Operational conditions:
Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0455 | 0.3209 |
0.0914 | 0.5188 |
0.1377 | 0.6506 |
0.1845 | 0.7361 |
0.2317 | 0.7849 |
0.2794 | 0.8112 |
0.3276 | 0.8152 |
0.3763 | 0.8082 |
0.4254 | 0.7790 |
0.4750 | 0.7485 |
0.5251 | 0.6990 |
0.5758 | 0.6419 |
0.6269 | 0.5831 |
0.6786 | 0.5086 |
0.7308 | 0.4326 |
0.7835 | 0.3514 |
0.8368 | 0.2690 |
0.8906 | 0.1817 |
0.9450 | 0.0903 |
Operational conditions:
Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0455 | 0.3209 |
0.0914 | 0.5188 |
0.1377 | 0.6506 |
0.1845 | 0.7361 |
0.2317 | 0.7849 |
0.2794 | 0.8112 |
0.3276 | 0.8152 |
0.3763 | 0.8082 |
0.4254 | 0.7790 |
0.4750 | 0.7485 |
0.5251 | 0.6990 |
0.5758 | 0.6419 |
0.6269 | 0.5831 |
0.6786 | 0.5086 |
0.7308 | 0.4326 |
0.7835 | 0.3514 |
0.8368 | 0.2690 |
0.8906 | 0.1817 |
0.9450 | 0.0903 |
Operational condition: Pressure, kPa = 101 (Liquid)
Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
---|---|
0.0000 | 278.95 |
0.0490 | 276.50 |
0.1013 | 274.73 |
0.1497 | 273.32 |
0.2008 | 271.64 |
0.2209 | 271.02 |
0.3029 | 268.35 |
0.3498 | 266.30 |
0.3999 | 264.29 |
0.4503 | 261.84 |
0.5000 | 258.92 |
0.5450 | 256.52 |
0.5995 | 252.62 |
0.6501 | 248.09 |
0.7005 | 242.30 |
0.7478 | 236.48 |
0.7996 | 227.95 |
0.8500 | 217.10 |
Operational condition: Pressure, kPa = 101 (Liquid)
Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
---|---|
0.0000 | 278.95 |
0.0490 | 276.50 |
0.1013 | 274.73 |
0.1497 | 273.32 |
0.2008 | 271.64 |
0.2209 | 271.02 |
0.3029 | 268.35 |
0.3498 | 266.30 |
0.3999 | 264.29 |
0.4503 | 261.84 |
0.5000 | 258.92 |
0.5450 | 256.52 |
0.5995 | 252.62 |
0.6501 | 248.09 |
0.7005 | 242.30 |
0.7478 | 236.48 |
0.7996 | 227.95 |
0.8500 | 217.10 |