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 |