Datasets
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Mole fraction (6)
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Tboil - Boiling temperature at pressure P, K (6)
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Vapor Liquid Equilibrium at Constant Temperature (3)
Mole fraction of Ethyl Acetate (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Gas)
| Mole fraction of Ethyl Acetate (2) - Liquid |
Mole fraction of Ethyl Acetate (2) - Gas |
| 0.0000 |
0.0000 |
| 0.0790 |
0.1250 |
| 0.1860 |
0.2630 |
| 0.2890 |
0.3600 |
| 0.3880 |
0.4460 |
| 0.4900 |
0.5300 |
| 0.5470 |
0.5770 |
| 0.5960 |
0.6140 |
| 0.6970 |
0.6960 |
| 0.8620 |
0.8430 |
| 0.9020 |
0.8860 |
| 1.0000 |
1.0000 |
Mole fraction of Ethyl Acetate (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Ethyl Acetate (2) - Liquid |
Mole fraction of Ethyl Acetate (2) - Gas |
| 352.45 |
0.0790 |
0.1250 |
| 350.65 |
0.1860 |
0.2630 |
| 349.95 |
0.2890 |
0.3600 |
| 349.15 |
0.3880 |
0.4460 |
| 348.75 |
0.4900 |
0.5300 |
| 348.55 |
0.5470 |
0.5770 |
| 348.45 |
0.5960 |
0.6140 |
| 348.45 |
0.6970 |
0.6960 |
| 348.85 |
0.8620 |
0.8430 |
| 349.15 |
0.9020 |
0.8860 |
Mole fraction of Ethyl Acetate (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Ethyl Acetate (2) - Liquid |
Mole fraction of Ethyl Acetate (2) - Gas |
| 0.0000 |
0.0000 |
| 0.0480 |
0.0800 |
| 0.1450 |
0.2150 |
| 0.2430 |
0.3160 |
| 0.3450 |
0.4080 |
| 0.4470 |
0.4920 |
| 0.5500 |
0.5770 |
| 0.6480 |
0.6530 |
| 0.7450 |
0.7360 |
| 0.8520 |
0.8300 |
| 0.9470 |
0.9380 |
| 1.0000 |
1.0000 |
Mole fraction of Ethyl Acetate (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Gas)
| Mole fraction of Ethyl Acetate (2) - Liquid |
Mole fraction of Ethyl Acetate (2) - Gas |
| 0.0000 |
0.0000 |
| 0.0790 |
0.1250 |
| 0.1860 |
0.2630 |
| 0.2890 |
0.3600 |
| 0.3880 |
0.4460 |
| 0.4900 |
0.5300 |
| 0.5470 |
0.5770 |
| 0.5960 |
0.6140 |
| 0.6970 |
0.6960 |
| 0.8620 |
0.8430 |
| 0.9020 |
0.8860 |
| 1.0000 |
1.0000 |
Mole fraction of Ethyl Acetate (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Ethyl Acetate (2) - Liquid |
Mole fraction of Ethyl Acetate (2) - Gas |
| 352.45 |
0.0790 |
0.1250 |
| 350.65 |
0.1860 |
0.2630 |
| 349.95 |
0.2890 |
0.3600 |
| 349.15 |
0.3880 |
0.4460 |
| 348.75 |
0.4900 |
0.5300 |
| 348.55 |
0.5470 |
0.5770 |
| 348.45 |
0.5960 |
0.6140 |
| 348.45 |
0.6970 |
0.6960 |
| 348.85 |
0.8620 |
0.8430 |
| 349.15 |
0.9020 |
0.8860 |
Mole fraction of Ethyl Acetate (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Ethyl Acetate (2) - Liquid |
Mole fraction of Ethyl Acetate (2) - Gas |
| 0.0000 |
0.0000 |
| 0.0480 |
0.0800 |
| 0.1450 |
0.2150 |
| 0.2430 |
0.3160 |
| 0.3450 |
0.4080 |
| 0.4470 |
0.4920 |
| 0.5500 |
0.5770 |
| 0.6480 |
0.6530 |
| 0.7450 |
0.7360 |
| 0.8520 |
0.8300 |
| 0.9470 |
0.9380 |
| 1.0000 |
1.0000 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Ethyl Acetate (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
354.65 |
| 0.0790 |
352.45 |
| 0.1860 |
350.65 |
| 0.2890 |
349.95 |
| 0.3880 |
349.15 |
| 0.4900 |
348.75 |
| 0.5470 |
348.55 |
| 0.5960 |
348.45 |
| 0.6970 |
348.45 |
| 0.8620 |
348.85 |
| 0.9020 |
349.15 |
| 1.0000 |
350.15 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Ethyl Acetate (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0790 |
352.45 |
| 0.1860 |
350.65 |
| 0.2890 |
349.95 |
| 0.3880 |
349.15 |
| 0.4900 |
348.75 |
| 0.5470 |
348.55 |
| 0.5960 |
348.45 |
| 0.6970 |
348.45 |
| 0.8620 |
348.85 |
| 0.9020 |
349.15 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Ethyl Acetate (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
354.30 |
| 0.0480 |
353.20 |
| 0.1450 |
351.60 |
| 0.2430 |
350.40 |
| 0.3450 |
349.60 |
| 0.4470 |
349.00 |
| 0.5500 |
348.70 |
| 0.6480 |
348.50 |
| 0.7450 |
348.60 |
| 0.8520 |
349.00 |
| 0.9470 |
349.50 |
| 1.0000 |
349.90 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Ethyl Acetate (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
354.65 |
| 0.0790 |
352.45 |
| 0.1860 |
350.65 |
| 0.2890 |
349.95 |
| 0.3880 |
349.15 |
| 0.4900 |
348.75 |
| 0.5470 |
348.55 |
| 0.5960 |
348.45 |
| 0.6970 |
348.45 |
| 0.8620 |
348.85 |
| 0.9020 |
349.15 |
| 1.0000 |
350.15 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Ethyl Acetate (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0790 |
352.45 |
| 0.1860 |
350.65 |
| 0.2890 |
349.95 |
| 0.3880 |
349.15 |
| 0.4900 |
348.75 |
| 0.5470 |
348.55 |
| 0.5960 |
348.45 |
| 0.6970 |
348.45 |
| 0.8620 |
348.85 |
| 0.9020 |
349.15 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
| Mole fraction of Ethyl Acetate (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
354.30 |
| 0.0480 |
353.20 |
| 0.1450 |
351.60 |
| 0.2430 |
350.40 |
| 0.3450 |
349.60 |
| 0.4470 |
349.00 |
| 0.5500 |
348.70 |
| 0.6480 |
348.50 |
| 0.7450 |
348.60 |
| 0.8520 |
349.00 |
| 0.9470 |
349.50 |
| 1.0000 |
349.90 |
Vapor Liquid Equilibrium at Constant Temperature
[ref]
Operational condition: Temperature, K =
333.15 (VLE)
| Fixed |
Measured |
| P [kPa] - VLE |
x1[mol/mol] of Ethyl Acetate (2) - Liquid |
y1[mol/mol] of Ethyl Acetate (2) - Vapour |
| 49.049 |
0.0000 |
0.0000 |
| 50.742 |
0.0487 |
0.0768 |
| 52.156 |
0.0887 |
0.1345 |
| 53.729 |
0.1500 |
0.2101 |
| 55.755 |
0.2234 |
0.2906 |
| 57.075 |
0.3089 |
0.3701 |
| 58.075 |
0.4040 |
0.4488 |
| 58.742 |
0.4984 |
0.5276 |
| 58.755 |
0.5735 |
0.5893 |
| 58.782 |
0.6384 |
0.6426 |
| 58.795 |
0.6530 |
0.6530 |
| 58.715 |
0.7073 |
0.6977 |
| 58.409 |
0.7779 |
0.7592 |
| 57.995 |
0.8410 |
0.8208 |
| 57.422 |
0.8963 |
0.8764 |
| 56.675 |
0.9593 |
0.9483 |
| 55.755 |
1.0000 |
1.0000 |
Vapor Liquid Equilibrium at Constant Temperature
[ref]
Operational condition: Temperature, K =
313.15 (VLE)
| P [kPa] - VLE |
x1[mol/mol] of Ethyl Acetate (2) - Liquid |
| 22.766 |
0.0000 |
| 23.433 |
0.0425 |
| 23.933 |
0.0814 |
| 24.589 |
0.1388 |
| 25.285 |
0.2135 |
| 25.853 |
0.3014 |
| 26.309 |
0.4017 |
| 26.594 |
0.5004 |
| 26.69 |
0.5960 |
| 26.612 |
0.6997 |
| 26.415 |
0.7874 |
| 26.114 |
0.8548 |
| 25.762 |
0.9127 |
| 25.525 |
0.9524 |
| 25.061 |
1.0000 |
Vapor Liquid Equilibrium at Constant Temperature
[ref]
Operational condition: Temperature, K =
353.15 (VLE)
| P [kPa] - VLE |
x1[mol/mol] of Ethyl Acetate (2) - Liquid |
| 96.369 |
0.0000 |
| 99.47 |
0.0425 |
| 101.79 |
0.0815 |
| 104.89 |
0.1389 |
| 108.23 |
0.2135 |
| 111.07 |
0.3014 |
| 113.429 |
0.4018 |
| 115.151 |
0.5004 |
| 115.98 |
0.5960 |
| 116.23 |
0.6996 |
| 115.78 |
0.7873 |
| 114.971 |
0.8547 |
| 113.811 |
0.9127 |
| 112.811 |
0.9527 |
| 111.36 |
1.0000 |
Sources