Operational conditions:
| Temperature, K - Liquid | Activity coefficient of Toluene (1) - Liquid |
|---|---|
| 333.15 | 3.457 |
| 343.15 | 3.382 |
| 353.15 | 3.291 |
| 363.15 | 3.228 |
| 373.15 | 3.197 |
Operational conditions:
| Temperature, K - Liquid | Activity coefficient of Toluene (1) - Liquid |
|---|---|
| 333.15 | 3.457 |
| 343.15 | 3.382 |
| 353.15 | 3.291 |
| 363.15 | 3.228 |
| 373.15 | 3.197 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of Toluene (1) - Liquid | Mole fraction of Toluene (1) - Gas |
|---|---|
| 0.1474 | 0.9884 |
| 0.2409 | 0.9969 |
| 0.3136 | 0.9975 |
| 0.3725 | 0.9983 |
| 0.5039 | 0.9987 |
| 0.5705 | 0.9989 |
| 0.8246 | 0.9994 |
| 0.8791 | 0.9995 |
| 0.9384 | 0.9996 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of Toluene (1) - Liquid | Mole fraction of Toluene (1) - Gas |
|---|---|
| 0.1474 | 0.9884 |
| 0.2409 | 0.9969 |
| 0.3136 | 0.9975 |
| 0.3725 | 0.9983 |
| 0.5039 | 0.9987 |
| 0.5705 | 0.9989 |
| 0.8246 | 0.9994 |
| 0.8791 | 0.9995 |
| 0.9384 | 0.9996 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Toluene (1) - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 0.0000 | 0.0101 |
| 303.15 | 0.1267 | 0.0061 |
| 303.15 | 0.2458 | 0.0040 |
| 303.15 | 0.3587 | 0.0027 |
| 303.15 | 0.4651 | 0.0020 |
| 303.15 | 0.5662 | 0.0016 |
| 303.15 | 0.6617 | 0.0012 |
| 303.15 | 0.7527 | 0.0009 |
| 303.15 | 0.8392 | 0.0008 |
| 303.15 | 0.9206 | 0.0006 |
| 303.15 | 1.0000 | 0.0005 |
| 323.15 | 0.0000 | 0.0062 |
| 323.15 | 0.1267 | 0.0039 |
| 323.15 | 0.2458 | 0.0027 |
| 323.15 | 0.3587 | 0.0019 |
| 323.15 | 0.4651 | 0.0015 |
| 323.15 | 0.5662 | 0.0012 |
| 323.15 | 0.6617 | 0.0009 |
| 323.15 | 0.7527 | 0.0007 |
| 323.15 | 0.8392 | 0.0006 |
| 323.15 | 0.9206 | 0.0005 |
| 323.15 | 1.0000 | 0.0004 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Toluene (1) - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 0.0000 | 0.0101 |
| 303.15 | 0.1267 | 0.0061 |
| 303.15 | 0.2458 | 0.0040 |
| 303.15 | 0.3587 | 0.0027 |
| 303.15 | 0.4651 | 0.0020 |
| 303.15 | 0.5662 | 0.0016 |
| 303.15 | 0.6617 | 0.0012 |
| 303.15 | 0.7527 | 0.0009 |
| 303.15 | 0.8392 | 0.0008 |
| 303.15 | 0.9206 | 0.0006 |
| 303.15 | 1.0000 | 0.0005 |
| 323.15 | 0.0000 | 0.0062 |
| 323.15 | 0.1267 | 0.0039 |
| 323.15 | 0.2458 | 0.0027 |
| 323.15 | 0.3587 | 0.0019 |
| 323.15 | 0.4651 | 0.0015 |
| 323.15 | 0.5662 | 0.0012 |
| 323.15 | 0.6617 | 0.0009 |
| 323.15 | 0.7527 | 0.0007 |
| 323.15 | 0.8392 | 0.0006 |
| 323.15 | 0.9206 | 0.0005 |
| 323.15 | 1.0000 | 0.0004 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Toluene (1) - Liquid | Mass density, kg/m3 - Liquid |
| 303.15 | 0.0000 | 1260.8 |
| 303.15 | 0.1267 | 1209.84 |
| 303.15 | 0.2458 | 1161.72 |
| 303.15 | 0.3587 | 1115.78 |
| 303.15 | 0.4651 | 1072.79 |
| 303.15 | 0.5662 | 1031.84 |
| 303.15 | 0.6617 | 994.05 |
| 303.15 | 0.7527 | 957.36 |
| 303.15 | 0.8392 | 922.76 |
| 303.15 | 0.9206 | 890.24 |
| 303.15 | 1.0000 | 858.32 |
| 323.15 | 0.0000 | 1243.36 |
| 323.15 | 0.1267 | 1191.98 |
| 323.15 | 0.2458 | 1143.65 |
| 323.15 | 0.3587 | 1097.6 |
| 323.15 | 0.4651 | 1054.45 |
| 323.15 | 0.5662 | 1013.37 |
| 323.15 | 0.6617 | 975.51 |
| 323.15 | 0.7527 | 938.7 |
| 323.15 | 0.8392 | 903.99 |
| 323.15 | 0.9206 | 871.46 |
| 323.15 | 1.0000 | 839.45 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Toluene (1) - Liquid | Mass density, kg/m3 - Liquid |
| 303.15 | 0.0000 | 1260.8 |
| 303.15 | 0.1267 | 1209.84 |
| 303.15 | 0.2458 | 1161.72 |
| 303.15 | 0.3587 | 1115.78 |
| 303.15 | 0.4651 | 1072.79 |
| 303.15 | 0.5662 | 1031.84 |
| 303.15 | 0.6617 | 994.05 |
| 303.15 | 0.7527 | 957.36 |
| 303.15 | 0.8392 | 922.76 |
| 303.15 | 0.9206 | 890.24 |
| 303.15 | 1.0000 | 858.32 |
| 323.15 | 0.0000 | 1243.36 |
| 323.15 | 0.1267 | 1191.98 |
| 323.15 | 0.2458 | 1143.65 |
| 323.15 | 0.3587 | 1097.6 |
| 323.15 | 0.4651 | 1054.45 |
| 323.15 | 0.5662 | 1013.37 |
| 323.15 | 0.6617 | 975.51 |
| 323.15 | 0.7527 | 938.7 |
| 323.15 | 0.8392 | 903.99 |
| 323.15 | 0.9206 | 871.46 |
| 323.15 | 1.0000 | 839.45 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of Toluene (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.1474 | 420.16 |
| 0.2409 | 401.27 |
| 0.3136 | 395.63 |
| 0.3725 | 392.47 |
| 0.5039 | 390.35 |
| 0.5705 | 389.40 |
| 0.8246 | 388.04 |
| 0.8791 | 386.65 |
| 0.9384 | 385.62 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of Toluene (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.1474 | 420.16 |
| 0.2409 | 401.27 |
| 0.3136 | 395.63 |
| 0.3725 | 392.47 |
| 0.5039 | 390.35 |
| 0.5705 | 389.40 |
| 0.8246 | 388.04 |
| 0.8791 | 386.65 |
| 0.9384 | 385.62 |