Operational condition: Pressure, kPa = 101.32 (Liquid mixture 1)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Linalool (3) - Liquid mixture 1 | Mole fraction of Ethanol (1) - Liquid mixture 1 | Mole fraction of Linalool (3) - Liquid mixture 2 | Mole fraction of Ethanol (1) - Liquid mixture 2 |
293.15 | 0.1180 | 0.3520 | 0.0100 | 0.2230 |
293.15 | 0.1840 | 0.3640 | 0.0010 | 0.1900 |
293.15 | 0.3030 | 0.3440 | 0.0010 | 0.1440 |
293.15 | 0.3680 | 0.3020 | 0.0010 | 0.1130 |
293.15 | 0.4190 | 0.2680 | 0.0010 | 0.1030 |
293.15 | 0.4800 | 0.2260 | 0.0010 | 0.0890 |
293.15 | 0.5620 | 0.1650 | 0.0010 | 0.0570 |
293.15 | 0.6010 | 0.1320 | 0.0010 | 0.0420 |
293.15 | 0.6660 | 0.0790 | 0.0010 | 0.0250 |
293.15 | 0.7450 | 0.0000 | 0.0010 | 0.0000 |
303.15 | 0.1090 | 0.3280 | 0.0110 | 0.2150 |
303.15 | 0.1980 | 0.3420 | 0.0010 | 0.1710 |
303.15 | 0.2380 | 0.3350 | 0.0010 | 0.1560 |
303.15 | 0.3190 | 0.3210 | 0.0010 | 0.1430 |
303.15 | 0.3790 | 0.2990 | 0.0010 | 0.1330 |
303.15 | 0.4840 | 0.2380 | 0.0010 | 0.0880 |
303.15 | 0.5780 | 0.1730 | 0.0010 | 0.0600 |
303.15 | 0.6780 | 0.0840 | 0.0010 | 0.0250 |
303.15 | 0.7850 | 0.0000 | 0.0010 | 0.0000 |
313.15 | 0.1060 | 0.3090 | 0.0130 | 0.2120 |
313.15 | 0.2350 | 0.3280 | 0.0010 | 0.1680 |
313.15 | 0.3260 | 0.3070 | 0.0010 | 0.1170 |
313.15 | 0.4620 | 0.2400 | 0.0010 | 0.0860 |
313.15 | 0.5580 | 0.1770 | 0.0010 | 0.0580 |
313.15 | 0.6560 | 0.0930 | 0.0010 | 0.0280 |
313.15 | 0.7560 | 0.0000 | 0.0010 | 0.0000 |
323.15 | 0.1260 | 0.2980 | 0.0110 | 0.1980 |
323.15 | 0.2310 | 0.3160 | 0.0010 | 0.1640 |
323.15 | 0.3400 | 0.2920 | 0.0010 | 0.1230 |
323.15 | 0.4420 | 0.2490 | 0.0010 | 0.0840 |
323.15 | 0.5440 | 0.1720 | 0.0010 | 0.0510 |
323.15 | 0.6210 | 0.1010 | 0.0010 | 0.0240 |
323.15 | 0.7410 | 0.0000 | 0.0010 | 0.0000 |
Operational condition: Pressure, kPa = 101 (Gas)
Fixed | Measured | |
---|---|---|
Mole fraction of Ethanol (1) - Liquid | Mole fraction of Linalool (3) - Liquid | Mole fraction of Ethanol (1) - Gas |
0.0101 | 1.5400e-06 | 0.0858 |
0.0110 | 1.8500e-06 | 0.0888 |
0.0120 | 1.6600e-06 | 0.0891 |
0.0560 | 0.0000 | 0.3466 |
0.0562 | 0.0000 | 0.3315 |
0.0618 | 0.0000 | 0.3679 |
0.0957 | 0.0000 | 0.4915 |
0.0979 | 0.0000 | 0.4749 |
0.1007 | 0.0000 | 0.4762 |
0.1035 | 0.0000 | 0.5833 |
0.1350 | 0.0000 | 0.4866 |
0.1365 | 0.0000 | 0.4813 |
0.1992 | 0.0000 | 0.5594 |
0.2066 | 0.0001 | 0.5529 |
0.2083 | 0.0000 | 0.5546 |
0.2665 | 0.0000 | 0.5953 |
0.2936 | 0.0000 | 0.5499 |
0.3049 | 0.0000 | 0.5981 |
0.3861 | 0.0000 | 0.6704 |
0.3940 | 0.0000 | 0.6315 |
0.4217 | 0.0000 | 0.6574 |
0.5365 | 0.0000 | 0.6841 |
0.5444 | 0.0000 | 0.7038 |
0.5516 | 0.0000 | 0.6548 |
0.8815 | 0.0000 | 0.8896 |
0.8937 | 0.0000 | 0.9166 |
0.9068 | 0.0000 | 0.8627 |
Operational condition: Pressure, kPa = 101 (Gas)
Fixed | Measured | |
---|---|---|
Mole fraction of Ethanol (1) - Liquid | Mole fraction of Linalool (3) - Liquid | Mole fraction of Linalool (3) - Gas |
0.0101 | 1.5400e-06 | 0.0002 |
0.0110 | 1.8500e-06 | 0.0002 |
0.0120 | 1.6600e-06 | 0.0002 |
0.0560 | 0.0000 | 0.0001 |
0.0562 | 0.0000 | 0.0001 |
0.0618 | 0.0000 | 0.0001 |
0.0957 | 0.0000 | 0.0000 |
0.0979 | 0.0000 | 0.0000 |
0.1007 | 0.0000 | 0.0000 |
0.1035 | 0.0000 | 0.0000 |
0.1350 | 0.0000 | 0.0000 |
0.1365 | 0.0000 | 0.0000 |
0.1992 | 0.0000 | 0.0000 |
0.2066 | 0.0001 | 0.0000 |
0.2083 | 0.0000 | 6.8900e-06 |
0.2665 | 0.0000 | 4.1500e-06 |
0.2936 | 0.0000 | 7.6800e-06 |
0.3049 | 0.0000 | 3.9200e-06 |
0.3861 | 0.0000 | 1.6600e-06 |
0.3940 | 0.0000 | 1.9800e-06 |
0.4217 | 0.0000 | 1.8600e-06 |
0.5365 | 0.0000 | 1.5000e-06 |
0.5444 | 0.0000 | 1.6800e-06 |
0.5516 | 0.0000 | 1.3700e-06 |
0.8815 | 0.0000 | 0.0000 |
0.8937 | 0.0000 | 0.0000 |
0.9068 | 0.0000 | 0.0000 |
Operational condition: Pressure, kPa = 101.32 (Liquid mixture 1)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Linalool (3) - Liquid mixture 1 | Mole fraction of Ethanol (1) - Liquid mixture 1 | Mole fraction of Linalool (3) - Liquid mixture 2 | Mole fraction of Ethanol (1) - Liquid mixture 2 |
293.15 | 0.1180 | 0.3520 | 0.0100 | 0.2230 |
293.15 | 0.1840 | 0.3640 | 0.0010 | 0.1900 |
293.15 | 0.3030 | 0.3440 | 0.0010 | 0.1440 |
293.15 | 0.3680 | 0.3020 | 0.0010 | 0.1130 |
293.15 | 0.4190 | 0.2680 | 0.0010 | 0.1030 |
293.15 | 0.4800 | 0.2260 | 0.0010 | 0.0890 |
293.15 | 0.5620 | 0.1650 | 0.0010 | 0.0570 |
293.15 | 0.6010 | 0.1320 | 0.0010 | 0.0420 |
293.15 | 0.6660 | 0.0790 | 0.0010 | 0.0250 |
293.15 | 0.7450 | 0.0000 | 0.0010 | 0.0000 |
303.15 | 0.1090 | 0.3280 | 0.0110 | 0.2150 |
303.15 | 0.1980 | 0.3420 | 0.0010 | 0.1710 |
303.15 | 0.2380 | 0.3350 | 0.0010 | 0.1560 |
303.15 | 0.3190 | 0.3210 | 0.0010 | 0.1430 |
303.15 | 0.3790 | 0.2990 | 0.0010 | 0.1330 |
303.15 | 0.4840 | 0.2380 | 0.0010 | 0.0880 |
303.15 | 0.5780 | 0.1730 | 0.0010 | 0.0600 |
303.15 | 0.6780 | 0.0840 | 0.0010 | 0.0250 |
303.15 | 0.7850 | 0.0000 | 0.0010 | 0.0000 |
313.15 | 0.1060 | 0.3090 | 0.0130 | 0.2120 |
313.15 | 0.2350 | 0.3280 | 0.0010 | 0.1680 |
313.15 | 0.3260 | 0.3070 | 0.0010 | 0.1170 |
313.15 | 0.4620 | 0.2400 | 0.0010 | 0.0860 |
313.15 | 0.5580 | 0.1770 | 0.0010 | 0.0580 |
313.15 | 0.6560 | 0.0930 | 0.0010 | 0.0280 |
313.15 | 0.7560 | 0.0000 | 0.0010 | 0.0000 |
323.15 | 0.1260 | 0.2980 | 0.0110 | 0.1980 |
323.15 | 0.2310 | 0.3160 | 0.0010 | 0.1640 |
323.15 | 0.3400 | 0.2920 | 0.0010 | 0.1230 |
323.15 | 0.4420 | 0.2490 | 0.0010 | 0.0840 |
323.15 | 0.5440 | 0.1720 | 0.0010 | 0.0510 |
323.15 | 0.6210 | 0.1010 | 0.0010 | 0.0240 |
323.15 | 0.7410 | 0.0000 | 0.0010 | 0.0000 |
Operational condition: Pressure, kPa = 101 (Gas)
Fixed | Measured | |
---|---|---|
Mole fraction of Ethanol (1) - Liquid | Mole fraction of Linalool (3) - Liquid | Mole fraction of Ethanol (1) - Gas |
0.0101 | 1.5400e-06 | 0.0858 |
0.0110 | 1.8500e-06 | 0.0888 |
0.0120 | 1.6600e-06 | 0.0891 |
0.0560 | 0.0000 | 0.3466 |
0.0562 | 0.0000 | 0.3315 |
0.0618 | 0.0000 | 0.3679 |
0.0957 | 0.0000 | 0.4915 |
0.0979 | 0.0000 | 0.4749 |
0.1007 | 0.0000 | 0.4762 |
0.1035 | 0.0000 | 0.5833 |
0.1350 | 0.0000 | 0.4866 |
0.1365 | 0.0000 | 0.4813 |
0.1992 | 0.0000 | 0.5594 |
0.2066 | 0.0001 | 0.5529 |
0.2083 | 0.0000 | 0.5546 |
0.2665 | 0.0000 | 0.5953 |
0.2936 | 0.0000 | 0.5499 |
0.3049 | 0.0000 | 0.5981 |
0.3861 | 0.0000 | 0.6704 |
0.3940 | 0.0000 | 0.6315 |
0.4217 | 0.0000 | 0.6574 |
0.5365 | 0.0000 | 0.6841 |
0.5444 | 0.0000 | 0.7038 |
0.5516 | 0.0000 | 0.6548 |
0.8815 | 0.0000 | 0.8896 |
0.8937 | 0.0000 | 0.9166 |
0.9068 | 0.0000 | 0.8627 |
Operational condition: Pressure, kPa = 101 (Gas)
Fixed | Measured | |
---|---|---|
Mole fraction of Ethanol (1) - Liquid | Mole fraction of Linalool (3) - Liquid | Mole fraction of Linalool (3) - Gas |
0.0101 | 1.5400e-06 | 0.0002 |
0.0110 | 1.8500e-06 | 0.0002 |
0.0120 | 1.6600e-06 | 0.0002 |
0.0560 | 0.0000 | 0.0001 |
0.0562 | 0.0000 | 0.0001 |
0.0618 | 0.0000 | 0.0001 |
0.0957 | 0.0000 | 0.0000 |
0.0979 | 0.0000 | 0.0000 |
0.1007 | 0.0000 | 0.0000 |
0.1035 | 0.0000 | 0.0000 |
0.1350 | 0.0000 | 0.0000 |
0.1365 | 0.0000 | 0.0000 |
0.1992 | 0.0000 | 0.0000 |
0.2066 | 0.0001 | 0.0000 |
0.2083 | 0.0000 | 6.8900e-06 |
0.2665 | 0.0000 | 4.1500e-06 |
0.2936 | 0.0000 | 7.6800e-06 |
0.3049 | 0.0000 | 3.9200e-06 |
0.3861 | 0.0000 | 1.6600e-06 |
0.3940 | 0.0000 | 1.9800e-06 |
0.4217 | 0.0000 | 1.8600e-06 |
0.5365 | 0.0000 | 1.5000e-06 |
0.5444 | 0.0000 | 1.6800e-06 |
0.5516 | 0.0000 | 1.3700e-06 |
0.8815 | 0.0000 | 0.0000 |
0.8937 | 0.0000 | 0.0000 |
0.9068 | 0.0000 | 0.0000 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of Ethanol (1) - Liquid | Mole fraction of Linalool (3) - Liquid | Boiling temperature at pressure P, K - Liquid |
0.0101 | 1.5400e-06 | 370.18 |
0.0110 | 1.8500e-06 | 369.93 |
0.0120 | 1.6600e-06 | 369.98 |
0.0560 | 0.0000 | 362.27 |
0.0562 | 0.0000 | 362.31 |
0.0618 | 0.0000 | 362.10 |
0.0957 | 0.0000 | 357.56 |
0.0979 | 0.0000 | 359.26 |
0.1007 | 0.0000 | 359.17 |
0.1035 | 0.0000 | 359.15 |
0.1350 | 0.0000 | 357.70 |
0.1365 | 0.0000 | 357.65 |
0.1992 | 0.0000 | 356.21 |
0.2066 | 0.0001 | 356.03 |
0.2083 | 0.0000 | 356.05 |
0.2665 | 0.0000 | 354.76 |
0.2936 | 0.0000 | 355.70 |
0.3049 | 0.0000 | 354.68 |
0.3861 | 0.0000 | 353.81 |
0.3940 | 0.0000 | 353.77 |
0.4217 | 0.0000 | 353.78 |
0.5365 | 0.0000 | 352.84 |
0.5444 | 0.0000 | 352.76 |
0.5516 | 0.0000 | 352.70 |
0.8815 | 0.0000 | 351.43 |
0.8937 | 0.0000 | 351.37 |
0.9068 | 0.0000 | 351.39 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Mole fraction of Ethanol (1) - Liquid | Mole fraction of Linalool (3) - Liquid | Boiling temperature at pressure P, K - Liquid |
0.0101 | 1.5400e-06 | 370.18 |
0.0110 | 1.8500e-06 | 369.93 |
0.0120 | 1.6600e-06 | 369.98 |
0.0560 | 0.0000 | 362.27 |
0.0562 | 0.0000 | 362.31 |
0.0618 | 0.0000 | 362.10 |
0.0957 | 0.0000 | 357.56 |
0.0979 | 0.0000 | 359.26 |
0.1007 | 0.0000 | 359.17 |
0.1035 | 0.0000 | 359.15 |
0.1350 | 0.0000 | 357.70 |
0.1365 | 0.0000 | 357.65 |
0.1992 | 0.0000 | 356.21 |
0.2066 | 0.0001 | 356.03 |
0.2083 | 0.0000 | 356.05 |
0.2665 | 0.0000 | 354.76 |
0.2936 | 0.0000 | 355.70 |
0.3049 | 0.0000 | 354.68 |
0.3861 | 0.0000 | 353.81 |
0.3940 | 0.0000 | 353.77 |
0.4217 | 0.0000 | 353.78 |
0.5365 | 0.0000 | 352.84 |
0.5444 | 0.0000 | 352.76 |
0.5516 | 0.0000 | 352.70 |
0.8815 | 0.0000 | 351.43 |
0.8937 | 0.0000 | 351.37 |
0.9068 | 0.0000 | 351.39 |