Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 2 | Mole fraction of Acetic acid (2) - Liquid mixture 1 | Mole fraction of Acetic acid ethenyl ester (1) - Liquid mixture 1 | Mole fraction of Acetic acid (2) - Liquid mixture 2 | Mole fraction of Acetic acid ethenyl ester (1) - Liquid mixture 2 |
298.15 | 0.0224 | 0.0043 | 0.0298 | 0.9134 |
298.15 | 0.1297 | 0.0254 | 0.1896 | 0.5643 |
298.15 | 0.1436 | 0.0298 | 0.2096 | 0.5076 |
308.15 | 0.0230 | 0.0047 | 0.0320 | 0.9070 |
308.15 | 0.0405 | 0.0053 | 0.0679 | 0.8470 |
308.15 | 0.0502 | 0.0072 | 0.0798 | 0.8250 |
308.15 | 0.0580 | 0.0085 | 0.0933 | 0.7995 |
308.15 | 0.0765 | 0.0117 | 0.1263 | 0.7308 |
308.15 | 0.0864 | 0.0134 | 0.1430 | 0.6896 |
308.15 | 0.0975 | 0.0160 | 0.1550 | 0.6570 |
308.15 | 0.1074 | 0.0192 | 0.1731 | 0.6068 |
298.15 | 0.0383 | 0.0051 | 0.0572 | 0.8692 |
308.15 | 0.1185 | 0.0230 | 0.1814 | 0.5813 |
308.15 | 0.1319 | 0.0272 | 0.2017 | 0.5252 |
308.15 | 0.1443 | 0.0338 | 0.2140 | 0.4861 |
298.15 | 0.0487 | 0.0067 | 0.0712 | 0.8450 |
298.15 | 0.0550 | 0.0075 | 0.0873 | 0.8142 |
298.15 | 0.0698 | 0.0095 | 0.1180 | 0.7534 |
298.15 | 0.0811 | 0.0119 | 0.1312 | 0.7225 |
298.15 | 0.0948 | 0.0153 | 0.1490 | 0.6763 |
298.15 | 0.1013 | 0.0176 | 0.1577 | 0.6529 |
298.15 | 0.1161 | 0.0212 | 0.1729 | 0.6092 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 2 | Mole fraction of Acetic acid (2) - Liquid mixture 1 | Mole fraction of Acetic acid ethenyl ester (1) - Liquid mixture 1 | Mole fraction of Acetic acid (2) - Liquid mixture 2 | Mole fraction of Acetic acid ethenyl ester (1) - Liquid mixture 2 |
298.15 | 0.0224 | 0.0043 | 0.0298 | 0.9134 |
298.15 | 0.1297 | 0.0254 | 0.1896 | 0.5643 |
298.15 | 0.1436 | 0.0298 | 0.2096 | 0.5076 |
308.15 | 0.0230 | 0.0047 | 0.0320 | 0.9070 |
308.15 | 0.0405 | 0.0053 | 0.0679 | 0.8470 |
308.15 | 0.0502 | 0.0072 | 0.0798 | 0.8250 |
308.15 | 0.0580 | 0.0085 | 0.0933 | 0.7995 |
308.15 | 0.0765 | 0.0117 | 0.1263 | 0.7308 |
308.15 | 0.0864 | 0.0134 | 0.1430 | 0.6896 |
308.15 | 0.0975 | 0.0160 | 0.1550 | 0.6570 |
308.15 | 0.1074 | 0.0192 | 0.1731 | 0.6068 |
298.15 | 0.0383 | 0.0051 | 0.0572 | 0.8692 |
308.15 | 0.1185 | 0.0230 | 0.1814 | 0.5813 |
308.15 | 0.1319 | 0.0272 | 0.2017 | 0.5252 |
308.15 | 0.1443 | 0.0338 | 0.2140 | 0.4861 |
298.15 | 0.0487 | 0.0067 | 0.0712 | 0.8450 |
298.15 | 0.0550 | 0.0075 | 0.0873 | 0.8142 |
298.15 | 0.0698 | 0.0095 | 0.1180 | 0.7534 |
298.15 | 0.0811 | 0.0119 | 0.1312 | 0.7225 |
298.15 | 0.0948 | 0.0153 | 0.1490 | 0.6763 |
298.15 | 0.1013 | 0.0176 | 0.1577 | 0.6529 |
298.15 | 0.1161 | 0.0212 | 0.1729 | 0.6092 |