Mixture of Methyl formate + Methyl Alcohol
Datasets
-
Excess molar enthalpy (molar enthalpy (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
ρl - Mass density, kg/m3 (2)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mole fraction of Methyl formate (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0200 |
0.0750 |
0.0487 |
0.1790 |
0.0833 |
0.3110 |
0.1225 |
0.4410 |
0.1670 |
0.5770 |
0.2135 |
0.7030 |
0.2613 |
0.8170 |
0.3086 |
0.9140 |
0.3501 |
0.9870 |
0.3644 |
1.01 |
0.3943 |
1.054 |
0.4077 |
1.074 |
0.4572 |
1.131 |
0.5127 |
1.179 |
0.5783 |
1.196 |
0.6460 |
1.178 |
0.7178 |
1.105 |
0.7842 |
0.9840 |
0.8517 |
0.8080 |
0.9098 |
0.5840 |
0.9505 |
0.3390 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mole fraction of Methyl formate (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
0.0200 |
0.0750 |
0.0487 |
0.1790 |
0.0833 |
0.3110 |
0.1225 |
0.4410 |
0.1670 |
0.5770 |
0.2135 |
0.7030 |
0.2613 |
0.8170 |
0.3086 |
0.9140 |
0.3501 |
0.9870 |
0.3644 |
1.01 |
0.3943 |
1.054 |
0.4077 |
1.074 |
0.4572 |
1.131 |
0.5127 |
1.179 |
0.5783 |
1.196 |
0.6460 |
1.178 |
0.7178 |
1.105 |
0.7842 |
0.9840 |
0.8517 |
0.8080 |
0.9098 |
0.5840 |
0.9505 |
0.3390 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Methyl formate (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
358.92 |
1.0000 |
550.40 |
358.93 |
0.0000 |
221.40 |
358.93 |
0.0976 |
321.20 |
358.93 |
0.2461 |
411.80 |
358.93 |
0.2959 |
432.90 |
358.93 |
0.3465 |
451.40 |
358.93 |
0.3961 |
467.10 |
358.93 |
0.4470 |
481.50 |
358.93 |
0.5482 |
504.80 |
358.93 |
0.9486 |
551.90 |
358.93 |
0.9690 |
551.80 |
358.93 |
0.9900 |
551.00 |
358.94 |
0.0108 |
235.90 |
358.94 |
0.0300 |
257.90 |
358.94 |
0.0488 |
277.70 |
358.94 |
0.1459 |
356.50 |
358.94 |
0.1962 |
386.90 |
358.94 |
0.4971 |
494.20 |
358.94 |
0.4988 |
494.20 |
358.94 |
0.5983 |
514.70 |
358.94 |
0.6483 |
523.40 |
358.94 |
0.6982 |
531.10 |
358.94 |
0.7484 |
537.90 |
358.94 |
0.7976 |
543.80 |
358.94 |
0.8486 |
548.30 |
358.94 |
0.8988 |
551.20 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Methyl formate (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
358.92 |
1.0000 |
550.40 |
358.93 |
0.0000 |
221.40 |
358.93 |
0.0976 |
321.20 |
358.93 |
0.2461 |
411.80 |
358.93 |
0.2959 |
432.90 |
358.93 |
0.3465 |
451.40 |
358.93 |
0.3961 |
467.10 |
358.93 |
0.4470 |
481.50 |
358.93 |
0.5482 |
504.80 |
358.93 |
0.9486 |
551.90 |
358.93 |
0.9690 |
551.80 |
358.93 |
0.9900 |
551.00 |
358.94 |
0.0108 |
235.90 |
358.94 |
0.0300 |
257.90 |
358.94 |
0.0488 |
277.70 |
358.94 |
0.1459 |
356.50 |
358.94 |
0.1962 |
386.90 |
358.94 |
0.4971 |
494.20 |
358.94 |
0.4988 |
494.20 |
358.94 |
0.5983 |
514.70 |
358.94 |
0.6483 |
523.40 |
358.94 |
0.6982 |
531.10 |
358.94 |
0.7484 |
537.90 |
358.94 |
0.7976 |
543.80 |
358.94 |
0.8486 |
548.30 |
358.94 |
0.8988 |
551.20 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mole fraction of Methyl formate (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
786.4 |
0.0337 |
795.73 |
0.0833 |
808.8 |
0.1557 |
826.74 |
0.1900 |
834.77 |
0.2499 |
848.14 |
0.3219 |
863.26 |
0.3906 |
876.73 |
0.4946 |
895.61 |
0.5416 |
903.58 |
0.6467 |
920.31 |
0.7271 |
932.1 |
0.7815 |
939.62 |
0.8533 |
949.01 |
0.8968 |
954.39 |
0.8968 |
954.39 |
0.9357 |
959.02 |
1.0000 |
966.28 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mole fraction of Methyl formate (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
786.4 |
0.0337 |
795.73 |
0.0833 |
808.8 |
0.1557 |
826.74 |
0.1900 |
834.77 |
0.2499 |
848.14 |
0.3219 |
863.26 |
0.3906 |
876.73 |
0.4946 |
895.61 |
0.5416 |
903.58 |
0.6467 |
920.31 |
0.7271 |
932.1 |
0.7815 |
939.62 |
0.8533 |
949.01 |
0.8968 |
954.39 |
0.8968 |
954.39 |
0.9357 |
959.02 |
1.0000 |
966.28 |
Sources