Operational conditions:
Mole fraction of Benzene, nitro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0997 | 0.4702 |
0.1991 | 0.8427 |
0.2988 | 1.106 |
0.4003 | 1.2855 |
0.4899 | 1.4298 |
0.5905 | 1.4862 |
0.6997 | 1.4403 |
0.7999 | 1.2721 |
0.8939 | 0.9275 |
Operational conditions:
Mole fraction of Benzene, nitro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0997 | 0.4702 |
0.1991 | 0.8427 |
0.2988 | 1.106 |
0.4003 | 1.2855 |
0.4899 | 1.4298 |
0.5905 | 1.4862 |
0.6997 | 1.4403 |
0.7999 | 1.2721 |
0.8939 | 0.9275 |
Operational condition: Pressure, kPa = 94.95 (Liquid)
Mole fraction of Ethanol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 481.15 |
0.0603 | 438.85 |
0.1187 | 419.85 |
0.2007 | 403.55 |
0.2878 | 392.05 |
0.3662 | 384.15 |
0.4469 | 377.45 |
0.5228 | 372.15 |
0.6028 | 367.15 |
0.6717 | 363.35 |
0.7399 | 359.85 |
0.8005 | 357.05 |
0.8836 | 353.65 |
0.9408 | 351.50 |
1.0000 | 349.85 |
Operational condition: Pressure, kPa = 94.95 (Liquid)
Mole fraction of Ethanol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 481.15 |
0.0603 | 438.85 |
0.1187 | 419.85 |
0.2007 | 403.55 |
0.2878 | 392.05 |
0.3662 | 384.15 |
0.4469 | 377.45 |
0.5228 | 372.15 |
0.6028 | 367.15 |
0.6717 | 363.35 |
0.7399 | 359.85 |
0.8005 | 357.05 |
0.8836 | 353.65 |
0.9408 | 351.50 |
1.0000 | 349.85 |