308.15 | 1002.99 |
| 0.7999 | 313.15 | 998.97 |
| 0.7999 | 318.15 | 994.93 |
| 0.7999 | 323.15 | 990.88 |
| 0.7999 | 328.15 | 987.18 |
| 0.8999 | 308.15 | 1013.19 |
| 0.8999 | 313.15 | 1009.18 |
| 0.8999 | 318.15 | 1005.13 |
| 0.8999 | 323.15 | 1001.1 |
| 0.8999 | 328.15 | 997.41 |
| 1.0000 | 308.15 | 1021.64 |
| 1.0000 | 313.15 | 1017.63 |
| 1.0000 | 318.15 | 1013.6 |
| 1.0000 | 323.15 | 1009.56 |
| 1.0000 | 328.15 | 1005.93 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Phenol, 3-methyl- (1) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 0.0000 | 308.15 | 776.92 |
| 0.0000 | 313.15 | 772.13 |
| 0.0000 | 318.15 | 767.31 |
| 0.0000 | 323.15 | 762.46 |
| 0.0000 | 328.15 | 757.85 |
| 0.0999 | 308.15 | 838.66 |
| 0.0999 | 313.15 | 834.09 |
| 0.0999 | 318.15 | 829.48 |
| 0.0999 | 323.15 | 824.84 |
| 0.0999 | 328.15 | 820.44 |
| 0.1999 | 308.15 | 880.62 |
| 0.1999 | 313.15 | 876.22 |
| 0.1999 | 318.15 | 871.78 |
| 0.1999 | 323.15 | 867.32 |
| 0.1999 | 328.15 | 863.14 |
| 0.2998 | 308.15 | 914.11 |
| 0.2998 | 313.15 | 909.92 |
| 0.2998 | 318.15 | 905.55 |
| 0.2998 | 323.15 | 901.14 |
| 0.2998 | 328.15 | 897.17 |
| 0.3999 | 308.15 | 939.8 |
| 0.3999 | 313.15 | 935.58 |
| 0.3999 | 318.15 | 931.38 |
| 0.3999 | 323.15 | 927.14 |
| 0.3999 | 328.15 | 923.28 |
| 0.4998 | 308.15 | 960.97 |
| 0.4998 | 313.15 | 956.82 |
| 0.4998 | 318.15 | 952.74 |
| 0.4998 | 323.15 | 948.57 |
| 0.4998 | 328.15 | 944.75 |
| 0.6001 | 308.15 | 977.35 |
| 0.6001 | 313.15 | 973.31 |
| 0.6001 | 318.15 | 969.31 |
| 0.6001 | 323.15 | 965.28 |
| 0.6001 | 328.15 | 961.59 |
| 0.6998 | 308.15 | 991.84 |
| 0.6998 | 313.15 | 987.87 |
| 0.6998 | 318.15 | 983.92 |
| 0.6998 | 323.15 | 979.59 |
| 0.6998 | 328.15 | 976.07 |
| 0.7999 | 308.15 | 1002.99 |
| 0.7999 | 313.15 | 998.97 |
| 0.7999 | 318.15 | 994.93 |
| 0.7999 | 323.15 | 990.88 |
| 0.7999 | 328.15 | 987.18 |
| 0.8999 | 308.15 | 1013.19 |
| 0.8999 | 313.15 | 1009.18 |
| 0.8999 | 318.15 | 1005.13 |
| 0.8999 | 323.15 | 1001.1 |
| 0.8999 | 328.15 | 997.41 |
| 1.0000 | 308.15 | 1021.64 |
| 1.0000 | 313.15 | 1017.63 |
| 1.0000 | 318.15 | 1013.6 |
| 1.0000 | 323.15 | 1009.56 |
| 1.0000 | 328.15 | 1005.93 |
Operational condition: Pressure, kPa = 95.5 (Liquid)
| Mole fraction of Methyl Alcohol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 473.75 |
| 0.0864 | 458.05 |
| 0.1765 | 437.05 |
| 0.2343 | 423.65 |
| 0.3002 | 409.45 |
| 0.3808 | 394.35 |
| 0.4616 | 381.65 |
| 0.5911 | 365.25 |
| 0.7208 | 352.75 |
| 0.7605 | 349.55 |
| 0.8377 | 343.55 |
| 0.8887 | 340.95 |
| 0.9393 | 338.35 |
| 1.0000 | 336.25 |
Operational condition: Pressure, kPa = 95.5 (Liquid)
| Mole fraction of Methyl Alcohol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 473.75 |
| 0.0864 | 458.05 |
| 0.1765 | 437.05 |
| 0.2343 | 423.65 |
| 0.3002 | 409.45 |
| 0.3808 | 394.35 |
| 0.4616 | 381.65 |
| 0.5911 | 365.25 |
| 0.7208 | 352.75 |
| 0.7605 | 349.55 |
| 0.8377 | 343.55 |
| 0.8887 | 340.95 |
| 0.9393 | 338.35 |
| 1.0000 | 336.25 |