Operational conditions:
| Mole fraction of Methylene chloride (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0709 | -0.4240 |
| 0.1387 | -0.7880 |
| 0.2037 | -1.108 |
| 0.2659 | -1.374 |
| 0.3257 | -1.587 |
| 0.3831 | -1.722 |
| 0.4383 | -1.834 |
| 0.4914 | -1.898 |
| 0.5425 | -1.916 |
| 0.5917 | -1.907 |
| 0.6391 | -1.842 |
| 0.6849 | -1.745 |
| 0.7291 | -1.614 |
| 0.7718 | -1.456 |
| 0.8130 | -1.267 |
| 0.8529 | -1.055 |
| 0.8914 | -0.8150 |
| 0.9288 | -0.5540 |
| 0.9650 | -0.2850 |
Operational conditions:
| Mole fraction of Methylene chloride (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0709 | -0.4240 |
| 0.1387 | -0.7880 |
| 0.2037 | -1.108 |
| 0.2659 | -1.374 |
| 0.3257 | -1.587 |
| 0.3831 | -1.722 |
| 0.4383 | -1.834 |
| 0.4914 | -1.898 |
| 0.5425 | -1.916 |
| 0.5917 | -1.907 |
| 0.6391 | -1.842 |
| 0.6849 | -1.745 |
| 0.7291 | -1.614 |
| 0.7718 | -1.456 |
| 0.8130 | -1.267 |
| 0.8529 | -1.055 |
| 0.8914 | -0.8150 |
| 0.9288 | -0.5540 |
| 0.9650 | -0.2850 |
Operational condition: Temperature, K = 333.15 (Liquid)
| Mole fraction of Methylene chloride (1) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
|---|---|
| 0.0000 | 2.23 |
| 0.0048 | 2.54 |
| 0.0092 | 2.90 |
| 0.0136 | 3.24 |
| 0.0237 | 3.98 |
| 0.0450 | 5.58 |
| 0.0931 | 9.47 |
| 0.1465 | 14.41 |
| 0.2120 | 21.50 |
| 0.2863 | 30.96 |
| 0.3693 | 43.78 |
| 0.4510 | 58.86 |
| 0.5265 | 74.94 |
| 0.5956 | 91.59 |
| 0.6539 | 106.79 |
| 0.7050 | 120.63 |
| 0.7669 | 138.11 |
| 0.8226 | 153.67 |
| 0.8917 | 172.73 |
| 0.9305 | 182.64 |
| 0.9596 | 189.62 |
| 0.9834 | 194.77 |
| 0.9933 | 196.66 |
| 0.9981 | 197.69 |
| 1.0000 | 197.94 |
Operational condition: Temperature, K = 333.15 (Liquid)
| Mole fraction of Methylene chloride (1) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
|---|---|
| 0.0000 | 2.23 |
| 0.0048 | 2.54 |
| 0.0092 | 2.90 |
| 0.0136 | 3.24 |
| 0.0237 | 3.98 |
| 0.0450 | 5.58 |
| 0.0931 | 9.47 |
| 0.1465 | 14.41 |
| 0.2120 | 21.50 |
| 0.2863 | 30.96 |
| 0.3693 | 43.78 |
| 0.4510 | 58.86 |
| 0.5265 | 74.94 |
| 0.5956 | 91.59 |
| 0.6539 | 106.79 |
| 0.7050 | 120.63 |
| 0.7669 | 138.11 |
| 0.8226 | 153.67 |
| 0.8917 | 172.73 |
| 0.9305 | 182.64 |
| 0.9596 | 189.62 |
| 0.9834 | 194.77 |
| 0.9933 | 196.66 |
| 0.9981 | 197.69 |
| 1.0000 | 197.94 |