- Name
- 1-Propanol
- InChI
- InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
- InChI Key
- BDERNNFJNOPAEC-UHFFFAOYSA-N
- Formula
- C3H8O
- SMILES
- CCCO
- Mol. Weight (g/mol)
- 60.09
- CAS
- 71-23-8
- Name
- Acetic acid, methyl ester
- InChI
- InChI=1S/C3H6O2/c1-3(4)5-2/h1-2H3
- InChI Key
- KXKVLQRXCPHEJC-UHFFFAOYSA-N
- Formula
- C3H6O2
- SMILES
- COC(C)=O
- Mol. Weight (g/mol)
- 74.08
- CAS
- 79-20-9
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Datasets
- Mole fraction (4)
- Excess molar enthalpy (molar enthalpy (2)
- ρl - Mass density, kg/m3 (2)
- Tboil - Boiling temperature at pressure P, K (4)
Mole fraction of Acetic acid, methyl ester (2) [ref]
Operational condition: Pressure, kPa = 300 (Liquid)
| Mole fraction of Acetic acid, methyl ester (2) - Liquid | Mole fraction of Acetic acid, methyl ester (2) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0070 | 0.0190 |
| 0.0160 | 0.0430 |
| 0.0560 | 0.1720 |
| 0.1290 | 0.3460 |
| 0.1920 | 0.4430 |
| 0.2610 | 0.5440 |
| 0.3680 | 0.6550 |
| 0.4210 | 0.6960 |
| 0.5020 | 0.7450 |
| 0.5300 | 0.7630 |
| 0.5690 | 0.7860 |
| 0.5910 | 0.7940 |
| 0.6220 | 0.8160 |
| 0.6630 | 0.8410 |
| 0.7180 | 0.8630 |
| 0.7520 | 0.8790 |
| 0.7920 | 0.8910 |
| 0.8770 | 0.9280 |
| 0.9400 | 0.9630 |
| 0.9640 | 0.9770 |
| 0.9900 | 0.9930 |
| 1.0000 | 1.0000 |
Mole fraction of Acetic acid, methyl ester (2) [ref]
Operational condition: Pressure, kPa = 600 (Liquid)
| Mole fraction of Acetic acid, methyl ester (2) - Liquid | Mole fraction of Acetic acid, methyl ester (2) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0050 | 0.0160 |
| 0.0190 | 0.0550 |
| 0.0340 | 0.0970 |
| 0.0820 | 0.2090 |
| 0.1930 | 0.3930 |
| 0.2940 | 0.5240 |
| 0.3510 | 0.5850 |
| 0.4500 | 0.6650 |
| 0.5290 | 0.7240 |
| 0.5640 | 0.7380 |
| 0.5870 | 0.7590 |
| 0.6220 | 0.7720 |
| 0.6480 | 0.7910 |
| 0.6760 | 0.8080 |
| 0.7100 | 0.8270 |
| 0.7460 | 0.8500 |
| 0.7810 | 0.8730 |
| 0.8180 | 0.8970 |
| 0.8590 | 0.9190 |
| 0.8930 | 0.9360 |
| 0.9190 | 0.9500 |
| 0.9420 | 0.9620 |
| 0.9760 | 0.9850 |
| 0.9880 | 0.9930 |
| 0.9950 | 0.9970 |
| 1.0000 | 1.0000 |
Mole fraction of Acetic acid, methyl ester (2) [ref]
Operational condition: Pressure, kPa = 300 (Liquid)
| Mole fraction of Acetic acid, methyl ester (2) - Liquid | Mole fraction of Acetic acid, methyl ester (2) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0070 | 0.0190 |
| 0.0160 | 0.0430 |
| 0.0560 | 0.1720 |
| 0.1290 | 0.3460 |
| 0.1920 | 0.4430 |
| 0.2610 | 0.5440 |
| 0.3680 | 0.6550 |
| 0.4210 | 0.6960 |
| 0.5020 | 0.7450 |
| 0.5300 | 0.7630 |
| 0.5690 | 0.7860 |
| 0.5910 | 0.7940 |
| 0.6220 | 0.8160 |
| 0.6630 | 0.8410 |
| 0.7180 | 0.8630 |
| 0.7520 | 0.8790 |
| 0.7920 | 0.8910 |
| 0.8770 | 0.9280 |
| 0.9400 | 0.9630 |
| 0.9640 | 0.9770 |
| 0.9900 | 0.9930 |
| 1.0000 | 1.0000 |
Mole fraction of Acetic acid, methyl ester (2) [ref]
Operational condition: Pressure, kPa = 600 (Liquid)
| Mole fraction of Acetic acid, methyl ester (2) - Liquid | Mole fraction of Acetic acid, methyl ester (2) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0050 | 0.0160 |
| 0.0190 | 0.0550 |
| 0.0340 | 0.0970 |
| 0.0820 | 0.2090 |
| 0.1930 | 0.3930 |
| 0.2940 | 0.5240 |
| 0.3510 | 0.5850 |
| 0.4500 | 0.6650 |
| 0.5290 | 0.7240 |
| 0.5640 | 0.7380 |
| 0.5870 | 0.7590 |
| 0.6220 | 0.7720 |
| 0.6480 | 0.7910 |
| 0.6760 | 0.8080 |
| 0.7100 | 0.8270 |
| 0.7460 | 0.8500 |
| 0.7810 | 0.8730 |
| 0.8180 | 0.8970 |
| 0.8590 | 0.9190 |
| 0.8930 | 0.9360 |
| 0.9190 | 0.9500 |
| 0.9420 | 0.9620 |
| 0.9760 | 0.9850 |
| 0.9880 | 0.9930 |
| 0.9950 | 0.9970 |
| 1.0000 | 1.0000 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mole fraction of Acetic acid, methyl ester (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 298.15 | 5000.00 | 0.0510 | 0.3129 |
| 298.15 | 5000.00 | 0.0990 | 0.5974 |
| 298.15 | 5000.00 | 0.1490 | 0.8406 |
| 298.15 | 5000.00 | 0.1990 | 1.0367 |
| 298.15 | 5000.00 | 0.2510 | 1.1999 |
| 298.15 | 5000.00 | 0.3000 | 1.3219 |
| 298.15 | 5000.00 | 0.3490 | 1.4143 |
| 298.15 | 5000.00 | 0.4000 | 1.4824 |
| 298.15 | 5000.00 | 0.4510 | 1.5181 |
| 298.15 | 5000.00 | 0.5010 | 1.5228 |
| 298.15 | 5000.00 | 0.5510 | 1.4979 |
| 298.15 | 5000.00 | 0.6000 | 1.4538 |
| 298.15 | 5000.00 | 0.6500 | 1.3826 |
| 298.15 | 5000.00 | 0.7010 | 1.2758 |
| 298.15 | 5000.00 | 0.7490 | 1.1425 |
| 298.15 | 5000.00 | 0.8000 | 0.9874 |
| 298.15 | 5000.00 | 0.8500 | 0.7973 |
| 298.15 | 5000.00 | 0.8990 | 0.5709 |
| 298.15 | 5000.00 | 0.9510 | 0.2976 |
| 298.15 | 10000.00 | 0.0510 | 0.3401 |
| 298.15 | 10000.00 | 0.0990 | 0.6084 |
| 298.15 | 10000.00 | 0.1490 | 0.8444 |
| 298.15 | 10000.00 | 0.1990 | 1.0383 |
| 298.15 | 10000.00 | 0.2500 | 1.2018 |
| 298.15 | 10000.00 | 0.3000 | 1.3208 |
| 298.15 | 10000.00 | 0.3490 | 1.4106 |
| 298.15 | 10000.00 | 0.3990 | 1.4749 |
| 298.15 | 10000.00 | 0.4500 | 1.5125 |
| 298.15 | 10000.00 | 0.5000 | 1.5158 |
| 298.15 | 10000.00 | 0.5500 | 1.4955 |
| 298.15 | 10000.00 | 0.5990 | 1.4496 |
| 298.15 | 10000.00 | 0.6490 | 1.3787 |
| 298.15 | 10000.00 | 0.7000 | 1.275 |
| 298.15 | 10000.00 | 0.7490 | 1.148 |
| 298.15 | 10000.00 | 0.7990 | 0.9898 |
| 298.15 | 10000.00 | 0.8490 | 0.7905 |
| 298.15 | 10000.00 | 0.8990 | 0.5654 |
| 298.15 | 10000.00 | 0.9510 | 0.2856 |
| 298.15 | 5000.00 | 0.0510 | 0.3129 |
| 298.15 | 5000.00 | 0.0990 | 0.5974 |
| 298.15 | 5000.00 | 0.1490 | 0.8406 |
| 298.15 | 5000.00 | 0.1990 | 1.0367 |
| 298.15 | 5000.00 | 0.2510 | 1.1999 |
| 298.15 | 5000.00 | 0.3000 | 1.3219 |
| 298.15 | 5000.00 | 0.3490 | 1.4143 |
| 298.15 | 5000.00 | 0.4000 | 1.4824 |
| 298.15 | 5000.00 | 0.4510 | 1.5181 |
| 298.15 | 5000.00 | 0.5010 | 1.5228 |
| 298.15 | 5000.00 | 0.5510 | 1.4979 |
| 298.15 | 5000.00 | 0.6000 | 1.4538 |
| 298.15 | 5000.00 | 0.6500 | 1.3826 |
| 298.15 | 5000.00 | 0.7010 | 1.2758 |
| 298.15 | 5000.00 | 0.7490 | 1.1425 |
| 298.15 | 5000.00 | 0.8000 | 0.9874 |
| 298.15 | 5000.00 | 0.8500 | 0.7973 |
| 298.15 | 5000.00 | 0.8990 | 0.5709 |
| 333.15 | 10000.00 | 0.0510 | 0.4022 |
| 333.15 | 10000.00 | 0.0990 | 0.7037 |
| 333.15 | 10000.00 | 0.1500 | 0.9723 |
| 333.15 | 10000.00 | 0.2000 | 1.201 |
| 333.15 | 10000.00 | 0.2500 | 1.3767 |
| 333.15 | 10000.00 | 0.3000 | 1.5191 |
| 333.15 | 10000.00 | 0.3500 | 1.6258 |
| 333.15 | 10000.00 | 0.3990 | 1.7066 |
| 333.15 | 10000.00 | 0.4480 | 1.7488 |
| 333.15 | 10000.00 | 0.5000 | 1.7664 |
| 333.15 | 10000.00 | 0.5480 | 1.7514 |
| 333.15 | 10000.00 | 0.5990 | 1.6953 |
| 333.15 | 10000.00 | 0.6500 | 1.6052 |
| 333.15 | 10000.00 | 0.7000 | 1.4849 |
| 333.15 | 10000.00 | 0.7510 | 1.325 |
| 333.15 | 10000.00 | 0.8010 | 1.1322 |
| 333.15 | 10000.00 | 0.8500 | 0.8981 |
| 333.15 | 10000.00 | 0.8990 | 0.6270 |
| 333.15 | 10000.00 | 0.9490 | 0.3143 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mole fraction of Acetic acid, methyl ester (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 298.15 | 5000.00 | 0.0510 | 0.3129 |
| 298.15 | 5000.00 | 0.0990 | 0.5974 |
| 298.15 | 5000.00 | 0.1490 | 0.8406 |
| 298.15 | 5000.00 | 0.1990 | 1.0367 |
| 298.15 | 5000.00 | 0.2510 | 1.1999 |
| 298.15 | 5000.00 | 0.3000 | 1.3219 |
| 298.15 | 5000.00 | 0.3490 | 1.4143 |
| 298.15 | 5000.00 | 0.4000 | 1.4824 |
| 298.15 | 5000.00 | 0.4510 | 1.5181 |
| 298.15 | 5000.00 | 0.5010 | 1.5228 |
| 298.15 | 5000.00 | 0.5510 | 1.4979 |
| 298.15 | 5000.00 | 0.6000 | 1.4538 |
| 298.15 | 5000.00 | 0.6500 | 1.3826 |
| 298.15 | 5000.00 | 0.7010 | 1.2758 |
| 298.15 | 5000.00 | 0.7490 | 1.1425 |
| 298.15 | 5000.00 | 0.8000 | 0.9874 |
| 298.15 | 5000.00 | 0.8500 | 0.7973 |
| 298.15 | 5000.00 | 0.8990 | 0.5709 |
| 298.15 | 5000.00 | 0.9510 | 0.2976 |
| 298.15 | 10000.00 | 0.0510 | 0.3401 |
| 298.15 | 10000.00 | 0.0990 | 0.6084 |
| 298.15 | 10000.00 | 0.1490 | 0.8444 |
| 298.15 | 10000.00 | 0.1990 | 1.0383 |
| 298.15 | 10000.00 | 0.2500 | 1.2018 |
| 298.15 | 10000.00 | 0.3000 | 1.3208 |
| 298.15 | 10000.00 | 0.3490 | 1.4106 |
| 298.15 | 10000.00 | 0.3990 | 1.4749 |
| 298.15 | 10000.00 | 0.4500 | 1.5125 |
| 298.15 | 10000.00 | 0.5000 | 1.5158 |
| 298.15 | 10000.00 | 0.5500 | 1.4955 |
| 298.15 | 10000.00 | 0.5990 | 1.4496 |
| 298.15 | 10000.00 | 0.6490 | 1.3787 |
| 298.15 | 10000.00 | 0.7000 | 1.275 |
| 298.15 | 10000.00 | 0.7490 | 1.148 |
| 298.15 | 10000.00 | 0.7990 | 0.9898 |
| 298.15 | 10000.00 | 0.8490 | 0.7905 |
| 298.15 | 10000.00 | 0.8990 | 0.5654 |
| 298.15 | 10000.00 | 0.9510 | 0.2856 |
| 298.15 | 5000.00 | 0.0510 | 0.3129 |
| 298.15 | 5000.00 | 0.0990 | 0.5974 |
| 298.15 | 5000.00 | 0.1490 | 0.8406 |
| 298.15 | 5000.00 | 0.1990 | 1.0367 |
| 298.15 | 5000.00 | 0.2510 | 1.1999 |
| 298.15 | 5000.00 | 0.3000 | 1.3219 |
| 298.15 | 5000.00 | 0.3490 | 1.4143 |
| 298.15 | 5000.00 | 0.4000 | 1.4824 |
| 298.15 | 5000.00 | 0.4510 | 1.5181 |
| 298.15 | 5000.00 | 0.5010 | 1.5228 |
| 298.15 | 5000.00 | 0.5510 | 1.4979 |
| 298.15 | 5000.00 | 0.6000 | 1.4538 |
| 298.15 | 5000.00 | 0.6500 | 1.3826 |
| 298.15 | 5000.00 | 0.7010 | 1.2758 |
| 298.15 | 5000.00 | 0.7490 | 1.1425 |
| 298.15 | 5000.00 | 0.8000 | 0.9874 |
| 298.15 | 5000.00 | 0.8500 | 0.7973 |
| 298.15 | 5000.00 | 0.8990 | 0.5709 |
| 333.15 | 10000.00 | 0.0510 | 0.4022 |
| 333.15 | 10000.00 | 0.0990 | 0.7037 |
| 333.15 | 10000.00 | 0.1500 | 0.9723 |
| 333.15 | 10000.00 | 0.2000 | 1.201 |
| 333.15 | 10000.00 | 0.2500 | 1.3767 |
| 333.15 | 10000.00 | 0.3000 | 1.5191 |
| 333.15 | 10000.00 | 0.3500 | 1.6258 |
| 333.15 | 10000.00 | 0.3990 | 1.7066 |
| 333.15 | 10000.00 | 0.4480 | 1.7488 |
| 333.15 | 10000.00 | 0.5000 | 1.7664 |
| 333.15 | 10000.00 | 0.5480 | 1.7514 |
| 333.15 | 10000.00 | 0.5990 | 1.6953 |
| 333.15 | 10000.00 | 0.6500 | 1.6052 |
| 333.15 | 10000.00 | 0.7000 | 1.4849 |
| 333.15 | 10000.00 | 0.7510 | 1.325 |
| 333.15 | 10000.00 | 0.8010 | 1.1322 |
| 333.15 | 10000.00 | 0.8500 | 0.8981 |
| 333.15 | 10000.00 | 0.8990 | 0.6270 |
| 333.15 | 10000.00 | 0.9490 | 0.3143 |
Mass density, kg/m3 [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Acetic acid, methyl ester (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 799.6 |
| 0.0968 | 811.3 |
| 0.1338 | 815.7 |
| 0.2033 | 824.2 |
| 0.2377 | 828.5 |
| 0.3169 | 838.3 |
| 0.3696 | 845.0 |
| 0.4037 | 849.3 |
| 0.4542 | 855.7 |
| 0.5026 | 861.9 |
| 0.5596 | 869.2 |
| 0.5975 | 874.0 |
| 0.6358 | 879.0 |
| 0.7047 | 888.0 |
| 0.8040 | 900.9 |
| 0.8537 | 907.5 |
| 0.9048 | 914.3 |
| 1.0000 | 927.3 |
Mass density, kg/m3 [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Acetic acid, methyl ester (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 799.6 |
| 0.0968 | 811.3 |
| 0.1338 | 815.7 |
| 0.2033 | 824.2 |
| 0.2377 | 828.5 |
| 0.3169 | 838.3 |
| 0.3696 | 845.0 |
| 0.4037 | 849.3 |
| 0.4542 | 855.7 |
| 0.5026 | 861.9 |
| 0.5596 | 869.2 |
| 0.5975 | 874.0 |
| 0.6358 | 879.0 |
| 0.7047 | 888.0 |
| 0.8040 | 900.9 |
| 0.8537 | 907.5 |
| 0.9048 | 914.3 |
| 1.0000 | 927.3 |
Boiling temperature at pressure P, K [ref]
Operational condition: Pressure, kPa = 300 (Liquid)
| Mole fraction of Acetic acid, methyl ester (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 402.55 |
| 0.0070 | 402.21 |
| 0.0160 | 401.63 |
| 0.0560 | 398.12 |
| 0.1290 | 392.77 |
| 0.1920 | 389.52 |
| 0.2610 | 385.81 |
| 0.3680 | 381.34 |
| 0.4210 | 379.48 |
| 0.5020 | 377.33 |
| 0.5300 | 376.49 |
| 0.5690 | 375.44 |
| 0.5910 | 375.09 |
| 0.6220 | 374.17 |
| 0.6630 | 373.05 |
| 0.7180 | 372.10 |
| 0.7520 | 371.32 |
| 0.7920 | 370.20 |
| 0.8770 | 368.29 |
| 0.9400 | 367.08 |
| 0.9640 | 366.61 |
| 0.9900 | 365.94 |
| 1.0000 | 365.85 |
Boiling temperature at pressure P, K [ref]
Operational condition: Pressure, kPa = 600 (Liquid)
| Mole fraction of Acetic acid, methyl ester (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 427.20 |
| 0.0050 | 426.94 |
| 0.0190 | 426.04 |
| 0.0340 | 424.74 |
| 0.0820 | 421.40 |
| 0.1930 | 415.56 |
| 0.2940 | 411.04 |
| 0.3510 | 408.83 |
| 0.4500 | 405.77 |
| 0.5290 | 403.40 |
| 0.5640 | 402.91 |
| 0.5870 | 402.09 |
| 0.6220 | 401.54 |
| 0.6480 | 400.86 |
| 0.6760 | 400.06 |
| 0.7100 | 399.48 |
| 0.7460 | 398.67 |
| 0.7810 | 397.65 |
| 0.8180 | 396.78 |
| 0.8590 | 395.81 |
| 0.8930 | 395.24 |
| 0.9190 | 394.69 |
| 0.9420 | 394.22 |
| 0.9760 | 393.49 |
| 0.9880 | 393.21 |
| 0.9950 | 393.13 |
| 1.0000 | 393.01 |
Boiling temperature at pressure P, K [ref]
Operational condition: Pressure, kPa = 300 (Liquid)
| Mole fraction of Acetic acid, methyl ester (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 402.55 |
| 0.0070 | 402.21 |
| 0.0160 | 401.63 |
| 0.0560 | 398.12 |
| 0.1290 | 392.77 |
| 0.1920 | 389.52 |
| 0.2610 | 385.81 |
| 0.3680 | 381.34 |
| 0.4210 | 379.48 |
| 0.5020 | 377.33 |
| 0.5300 | 376.49 |
| 0.5690 | 375.44 |
| 0.5910 | 375.09 |
| 0.6220 | 374.17 |
| 0.6630 | 373.05 |
| 0.7180 | 372.10 |
| 0.7520 | 371.32 |
| 0.7920 | 370.20 |
| 0.8770 | 368.29 |
| 0.9400 | 367.08 |
| 0.9640 | 366.61 |
| 0.9900 | 365.94 |
| 1.0000 | 365.85 |
Boiling temperature at pressure P, K [ref]
Operational condition: Pressure, kPa = 600 (Liquid)
| Mole fraction of Acetic acid, methyl ester (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 427.20 |
| 0.0050 | 426.94 |
| 0.0190 | 426.04 |
| 0.0340 | 424.74 |
| 0.0820 | 421.40 |
| 0.1930 | 415.56 |
| 0.2940 | 411.04 |
| 0.3510 | 408.83 |
| 0.4500 | 405.77 |
| 0.5290 | 403.40 |
| 0.5640 | 402.91 |
| 0.5870 | 402.09 |
| 0.6220 | 401.54 |
| 0.6480 | 400.86 |
| 0.6760 | 400.06 |
| 0.7100 | 399.48 |
| 0.7460 | 398.67 |
| 0.7810 | 397.65 |
| 0.8180 | 396.78 |
| 0.8590 | 395.81 |
| 0.8930 | 395.24 |
| 0.9190 | 394.69 |
| 0.9420 | 394.22 |
| 0.9760 | 393.49 |
| 0.9880 | 393.21 |
| 0.9950 | 393.13 |
| 1.0000 | 393.01 |
Sources
- Experimental Determination of Densities and Isobaric Vapor Liquid Equilibria of Methyl Acetate and Ethyl Acetate with Alcohols (C3 and C4) at 0.3 MPa
- Excess Molar Enthalpies of Methyl Acetate and (1-Propanol, 2-Propanol, 1-Butanol, 2-Butanol, and 1-Pentanol) at T = (298.15 and 308.15) K and P = (5.0 and 10.0) MPa
- Experimental Determination of Vapor Liquid Equilibria. Binary Systems of Methyl Acetate, Ethyl Acetate, and Propyl Acetate with 1-Propanol at 0.6 MPa