Operational condition: Pressure, kPa = 101.32 (Gas)
Mole fraction of Methyl formate (1) - Liquid | Mole fraction of Methyl formate (1) - Gas |
---|---|
0.0000 | 0.0000 |
0.0160 | 0.4190 |
0.0260 | 0.5540 |
0.0390 | 0.6700 |
0.0510 | 0.7430 |
0.0620 | 0.7800 |
0.1300 | 0.9060 |
0.1940 | 0.9400 |
0.2400 | 0.9530 |
0.2780 | 0.9620 |
0.3460 | 0.9700 |
0.4040 | 0.9720 |
0.4620 | 0.9740 |
0.5050 | 0.9770 |
0.5920 | 0.9770 |
0.7190 | 0.9800 |
0.7910 | 0.9810 |
0.8240 | 0.9810 |
0.8520 | 0.9820 |
0.8680 | 0.9810 |
0.8930 | 0.9830 |
0.9050 | 0.9830 |
0.9240 | 0.9850 |
0.9240 | 0.9840 |
0.9480 | 0.9880 |
0.9620 | 0.9900 |
0.9740 | 0.9930 |
0.9800 | 0.9940 |
0.9840 | 0.9950 |
0.9930 | 0.9980 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.32 (Gas)
Mole fraction of Methyl formate (1) - Liquid | Mole fraction of Methyl formate (1) - Gas |
---|---|
0.0000 | 0.0000 |
0.0160 | 0.4190 |
0.0260 | 0.5540 |
0.0390 | 0.6700 |
0.0510 | 0.7430 |
0.0620 | 0.7800 |
0.1300 | 0.9060 |
0.1940 | 0.9400 |
0.2400 | 0.9530 |
0.2780 | 0.9620 |
0.3460 | 0.9700 |
0.4040 | 0.9720 |
0.4620 | 0.9740 |
0.5050 | 0.9770 |
0.5920 | 0.9770 |
0.7190 | 0.9800 |
0.7910 | 0.9810 |
0.8240 | 0.9810 |
0.8520 | 0.9820 |
0.8680 | 0.9810 |
0.8930 | 0.9830 |
0.9050 | 0.9830 |
0.9240 | 0.9850 |
0.9240 | 0.9840 |
0.9480 | 0.9880 |
0.9620 | 0.9900 |
0.9740 | 0.9930 |
0.9800 | 0.9940 |
0.9840 | 0.9950 |
0.9930 | 0.9980 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Methyl formate (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
291.15 | 0.1210 | 1.011 |
291.15 | 0.1960 | 1.514 |
291.15 | 0.2670 | 1.879 |
291.15 | 0.3480 | 2.171 |
291.15 | 0.4190 | 2.336 |
291.15 | 0.4760 | 2.391 |
291.15 | 0.5280 | 2.385 |
291.15 | 0.5730 | 2.339 |
291.15 | 0.6120 | 2.276 |
291.15 | 0.6600 | 2.148 |
291.15 | 0.7010 | 2.002 |
291.15 | 0.7470 | 1.814 |
291.15 | 0.7890 | 1.618 |
291.15 | 0.8290 | 1.378 |
291.15 | 0.8680 | 1.154 |
291.15 | 0.9070 | 0.8950 |
291.15 | 0.9430 | 0.6250 |
291.15 | 0.9730 | 0.3410 |
298.15 | 0.0760 | 0.6530 |
298.15 | 0.1620 | 1.232 |
298.15 | 0.2700 | 1.876 |
298.15 | 0.3670 | 2.291 |
298.15 | 0.4260 | 2.435 |
298.15 | 0.4920 | 2.531 |
298.15 | 0.5430 | 2.532 |
298.15 | 0.5850 | 2.484 |
298.15 | 0.5910 | 2.492 |
298.15 | 0.6320 | 2.425 |
298.15 | 0.6790 | 2.321 |
298.15 | 0.7300 | 2.158 |
298.15 | 0.7860 | 1.94 |
298.15 | 0.8380 | 1.689 |
298.15 | 0.8820 | 1.397 |
298.15 | 0.9280 | 1.035 |
298.15 | 0.9650 | 0.6760 |
298.15 | 0.9870 | 0.3030 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Methyl formate (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
291.15 | 0.1210 | 1.011 |
291.15 | 0.1960 | 1.514 |
291.15 | 0.2670 | 1.879 |
291.15 | 0.3480 | 2.171 |
291.15 | 0.4190 | 2.336 |
291.15 | 0.4760 | 2.391 |
291.15 | 0.5280 | 2.385 |
291.15 | 0.5730 | 2.339 |
291.15 | 0.6120 | 2.276 |
291.15 | 0.6600 | 2.148 |
291.15 | 0.7010 | 2.002 |
291.15 | 0.7470 | 1.814 |
291.15 | 0.7890 | 1.618 |
291.15 | 0.8290 | 1.378 |
291.15 | 0.8680 | 1.154 |
291.15 | 0.9070 | 0.8950 |
291.15 | 0.9430 | 0.6250 |
291.15 | 0.9730 | 0.3410 |
298.15 | 0.0760 | 0.6530 |
298.15 | 0.1620 | 1.232 |
298.15 | 0.2700 | 1.876 |
298.15 | 0.3670 | 2.291 |
298.15 | 0.4260 | 2.435 |
298.15 | 0.4920 | 2.531 |
298.15 | 0.5430 | 2.532 |
298.15 | 0.5850 | 2.484 |
298.15 | 0.5910 | 2.492 |
298.15 | 0.6320 | 2.425 |
298.15 | 0.6790 | 2.321 |
298.15 | 0.7300 | 2.158 |
298.15 | 0.7860 | 1.94 |
298.15 | 0.8380 | 1.689 |
298.15 | 0.8820 | 1.397 |
298.15 | 0.9280 | 1.035 |
298.15 | 0.9650 | 0.6760 |
298.15 | 0.9870 | 0.3030 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Methyl formate (1) - Liquid | Mass density, kg/m3 - Liquid |
291.15 | 0.0000 | 704.17 |
291.15 | 0.0536 | 707.45 |
291.15 | 0.1137 | 712.28 |
291.15 | 0.1547 | 715.89 |
291.15 | 0.2040 | 721.07 |
291.15 | 0.2519 | 726.33 |
291.15 | 0.3039 | 732.8 |
291.15 | 0.3536 | 739.63 |
291.15 | 0.4040 | 747.53 |
291.15 | 0.4485 | 755.25 |
291.15 | 0.5059 | 766.45 |
291.15 | 0.5516 | 776.37 |
291.15 | 0.6001 | 788.04 |
291.15 | 0.6507 | 801.77 |
291.15 | 0.7021 | 817.89 |
291.15 | 0.7498 | 834.46 |
291.15 | 0.8010 | 854.97 |
291.15 | 0.8496 | 876.97 |
291.15 | 0.8987 | 903.9 |
291.15 | 0.9484 | 935.34 |
291.15 | 1.0000 | 976.46 |
298.15 | 0.0000 | 698.52 |
298.15 | 0.0297 | 700.47 |
298.15 | 0.0917 | 705.28 |
298.15 | 0.1332 | 708.34 |
298.15 | 0.2017 | 714.88 |
298.15 | 0.2416 | 719.0 |
298.15 | 0.3038 | 726.48 |
298.15 | 0.3520 | 732.97 |
298.15 | 0.3979 | 739.97 |
298.15 | 0.4465 | 748.0 |
298.15 | 0.5009 | 758.04 |
298.15 | 0.5483 | 767.97 |
298.15 | 0.5980 | 779.83 |
298.15 | 0.6501 | 793.37 |
298.15 | 0.7007 | 808.78 |
298.15 | 0.7513 | 826.49 |
298.15 | 0.8039 | 846.86 |
298.15 | 0.8486 | 867.89 |
298.15 | 0.9247 | 909.52 |
298.15 | 0.9482 | 925.15 |
298.15 | 1.0000 | 966.1 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Methyl formate (1) - Liquid | Mass density, kg/m3 - Liquid |
291.15 | 0.0000 | 704.17 |
291.15 | 0.0536 | 707.45 |
291.15 | 0.1137 | 712.28 |
291.15 | 0.1547 | 715.89 |
291.15 | 0.2040 | 721.07 |
291.15 | 0.2519 | 726.33 |
291.15 | 0.3039 | 732.8 |
291.15 | 0.3536 | 739.63 |
291.15 | 0.4040 | 747.53 |
291.15 | 0.4485 | 755.25 |
291.15 | 0.5059 | 766.45 |
291.15 | 0.5516 | 776.37 |
291.15 | 0.6001 | 788.04 |
291.15 | 0.6507 | 801.77 |
291.15 | 0.7021 | 817.89 |
291.15 | 0.7498 | 834.46 |
291.15 | 0.8010 | 854.97 |
291.15 | 0.8496 | 876.97 |
291.15 | 0.8987 | 903.9 |
291.15 | 0.9484 | 935.34 |
291.15 | 1.0000 | 976.46 |
298.15 | 0.0000 | 698.52 |
298.15 | 0.0297 | 700.47 |
298.15 | 0.0917 | 705.28 |
298.15 | 0.1332 | 708.34 |
298.15 | 0.2017 | 714.88 |
298.15 | 0.2416 | 719.0 |
298.15 | 0.3038 | 726.48 |
298.15 | 0.3520 | 732.97 |
298.15 | 0.3979 | 739.97 |
298.15 | 0.4465 | 748.0 |
298.15 | 0.5009 | 758.04 |
298.15 | 0.5483 | 767.97 |
298.15 | 0.5980 | 779.83 |
298.15 | 0.6501 | 793.37 |
298.15 | 0.7007 | 808.78 |
298.15 | 0.7513 | 826.49 |
298.15 | 0.8039 | 846.86 |
298.15 | 0.8486 | 867.89 |
298.15 | 0.9247 | 909.52 |
298.15 | 0.9482 | 925.15 |
298.15 | 1.0000 | 966.1 |
Operational condition: Pressure, kPa = 101.32 (Liquid)
Mole fraction of Methyl formate (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 398.83 |
0.0160 | 380.17 |
0.0260 | 371.94 |
0.0390 | 363.25 |
0.0510 | 356.28 |
0.0620 | 352.40 |
0.1300 | 332.26 |
0.1940 | 323.04 |
0.2400 | 318.17 |
0.2780 | 314.24 |
0.3460 | 309.95 |
0.4040 | 309.14 |
0.4620 | 308.36 |
0.5050 | 307.80 |
0.5920 | 308.14 |
0.7190 | 306.84 |
0.7910 | 306.54 |
0.8240 | 306.53 |
0.8520 | 306.28 |
0.8680 | 306.25 |
0.8930 | 305.99 |
0.9050 | 305.89 |
0.9240 | 305.76 |
0.9240 | 305.73 |
0.9480 | 305.48 |
0.9620 | 305.33 |
0.9740 | 305.28 |
0.9800 | 305.15 |
0.9840 | 305.06 |
0.9930 | 304.92 |
1.0000 | 304.70 |
Operational condition: Pressure, kPa = 101.32 (Liquid)
Mole fraction of Methyl formate (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 398.83 |
0.0160 | 380.17 |
0.0260 | 371.94 |
0.0390 | 363.25 |
0.0510 | 356.28 |
0.0620 | 352.40 |
0.1300 | 332.26 |
0.1940 | 323.04 |
0.2400 | 318.17 |
0.2780 | 314.24 |
0.3460 | 309.95 |
0.4040 | 309.14 |
0.4620 | 308.36 |
0.5050 | 307.80 |
0.5920 | 308.14 |
0.7190 | 306.84 |
0.7910 | 306.54 |
0.8240 | 306.53 |
0.8520 | 306.28 |
0.8680 | 306.25 |
0.8930 | 305.99 |
0.9050 | 305.89 |
0.9240 | 305.76 |
0.9240 | 305.73 |
0.9480 | 305.48 |
0.9620 | 305.33 |
0.9740 | 305.28 |
0.9800 | 305.15 |
0.9840 | 305.06 |
0.9930 | 304.92 |
1.0000 | 304.70 |