Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Methane, nitro- (2) - Liquid mixture 1 |
|---|---|
| 263.05 | 0.3113 |
| 268.70 | 0.3484 |
| 272.88 | 0.3742 |
| 278.04 | 0.4194 |
| 281.72 | 0.4595 |
| 283.91 | 0.4857 |
| 287.12 | 0.5334 |
| 289.13 | 0.5732 |
| 290.47 | 0.6132 |
| 291.33 | 0.6530 |
| 291.82 | 0.6979 |
| 291.84 | 0.7491 |
| 291.68 | 0.8008 |
| 290.52 | 0.8480 |
| 288.46 | 0.8787 |
| 286.63 | 0.8931 |
| 284.28 | 0.9064 |
| 281.74 | 0.9177 |
| 278.25 | 0.9293 |
| 275.17 | 0.9379 |
| 268.63 | 0.9511 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Methane, nitro- (2) - Liquid mixture 1 |
|---|---|
| 263.05 | 0.3113 |
| 268.70 | 0.3484 |
| 272.88 | 0.3742 |
| 278.04 | 0.4194 |
| 281.72 | 0.4595 |
| 283.91 | 0.4857 |
| 287.12 | 0.5334 |
| 289.13 | 0.5732 |
| 290.47 | 0.6132 |
| 291.33 | 0.6530 |
| 291.82 | 0.6979 |
| 291.84 | 0.7491 |
| 291.68 | 0.8008 |
| 290.52 | 0.8480 |
| 288.46 | 0.8787 |
| 286.63 | 0.8931 |
| 284.28 | 0.9064 |
| 281.74 | 0.9177 |
| 278.25 | 0.9293 |
| 275.17 | 0.9379 |
| 268.63 | 0.9511 |