Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Methane, nitro- (2) - Liquid mixture 1 |
|---|---|
| 275.54 | 0.2783 |
| 279.29 | 0.3003 |
| 281.78 | 0.3165 |
| 285.50 | 0.3420 |
| 289.10 | 0.3709 |
| 291.64 | 0.3932 |
| 294.65 | 0.4229 |
| 297.68 | 0.4589 |
| 300.35 | 0.4969 |
| 303.09 | 0.5448 |
| 304.50 | 0.5816 |
| 305.48 | 0.6176 |
| 306.10 | 0.6553 |
| 306.39 | 0.7007 |
| 306.44 | 0.7496 |
| 306.14 | 0.8004 |
| 304.90 | 0.8396 |
| 302.56 | 0.8706 |
| 299.92 | 0.8906 |
| 298.06 | 0.9010 |
| 295.27 | 0.9132 |
| 291.72 | 0.9248 |
| 287.54 | 0.9359 |
| 282.11 | 0.9470 |
| 278.02 | 0.9536 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Methane, nitro- (2) - Liquid mixture 1 |
|---|---|
| 275.54 | 0.2783 |
| 279.29 | 0.3003 |
| 281.78 | 0.3165 |
| 285.50 | 0.3420 |
| 289.10 | 0.3709 |
| 291.64 | 0.3932 |
| 294.65 | 0.4229 |
| 297.68 | 0.4589 |
| 300.35 | 0.4969 |
| 303.09 | 0.5448 |
| 304.50 | 0.5816 |
| 305.48 | 0.6176 |
| 306.10 | 0.6553 |
| 306.39 | 0.7007 |
| 306.44 | 0.7496 |
| 306.14 | 0.8004 |
| 304.90 | 0.8396 |
| 302.56 | 0.8706 |
| 299.92 | 0.8906 |
| 298.06 | 0.9010 |
| 295.27 | 0.9132 |
| 291.72 | 0.9248 |
| 287.54 | 0.9359 |
| 282.11 | 0.9470 |
| 278.02 | 0.9536 |