Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Acetonitrile (1) - Liquid mixture 1 |
---|---|
298.15 | 0.1030 |
303.15 | 0.1080 |
313.15 | 0.1340 |
323.15 | 0.1450 |
333.15 | 0.1680 |
343.15 | 0.1940 |
353.15 | 0.2380 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 2 | Mole fraction of Acetonitrile (1) - Liquid mixture 2 |
---|---|
298.15 | 0.9980 |
303.15 | 0.9970 |
313.15 | 0.9960 |
323.15 | 0.9950 |
333.15 | 0.9940 |
343.15 | 0.9920 |
353.15 | 0.9900 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Acetonitrile (1) - Liquid mixture 1 |
---|---|
298.15 | 0.1030 |
303.15 | 0.1080 |
313.15 | 0.1340 |
323.15 | 0.1450 |
333.15 | 0.1680 |
343.15 | 0.1940 |
353.15 | 0.2380 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 2 | Mole fraction of Acetonitrile (1) - Liquid mixture 2 |
---|---|
298.15 | 0.9980 |
303.15 | 0.9970 |
313.15 | 0.9960 |
323.15 | 0.9950 |
333.15 | 0.9940 |
343.15 | 0.9920 |
353.15 | 0.9900 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Mole fraction of Acetonitrile (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.4205 | 382.69 |
0.4628 | 389.79 |
0.5138 | 398.42 |
0.5587 | 403.28 |
0.6068 | 408.87 |
0.6321 | 411.43 |
0.6626 | 412.96 |
0.6967 | 414.42 |
0.7360 | 415.20 |
0.7389 | 415.31 |
0.7538 | 415.52 |
0.7643 | 415.65 |
0.7737 | 415.80 |
0.8098 | 416.17 |
0.8311 | 416.29 |
0.8459 | 416.38 |
0.8694 | 416.28 |
0.8715 | 416.32 |
0.8963 | 416.09 |
0.9066 | 415.61 |
0.9206 | 414.41 |
0.9298 | 413.48 |
0.9408 | 410.28 |
0.9497 | 407.71 |
0.9579 | 404.02 |
0.9693 | 396.72 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Mole fraction of Acetonitrile (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.4205 | 382.69 |
0.4628 | 389.79 |
0.5138 | 398.42 |
0.5587 | 403.28 |
0.6068 | 408.87 |
0.6321 | 411.43 |
0.6626 | 412.96 |
0.6967 | 414.42 |
0.7360 | 415.20 |
0.7389 | 415.31 |
0.7538 | 415.52 |
0.7643 | 415.65 |
0.7737 | 415.80 |
0.8098 | 416.17 |
0.8311 | 416.29 |
0.8459 | 416.38 |
0.8694 | 416.28 |
0.8715 | 416.32 |
0.8963 | 416.09 |
0.9066 | 415.61 |
0.9206 | 414.41 |
0.9298 | 413.48 |
0.9408 | 410.28 |
0.9497 | 407.71 |
0.9579 | 404.02 |
0.9693 | 396.72 |