Operational condition: Pressure, kPa = 101.3 (Gas)
Mole fraction of Acetic acid, trifluoro-, ethyl ester (1) - Liquid | Mole fraction of Acetic acid, trifluoro-, ethyl ester (1) - Gas |
---|---|
0.8740 | 0.9770 |
0.8573 | 0.9690 |
0.8453 | 0.9590 |
0.8042 | 0.9470 |
0.7502 | 0.8990 |
0.7840 | 0.9270 |
0.7055 | 0.8690 |
0.6872 | 0.8550 |
0.6764 | 0.8270 |
0.6300 | 0.8020 |
0.6153 | 0.7840 |
0.5494 | 0.7060 |
0.5932 | 0.7540 |
0.5180 | 0.6600 |
0.4802 | 0.6020 |
0.4678 | 0.5800 |
0.4505 | 0.5650 |
0.4293 | 0.5290 |
0.4090 | 0.5000 |
0.3892 | 0.4580 |
0.3615 | 0.4350 |
0.3344 | 0.3750 |
0.2990 | 0.3290 |
0.2633 | 0.2890 |
0.2324 | 0.2390 |
0.1991 | 0.1970 |
0.1552 | 0.1340 |
0.1228 | 0.1010 |
0.1069 | 0.0840 |
0.0904 | 0.0650 |
0.0740 | 0.0470 |
0.0612 | 0.0390 |
0.0502 | 0.0320 |
0.0402 | 0.0250 |
0.0321 | 0.0190 |
0.0180 | 0.0100 |
Operational condition: Pressure, kPa = 101.3 (Gas)
Mole fraction of Acetic acid, trifluoro-, ethyl ester (1) - Liquid | Mole fraction of Acetic acid, trifluoro-, ethyl ester (1) - Gas |
---|---|
0.8740 | 0.9770 |
0.8573 | 0.9690 |
0.8453 | 0.9590 |
0.8042 | 0.9470 |
0.7502 | 0.8990 |
0.7840 | 0.9270 |
0.7055 | 0.8690 |
0.6872 | 0.8550 |
0.6764 | 0.8270 |
0.6300 | 0.8020 |
0.6153 | 0.7840 |
0.5494 | 0.7060 |
0.5932 | 0.7540 |
0.5180 | 0.6600 |
0.4802 | 0.6020 |
0.4678 | 0.5800 |
0.4505 | 0.5650 |
0.4293 | 0.5290 |
0.4090 | 0.5000 |
0.3892 | 0.4580 |
0.3615 | 0.4350 |
0.3344 | 0.3750 |
0.2990 | 0.3290 |
0.2633 | 0.2890 |
0.2324 | 0.2390 |
0.1991 | 0.1970 |
0.1552 | 0.1340 |
0.1228 | 0.1010 |
0.1069 | 0.0840 |
0.0904 | 0.0650 |
0.0740 | 0.0470 |
0.0612 | 0.0390 |
0.0502 | 0.0320 |
0.0402 | 0.0250 |
0.0321 | 0.0190 |
0.0180 | 0.0100 |
Operational condition: Pressure, kPa = 101.3 (Gas)
Mole fraction of Acetic acid, trifluoro-, ethyl ester (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
1.0000 | 335.65 |
0.8740 | 337.83 |
0.8573 | 338.27 |
0.8453 | 338.52 |
0.8042 | 339.13 |
0.7502 | 340.52 |
0.7840 | 339.63 |
0.7055 | 341.46 |
0.6872 | 341.97 |
0.6764 | 342.47 |
0.6300 | 343.03 |
0.6153 | 343.43 |
0.5494 | 344.65 |
0.5932 | 344.13 |
0.5180 | 345.18 |
0.4802 | 345.95 |
0.4678 | 346.28 |
0.4505 | 346.63 |
0.4293 | 346.95 |
0.3892 | 347.55 |
0.3615 | 347.77 |
0.3344 | 348.10 |
0.2990 | 348.35 |
0.2633 | 348.56 |
0.2324 | 348.65 |
0.1991 | 348.62 |
0.1552 | 348.28 |
0.1228 | 347.88 |
0.1069 | 347.57 |
0.0904 | 347.23 |
0.0740 | 346.87 |
0.0612 | 346.67 |
0.0502 | 346.46 |
0.0402 | 346.23 |
0.0321 | 346.03 |
0.0180 | 345.60 |
0.0000 | 344.95 |
0.4090 | 347.25 |
Operational condition: Pressure, kPa = 101.3 (Gas)
Mole fraction of Acetic acid, trifluoro-, ethyl ester (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
1.0000 | 335.65 |
0.8740 | 337.83 |
0.8573 | 338.27 |
0.8453 | 338.52 |
0.8042 | 339.13 |
0.7502 | 340.52 |
0.7840 | 339.63 |
0.7055 | 341.46 |
0.6872 | 341.97 |
0.6764 | 342.47 |
0.6300 | 343.03 |
0.6153 | 343.43 |
0.5494 | 344.65 |
0.5932 | 344.13 |
0.5180 | 345.18 |
0.4802 | 345.95 |
0.4678 | 346.28 |
0.4505 | 346.63 |
0.4293 | 346.95 |
0.3892 | 347.55 |
0.3615 | 347.77 |
0.3344 | 348.10 |
0.2990 | 348.35 |
0.2633 | 348.56 |
0.2324 | 348.65 |
0.1991 | 348.62 |
0.1552 | 348.28 |
0.1228 | 347.88 |
0.1069 | 347.57 |
0.0904 | 347.23 |
0.0740 | 346.87 |
0.0612 | 346.67 |
0.0502 | 346.46 |
0.0402 | 346.23 |
0.0321 | 346.03 |
0.0180 | 345.60 |
0.0000 | 344.95 |
0.4090 | 347.25 |