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 |