Operational condition: Temperature, K = 332.95 (Gas)
| Mole fraction of Ethyl Acetate (2) - Liquid | Mole fraction of Ethyl Acetate (2) - Gas |
|---|---|
| 0.0107 | 0.1794 |
| 0.0299 | 0.3960 |
| 0.0590 | 0.5503 |
| 0.0893 | 0.6506 |
| 0.1195 | 0.7166 |
| 0.1621 | 0.7711 |
| 0.1893 | 0.7909 |
| 0.2400 | 0.8293 |
| 0.2901 | 0.8561 |
| 0.3395 | 0.8764 |
| 0.3889 | 0.8897 |
| 0.4390 | 0.9033 |
| 0.4891 | 0.9134 |
| 0.5399 | 0.9258 |
| 0.5902 | 0.9343 |
| 0.6397 | 0.9378 |
| 0.6886 | 0.9508 |
| 0.7397 | 0.9586 |
| 0.7897 | 0.9647 |
| 0.8313 | 0.9719 |
| 0.8898 | 0.9807 |
| 0.9397 | 0.9897 |
| 0.9801 | 0.9961 |
Operational condition: Pressure, kPa = 101 (Gas)
| Mole fraction of Ethyl Acetate (2) - Liquid | Mole fraction of Ethyl Acetate (2) - Gas |
|---|---|
| 0.0220 | 0.1290 |
| 0.0400 | 0.1970 |
| 0.0570 | 0.2570 |
| 0.0730 | 0.3100 |
| 0.1010 | 0.3910 |
| 0.1430 | 0.4890 |
| 0.1730 | 0.5480 |
| 0.2150 | 0.6230 |
| 0.2740 | 0.6980 |
| 0.3490 | 0.7600 |
| 0.4300 | 0.8230 |
| 0.5070 | 0.8620 |
| 0.5660 | 0.8860 |
| 0.6350 | 0.9090 |
| 0.7110 | 0.9310 |
| 0.7430 | 0.9410 |
| 0.8190 | 0.9590 |
| 0.8940 | 0.9760 |
| 0.9370 | 0.9840 |
Operational condition: Temperature, K = 332.95 (Gas)
| Mole fraction of Ethyl Acetate (2) - Liquid | Mole fraction of Ethyl Acetate (2) - Gas |
|---|---|
| 0.0107 | 0.1794 |
| 0.0299 | 0.3960 |
| 0.0590 | 0.5503 |
| 0.0893 | 0.6506 |
| 0.1195 | 0.7166 |
| 0.1621 | 0.7711 |
| 0.1893 | 0.7909 |
| 0.2400 | 0.8293 |
| 0.2901 | 0.8561 |
| 0.3395 | 0.8764 |
| 0.3889 | 0.8897 |
| 0.4390 | 0.9033 |
| 0.4891 | 0.9134 |
| 0.5399 | 0.9258 |
| 0.5902 | 0.9343 |
| 0.6397 | 0.9378 |
| 0.6886 | 0.9508 |
| 0.7397 | 0.9586 |
| 0.7897 | 0.9647 |
| 0.8313 | 0.9719 |
| 0.8898 | 0.9807 |
| 0.9397 | 0.9897 |
| 0.9801 | 0.9961 |
Operational condition: Pressure, kPa = 101 (Gas)
| Mole fraction of Ethyl Acetate (2) - Liquid | Mole fraction of Ethyl Acetate (2) - Gas |
|---|---|
| 0.0220 | 0.1290 |
| 0.0400 | 0.1970 |
| 0.0570 | 0.2570 |
| 0.0730 | 0.3100 |
| 0.1010 | 0.3910 |
| 0.1430 | 0.4890 |
| 0.1730 | 0.5480 |
| 0.2150 | 0.6230 |
| 0.2740 | 0.6980 |
| 0.3490 | 0.7600 |
| 0.4300 | 0.8230 |
| 0.5070 | 0.8620 |
| 0.5660 | 0.8860 |
| 0.6350 | 0.9090 |
| 0.7110 | 0.9310 |
| 0.7430 | 0.9410 |
| 0.8190 | 0.9590 |
| 0.8940 | 0.9760 |
| 0.9370 | 0.9840 |
Operational conditions:
| Mole fraction of Ethyl Acetate (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0500 | 817.8 |
| 0.0990 | 820.9 |
| 0.1500 | 824.2 |
| 0.2000 | 827.5 |
| 0.2500 | 830.9 |
| 0.3000 | 834.4 |
| 0.3490 | 838.0 |
| 0.3990 | 841.7 |
| 0.4510 | 845.6 |
| 0.4990 | 849.4 |
| 0.5490 | 853.3 |
| 0.5980 | 857.3 |
| 0.6500 | 861.6 |
| 0.6990 | 865.8 |
| 0.7500 | 870.2 |
| 0.7930 | 874.2 |
| 0.8460 | 879.1 |
| 0.9000 | 884.2 |
| 0.9500 | 889.1 |
Operational conditions:
| Mole fraction of Ethyl Acetate (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0500 | 817.8 |
| 0.0990 | 820.9 |
| 0.1500 | 824.2 |
| 0.2000 | 827.5 |
| 0.2500 | 830.9 |
| 0.3000 | 834.4 |
| 0.3490 | 838.0 |
| 0.3990 | 841.7 |
| 0.4510 | 845.6 |
| 0.4990 | 849.4 |
| 0.5490 | 853.3 |
| 0.5980 | 857.3 |
| 0.6500 | 861.6 |
| 0.6990 | 865.8 |
| 0.7500 | 870.2 |
| 0.7930 | 874.2 |
| 0.8460 | 879.1 |
| 0.9000 | 884.2 |
| 0.9500 | 889.1 |
Operational condition: Pressure, kPa = 101 (Gas)
| Mole fraction of Ethyl Acetate (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0220 | 398.48 |
| 0.0400 | 396.72 |
| 0.0570 | 395.04 |
| 0.0730 | 393.35 |
| 0.1010 | 390.75 |
| 0.1430 | 386.95 |
| 0.1730 | 384.53 |
| 0.2150 | 380.95 |
| 0.2740 | 376.93 |
| 0.3490 | 373.00 |
| 0.4300 | 368.19 |
| 0.5070 | 364.92 |
| 0.5660 | 362.72 |
| 0.6350 | 360.39 |
| 0.7110 | 357.99 |
| 0.7430 | 356.86 |
| 0.8190 | 354.79 |
| 0.8940 | 352.60 |
| 0.9370 | 351.59 |
Operational condition: Pressure, kPa = 101 (Gas)
| Mole fraction of Ethyl Acetate (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0220 | 398.48 |
| 0.0400 | 396.72 |
| 0.0570 | 395.04 |
| 0.0730 | 393.35 |
| 0.1010 | 390.75 |
| 0.1430 | 386.95 |
| 0.1730 | 384.53 |
| 0.2150 | 380.95 |
| 0.2740 | 376.93 |
| 0.3490 | 373.00 |
| 0.4300 | 368.19 |
| 0.5070 | 364.92 |
| 0.5660 | 362.72 |
| 0.6350 | 360.39 |
| 0.7110 | 357.99 |
| 0.7430 | 356.86 |
| 0.8190 | 354.79 |
| 0.8940 | 352.60 |
| 0.9370 | 351.59 |