Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Methane, nitro- (2) - Liquid mixture 1 |
|---|---|
| 279.36 | 0.2957 |
| 284.38 | 0.3188 |
| 285.24 | 0.3238 |
| 289.71 | 0.3568 |
| 293.47 | 0.3899 |
| 296.69 | 0.4220 |
| 299.58 | 0.4575 |
| 302.58 | 0.5007 |
| 304.95 | 0.5458 |
| 306.23 | 0.5836 |
| 307.09 | 0.6160 |
| 307.74 | 0.6553 |
| 307.99 | 0.6998 |
| 308.00 | 0.7502 |
| 307.78 | 0.7925 |
| 306.45 | 0.8378 |
| 303.60 | 0.8709 |
| 303.74 | 0.8715 |
| 301.25 | 0.8875 |
| 299.13 | 0.8994 |
| 296.63 | 0.9117 |
| 294.57 | 0.9200 |
| 290.01 | 0.9327 |
| 285.89 | 0.9419 |
| 279.92 | 0.9522 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Methane, nitro- (2) - Liquid mixture 1 |
|---|---|
| 279.36 | 0.2957 |
| 284.38 | 0.3188 |
| 285.24 | 0.3238 |
| 289.71 | 0.3568 |
| 293.47 | 0.3899 |
| 296.69 | 0.4220 |
| 299.58 | 0.4575 |
| 302.58 | 0.5007 |
| 304.95 | 0.5458 |
| 306.23 | 0.5836 |
| 307.09 | 0.6160 |
| 307.74 | 0.6553 |
| 307.99 | 0.6998 |
| 308.00 | 0.7502 |
| 307.78 | 0.7925 |
| 306.45 | 0.8378 |
| 303.60 | 0.8709 |
| 303.74 | 0.8715 |
| 301.25 | 0.8875 |
| 299.13 | 0.8994 |
| 296.63 | 0.9117 |
| 294.57 | 0.9200 |
| 290.01 | 0.9327 |
| 285.89 | 0.9419 |
| 279.92 | 0.9522 |