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 |