Operational condition: Mole fraction = 0 (Liquid)
Temperature, K - Liquid | Activity coefficient of n-Hexane (1) - Liquid |
---|---|
303.15 | 413.74 |
313.15 | 382.52 |
323.15 | 340.01 |
333.15 | 315.78 |
343.15 | 268.43 |
Operational condition: Mole fraction = 0 (Liquid)
Temperature, K - Liquid | Activity coefficient of n-Hexane (1) - Liquid |
---|---|
303.15 | 413.74 |
313.15 | 382.52 |
323.15 | 340.01 |
333.15 | 315.78 |
343.15 | 268.43 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of n-Hexane (1) - Liquid mixture 1 |
---|---|
303.20 | 0.9960 |
313.20 | 0.9960 |
317.20 | 0.9950 |
322.20 | 0.9950 |
327.20 | 0.9950 |
331.20 | 0.9950 |
335.20 | 0.9940 |
338.20 | 0.9940 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of n-Hexane (1) - Liquid mixture 2 |
---|---|
303.20 | 0.0120 |
313.20 | 0.0130 |
317.20 | 0.0140 |
322.20 | 0.0130 |
327.20 | 0.0140 |
331.20 | 0.0150 |
335.20 | 0.0160 |
338.20 | 0.0160 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of n-Hexane (1) - Liquid mixture 1 |
---|---|
303.20 | 0.9960 |
313.20 | 0.9960 |
317.20 | 0.9950 |
322.20 | 0.9950 |
327.20 | 0.9950 |
331.20 | 0.9950 |
335.20 | 0.9940 |
338.20 | 0.9940 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of n-Hexane (1) - Liquid mixture 2 |
---|---|
303.20 | 0.0120 |
313.20 | 0.0130 |
317.20 | 0.0140 |
322.20 | 0.0130 |
327.20 | 0.0140 |
331.20 | 0.0150 |
335.20 | 0.0160 |
338.20 | 0.0160 |