Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid | Mole fraction of Toluene (1) - Liquid | Mole fraction of Ethanol, 2-methoxy- (2) - Liquid | Mole fraction of Ethanol, 2-methoxy- (2) - Gas | Mole fraction of Toluene (1) - Gas |
385.71 | 0.2675 | 0.6339 | 0.4867 | 0.5082 |
386.48 | 0.5161 | 0.2716 | 0.2289 | 0.7539 |
387.12 | 0.3709 | 0.4234 | 0.3291 | 0.6573 |
387.45 | 0.6314 | 0.1429 | 0.1414 | 0.8373 |
392.03 | 0.1874 | 0.6134 | 0.5389 | 0.4471 |
392.36 | 0.1377 | 0.7126 | 0.6197 | 0.3689 |
393.73 | 0.4842 | 0.0997 | 0.0955 | 0.8559 |
396.04 | 0.3321 | 0.2597 | 0.2111 | 0.7392 |
397.77 | 0.1254 | 0.6142 | 0.6154 | 0.3598 |
400.69 | 0.1905 | 0.4113 | 0.4285 | 0.5238 |
403.32 | 0.2908 | 0.0980 | 0.0763 | 0.8256 |
406.67 | 0.0785 | 0.5339 | 0.6355 | 0.3097 |
409.80 | 0.1812 | 0.2116 | 0.2492 | 0.6373 |
411.62 | 0.1084 | 0.3604 | 0.4449 | 0.4502 |
412.53 | 0.1880 | 0.0805 | 0.0783 | 0.7621 |
414.71 | 0.1077 | 0.2959 | 0.3797 | 0.4867 |
421.75 | 0.0431 | 0.3683 | 0.6022 | 0.2398 |
430.41 | 0.0654 | 0.1249 | 0.2015 | 0.4892 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid | Mole fraction of Toluene (1) - Liquid | Mole fraction of Ethanol, 2-methoxy- (2) - Liquid | Mole fraction of Ethanol, 2-methoxy- (2) - Gas | Mole fraction of Toluene (1) - Gas |
385.71 | 0.2675 | 0.6339 | 0.4867 | 0.5082 |
386.48 | 0.5161 | 0.2716 | 0.2289 | 0.7539 |
387.12 | 0.3709 | 0.4234 | 0.3291 | 0.6573 |
387.45 | 0.6314 | 0.1429 | 0.1414 | 0.8373 |
392.03 | 0.1874 | 0.6134 | 0.5389 | 0.4471 |
392.36 | 0.1377 | 0.7126 | 0.6197 | 0.3689 |
393.73 | 0.4842 | 0.0997 | 0.0955 | 0.8559 |
396.04 | 0.3321 | 0.2597 | 0.2111 | 0.7392 |
397.77 | 0.1254 | 0.6142 | 0.6154 | 0.3598 |
400.69 | 0.1905 | 0.4113 | 0.4285 | 0.5238 |
403.32 | 0.2908 | 0.0980 | 0.0763 | 0.8256 |
406.67 | 0.0785 | 0.5339 | 0.6355 | 0.3097 |
409.80 | 0.1812 | 0.2116 | 0.2492 | 0.6373 |
411.62 | 0.1084 | 0.3604 | 0.4449 | 0.4502 |
412.53 | 0.1880 | 0.0805 | 0.0783 | 0.7621 |
414.71 | 0.1077 | 0.2959 | 0.3797 | 0.4867 |
421.75 | 0.0431 | 0.3683 | 0.6022 | 0.2398 |
430.41 | 0.0654 | 0.1249 | 0.2015 | 0.4892 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of Toluene (1) - Liquid | Mole fraction of Ethanol, 2-methoxy- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
0.2675 | 0.6339 | 385.71 |
0.5161 | 0.2716 | 386.48 |
0.3709 | 0.4234 | 387.12 |
0.6314 | 0.1429 | 387.45 |
0.1874 | 0.6134 | 392.03 |
0.1377 | 0.7126 | 392.36 |
0.4842 | 0.0997 | 393.73 |
0.3321 | 0.2597 | 396.04 |
0.1254 | 0.6142 | 397.77 |
0.1905 | 0.4113 | 400.69 |
0.2908 | 0.0980 | 403.32 |
0.0785 | 0.5339 | 406.67 |
0.1812 | 0.2116 | 409.80 |
0.1084 | 0.3604 | 411.62 |
0.1880 | 0.0805 | 412.53 |
0.1077 | 0.2959 | 414.71 |
0.0431 | 0.3683 | 421.75 |
0.0654 | 0.1249 | 430.41 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of Toluene (1) - Liquid | Mole fraction of Ethanol, 2-methoxy- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
0.2675 | 0.6339 | 385.71 |
0.5161 | 0.2716 | 386.48 |
0.3709 | 0.4234 | 387.12 |
0.6314 | 0.1429 | 387.45 |
0.1874 | 0.6134 | 392.03 |
0.1377 | 0.7126 | 392.36 |
0.4842 | 0.0997 | 393.73 |
0.3321 | 0.2597 | 396.04 |
0.1254 | 0.6142 | 397.77 |
0.1905 | 0.4113 | 400.69 |
0.2908 | 0.0980 | 403.32 |
0.0785 | 0.5339 | 406.67 |
0.1812 | 0.2116 | 409.80 |
0.1084 | 0.3604 | 411.62 |
0.1880 | 0.0805 | 412.53 |
0.1077 | 0.2959 | 414.71 |
0.0431 | 0.3683 | 421.75 |
0.0654 | 0.1249 | 430.41 |