Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Phenol (2) - Liquid mixture 1 |
|---|---|
| 313.15 | 0.0230 |
| 333.15 | 0.0338 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 | Mole fraction of Phenol (2) - Liquid mixture 2 |
|---|---|
| 313.15 | 0.3478 |
| 333.15 | 0.2659 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Heptane (1) - Liquid mixture 1 |
|---|---|
| 313.15 | 0.9520 |
| 333.15 | 0.9249 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 | Mole fraction of Heptane (1) - Liquid mixture 2 |
|---|---|
| 313.15 | 0.0101 |
| 333.15 | 0.0082 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid mixture 1 | Mole fraction of Heptane (1) - Liquid mixture 1 | Mole fraction of Phenol (2) - Liquid mixture 1 |
| 313.15 | 0.0000 | 0.2755 |
| 313.15 | 0.0309 | 0.4104 |
| 313.15 | 0.0376 | 0.4700 |
| 313.15 | 0.0467 | 0.5309 |
| 313.15 | 0.0606 | 0.6200 |
| 313.15 | 0.0697 | 0.6476 |
| 313.15 | 0.0975 | 0.6901 |
| 313.15 | 0.1114 | 0.7281 |
| 313.15 | 0.1140 | 0.7434 |
| 313.15 | 0.1162 | 0.7346 |
| 313.15 | 0.1395 | 0.7773 |
| 313.15 | 0.1587 | 0.7855 |
| 313.15 | 0.1868 | 0.7935 |
| 313.15 | 0.1909 | 0.8091 |
| 313.15 | 0.7915 | 0.2085 |
| 313.15 | 0.8520 | 0.1451 |
| 313.15 | 0.9318 | 0.0615 |
| 313.15 | 0.9606 | 0.0259 |
| 313.15 | 0.0606 | 0.6200 |
| 333.15 | 0.0000 | 0.1932 |
| 333.15 | 0.0191 | 0.3039 |
| 333.15 | 0.0266 | 0.3860 |
| 333.15 | 0.0354 | 0.4443 |
| 333.15 | 0.0516 | 0.5201 |
| 333.15 | 0.0626 | 0.5462 |
| 333.15 | 0.0735 | 0.5753 |
| 333.15 | 0.0844 | 0.5839 |
| 333.15 | 0.0893 | 0.5921 |
| 333.15 | 0.0896 | 0.6165 |
| 333.15 | 0.1090 | 0.6227 |
| 333.15 | 0.1322 | 0.6710 |
| 333.15 | 0.1520 | 0.7064 |
| 333.15 | 0.1913 | 0.7124 |
| 333.15 | 0.2155 | 0.7081 |
| 333.15 | 0.2888 | 0.6726 |
| 333.15 | 0.3445 | 0.6270 |
| 333.15 | 0.3668 | 0.6160 |
| 333.15 | 0.4087 | 0.5756 |
| 333.15 | 0.4643 | 0.5180 |
| 333.15 | 0.4858 | 0.4946 |
| 333.15 | 0.5768 | 0.4056 |
| 333.15 | 0.7514 | 0.2321 |
| 333.15 | 0.7704 | 0.2147 |
| 333.15 | 0.8400 | 0.1422 |
| 333.15 | 0.9206 | 0.0652 |
| 333.15 | 0.0516 | 0.5201 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Phenol (2) - Liquid mixture 1 |
|---|---|
| 313.15 | 0.0230 |
| 333.15 | 0.0338 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 | Mole fraction of Phenol (2) - Liquid mixture 2 |
|---|---|
| 313.15 | 0.3478 |
| 333.15 | 0.2659 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Heptane (1) - Liquid mixture 1 |
|---|---|
| 313.15 | 0.9520 |
| 333.15 | 0.9249 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 | Mole fraction of Heptane (1) - Liquid mixture 2 |
|---|---|
| 313.15 | 0.0101 |
| 333.15 | 0.0082 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid mixture 1 | Mole fraction of Heptane (1) - Liquid mixture 1 | Mole fraction of Phenol (2) - Liquid mixture 1 |
| 313.15 | 0.0000 | 0.2755 |
| 313.15 | 0.0309 | 0.4104 |
| 313.15 | 0.0376 | 0.4700 |
| 313.15 | 0.0467 | 0.5309 |
| 313.15 | 0.0606 | 0.6200 |
| 313.15 | 0.0697 | 0.6476 |
| 313.15 | 0.0975 | 0.6901 |
| 313.15 | 0.1114 | 0.7281 |
| 313.15 | 0.1140 | 0.7434 |
| 313.15 | 0.1162 | 0.7346 |
| 313.15 | 0.1395 | 0.7773 |
| 313.15 | 0.1587 | 0.7855 |
| 313.15 | 0.1868 | 0.7935 |
| 313.15 | 0.1909 | 0.8091 |
| 313.15 | 0.7915 | 0.2085 |
| 313.15 | 0.8520 | 0.1451 |
| 313.15 | 0.9318 | 0.0615 |
| 313.15 | 0.9606 | 0.0259 |
| 313.15 | 0.0606 | 0.6200 |
| 333.15 | 0.0000 | 0.1932 |
| 333.15 | 0.0191 | 0.3039 |
| 333.15 | 0.0266 | 0.3860 |
| 333.15 | 0.0354 | 0.4443 |
| 333.15 | 0.0516 | 0.5201 |
| 333.15 | 0.0626 | 0.5462 |
| 333.15 | 0.0735 | 0.5753 |
| 333.15 | 0.0844 | 0.5839 |
| 333.15 | 0.0893 | 0.5921 |
| 333.15 | 0.0896 | 0.6165 |
| 333.15 | 0.1090 | 0.6227 |
| 333.15 | 0.1322 | 0.6710 |
| 333.15 | 0.1520 | 0.7064 |
| 333.15 | 0.1913 | 0.7124 |
| 333.15 | 0.2155 | 0.7081 |
| 333.15 | 0.2888 | 0.6726 |
| 333.15 | 0.3445 | 0.6270 |
| 333.15 | 0.3668 | 0.6160 |
| 333.15 | 0.4087 | 0.5756 |
| 333.15 | 0.4643 | 0.5180 |
| 333.15 | 0.4858 | 0.4946 |
| 333.15 | 0.5768 | 0.4056 |
| 333.15 | 0.7514 | 0.2321 |
| 333.15 | 0.7704 | 0.2147 |
| 333.15 | 0.8400 | 0.1422 |
| 333.15 | 0.9206 | 0.0652 |
| 333.15 | 0.0516 | 0.5201 |