Operational conditions:
Mole fraction of Benzene, nitro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.1116 | 0.7713 |
0.2145 | 1.2985 |
0.3183 | 1.6646 |
0.4126 | 1.8747 |
0.5133 | 1.94 |
0.6100 | 1.9495 |
0.6849 | 1.879 |
0.7953 | 1.6345 |
0.8987 | 1.0969 |
Operational conditions:
Mole fraction of Benzene, nitro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.1116 | 0.7713 |
0.2145 | 1.2985 |
0.3183 | 1.6646 |
0.4126 | 1.8747 |
0.5133 | 1.94 |
0.6100 | 1.9495 |
0.6849 | 1.879 |
0.7953 | 1.6345 |
0.8987 | 1.0969 |
Operational condition: Pressure, kPa = 94.95 (Liquid)
Mole fraction of 1-Butanol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 481.15 |
0.0733 | 449.75 |
0.1465 | 437.25 |
0.2557 | 425.45 |
0.3402 | 418.55 |
0.4074 | 413.85 |
0.4620 | 410.45 |
0.5077 | 407.85 |
0.5922 | 403.55 |
0.6448 | 401.25 |
0.7070 | 398.65 |
0.7840 | 395.75 |
0.8780 | 392.65 |
1.0000 | 389.15 |
Operational condition: Pressure, kPa = 94.95 (Liquid)
Mole fraction of 1-Butanol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 481.15 |
0.0733 | 449.75 |
0.1465 | 437.25 |
0.2557 | 425.45 |
0.3402 | 418.55 |
0.4074 | 413.85 |
0.4620 | 410.45 |
0.5077 | 407.85 |
0.5922 | 403.55 |
0.6448 | 401.25 |
0.7070 | 398.65 |
0.7840 | 395.75 |
0.8780 | 392.65 |
1.0000 | 389.15 |