Operational condition: Temperature, K = 332.95 (Gas)
| Mole fraction of Ethyl Acetate (2) - Liquid | Mole fraction of Ethyl Acetate (2) - Gas |
|---|---|
| 0.0204 | 0.1508 |
| 0.0402 | 0.2593 |
| 0.0606 | 0.3465 |
| 0.1035 | 0.4618 |
| 0.1494 | 0.5484 |
| 0.1999 | 0.6066 |
| 0.2486 | 0.6544 |
| 0.2996 | 0.6931 |
| 0.3440 | 0.7221 |
| 0.3888 | 0.7519 |
| 0.4350 | 0.7802 |
| 0.4800 | 0.8013 |
| 0.5242 | 0.8176 |
| 0.5698 | 0.8386 |
| 0.6146 | 0.8557 |
| 0.6595 | 0.8736 |
| 0.7043 | 0.8894 |
| 0.7479 | 0.9064 |
| 0.8306 | 0.9353 |
| 0.8844 | 0.9548 |
| 0.9297 | 0.9724 |
| 0.9748 | 0.9903 |
Operational condition: Pressure, kPa = 101 (Gas)
| Mole fraction of Ethyl Acetate (2) - Liquid | Mole fraction of Ethyl Acetate (2) - Gas |
|---|---|
| 0.0160 | 0.0530 |
| 0.0480 | 0.1480 |
| 0.0830 | 0.2370 |
| 0.1100 | 0.3060 |
| 0.1590 | 0.3970 |
| 0.2130 | 0.4840 |
| 0.2810 | 0.5650 |
| 0.3570 | 0.6410 |
| 0.4030 | 0.6810 |
| 0.4460 | 0.7120 |
| 0.4890 | 0.7450 |
| 0.5280 | 0.7710 |
| 0.5710 | 0.7940 |
| 0.6140 | 0.8170 |
| 0.6520 | 0.8360 |
| 0.6950 | 0.8580 |
| 0.7410 | 0.8800 |
| 0.7810 | 0.8990 |
| 0.8180 | 0.9160 |
| 0.8490 | 0.9300 |
| 0.8790 | 0.9450 |
Operational condition: Temperature, K = 332.95 (Gas)
| Mole fraction of Ethyl Acetate (2) - Liquid | Mole fraction of Ethyl Acetate (2) - Gas |
|---|---|
| 0.0204 | 0.1508 |
| 0.0402 | 0.2593 |
| 0.0606 | 0.3465 |
| 0.1035 | 0.4618 |
| 0.1494 | 0.5484 |
| 0.1999 | 0.6066 |
| 0.2486 | 0.6544 |
| 0.2996 | 0.6931 |
| 0.3440 | 0.7221 |
| 0.3888 | 0.7519 |
| 0.4350 | 0.7802 |
| 0.4800 | 0.8013 |
| 0.5242 | 0.8176 |
| 0.5698 | 0.8386 |
| 0.6146 | 0.8557 |
| 0.6595 | 0.8736 |
| 0.7043 | 0.8894 |
| 0.7479 | 0.9064 |
| 0.8306 | 0.9353 |
| 0.8844 | 0.9548 |
| 0.9297 | 0.9724 |
| 0.9748 | 0.9903 |
Operational condition: Pressure, kPa = 101 (Gas)
| Mole fraction of Ethyl Acetate (2) - Liquid | Mole fraction of Ethyl Acetate (2) - Gas |
|---|---|
| 0.0160 | 0.0530 |
| 0.0480 | 0.1480 |
| 0.0830 | 0.2370 |
| 0.1100 | 0.3060 |
| 0.1590 | 0.3970 |
| 0.2130 | 0.4840 |
| 0.2810 | 0.5650 |
| 0.3570 | 0.6410 |
| 0.4030 | 0.6810 |
| 0.4460 | 0.7120 |
| 0.4890 | 0.7450 |
| 0.5280 | 0.7710 |
| 0.5710 | 0.7940 |
| 0.6140 | 0.8170 |
| 0.6520 | 0.8360 |
| 0.6950 | 0.8580 |
| 0.7410 | 0.8800 |
| 0.7810 | 0.8990 |
| 0.8180 | 0.9160 |
| 0.8490 | 0.9300 |
| 0.8790 | 0.9450 |
Operational conditions:
| Mole fraction of Ethyl Acetate (2) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.0520 | 1.3925 |
| 0.1040 | 1.3914 |
| 0.1550 | 1.3901 |
| 0.2060 | 1.3889 |
| 0.2580 | 1.3875 |
| 0.3080 | 1.3861 |
| 0.3590 | 1.3847 |
| 0.4100 | 1.3833 |
| 0.4600 | 1.3817 |
| 0.5100 | 1.3803 |
| 0.5600 | 1.3784 |
| 0.6090 | 1.3767 |
| 0.6590 | 1.3751 |
| 0.7080 | 1.373 |
| 0.7570 | 1.3711 |
| 0.8060 | 1.3688 |
| 0.8550 | 1.3667 |
| 0.9040 | 1.3643 |
| 0.9520 | 1.3619 |
Operational conditions:
| Mole fraction of Ethyl Acetate (2) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.0520 | 1.3925 |
| 0.1040 | 1.3914 |
| 0.1550 | 1.3901 |
| 0.2060 | 1.3889 |
| 0.2580 | 1.3875 |
| 0.3080 | 1.3861 |
| 0.3590 | 1.3847 |
| 0.4100 | 1.3833 |
| 0.4600 | 1.3817 |
| 0.5100 | 1.3803 |
| 0.5600 | 1.3784 |
| 0.6090 | 1.3767 |
| 0.6590 | 1.3751 |
| 0.7080 | 1.373 |
| 0.7570 | 1.3711 |
| 0.8060 | 1.3688 |
| 0.8550 | 1.3667 |
| 0.9040 | 1.3643 |
| 0.9520 | 1.3619 |
Operational conditions:
| Mole fraction of Ethyl Acetate (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0520 | 797.95 |
| 0.1040 | 797.48 |
| 0.1550 | 796.99 |
| 0.2060 | 796.46 |
| 0.2580 | 795.94 |
| 0.3080 | 795.35 |
| 0.3590 | 794.79 |
| 0.4100 | 794.16 |
| 0.4600 | 793.58 |
| 0.5100 | 793.0 |
| 0.5600 | 791.89 |
| 0.6090 | 791.22 |
| 0.6590 | 790.55 |
| 0.7080 | 789.9 |
| 0.7570 | 789.15 |
| 0.8060 | 788.4 |
| 0.8550 | 787.68 |
| 0.9040 | 786.87 |
| 0.9520 | 786.08 |
Operational conditions:
| Mole fraction of Ethyl Acetate (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0490 | 802.3 |
| 0.1010 | 806.8 |
| 0.1530 | 811.5 |
| 0.2020 | 816.0 |
| 0.2510 | 820.6 |
| 0.3000 | 825.2 |
| 0.3500 | 829.9 |
| 0.4010 | 834.7 |
| 0.4510 | 839.5 |
| 0.5010 | 844.3 |
| 0.5500 | 849.0 |
| 0.6000 | 853.8 |
| 0.6500 | 858.8 |
| 0.7000 | 863.7 |
| 0.7510 | 868.9 |
| 0.8010 | 873.8 |
| 0.8500 | 878.7 |
| 0.9000 | 883.8 |
| 0.9500 | 888.9 |
Operational conditions:
| Mole fraction of Ethyl Acetate (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0520 | 797.95 |
| 0.1040 | 797.48 |
| 0.1550 | 796.99 |
| 0.2060 | 796.46 |
| 0.2580 | 795.94 |
| 0.3080 | 795.35 |
| 0.3590 | 794.79 |
| 0.4100 | 794.16 |
| 0.4600 | 793.58 |
| 0.5100 | 793.0 |
| 0.5600 | 791.89 |
| 0.6090 | 791.22 |
| 0.6590 | 790.55 |
| 0.7080 | 789.9 |
| 0.7570 | 789.15 |
| 0.8060 | 788.4 |
| 0.8550 | 787.68 |
| 0.9040 | 786.87 |
| 0.9520 | 786.08 |
Operational conditions:
| Mole fraction of Ethyl Acetate (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0490 | 802.3 |
| 0.1010 | 806.8 |
| 0.1530 | 811.5 |
| 0.2020 | 816.0 |
| 0.2510 | 820.6 |
| 0.3000 | 825.2 |
| 0.3500 | 829.9 |
| 0.4010 | 834.7 |
| 0.4510 | 839.5 |
| 0.5010 | 844.3 |
| 0.5500 | 849.0 |
| 0.6000 | 853.8 |
| 0.6500 | 858.8 |
| 0.7000 | 863.7 |
| 0.7510 | 868.9 |
| 0.8010 | 873.8 |
| 0.8500 | 878.7 |
| 0.9000 | 883.8 |
| 0.9500 | 888.9 |
Operational conditions:
| Mole fraction of Ethyl Acetate (2) - Liquid | Speed of sound, m/s - Liquid |
|---|---|
| 0.0520 | 1186.09 |
| 0.1040 | 1184.42 |
| 0.1550 | 1182.91 |
| 0.2060 | 1181.47 |
| 0.2580 | 1179.29 |
| 0.3080 | 1177.47 |
| 0.3590 | 1175.62 |
| 0.4100 | 1174.15 |
| 0.4600 | 1171.26 |
| 0.5100 | 1169.01 |
| 0.5600 | 1165.22 |
| 0.6090 | 1162.97 |
| 0.6590 | 1160.41 |
| 0.7080 | 1158.25 |
| 0.7570 | 1155.32 |
| 0.8060 | 1152.79 |
| 0.8550 | 1150.1 |
| 0.9040 | 1147.39 |
| 0.9520 | 1144.67 |
Operational conditions:
| Mole fraction of Ethyl Acetate (2) - Liquid | Speed of sound, m/s - Liquid |
|---|---|
| 0.0520 | 1186.09 |
| 0.1040 | 1184.42 |
| 0.1550 | 1182.91 |
| 0.2060 | 1181.47 |
| 0.2580 | 1179.29 |
| 0.3080 | 1177.47 |
| 0.3590 | 1175.62 |
| 0.4100 | 1174.15 |
| 0.4600 | 1171.26 |
| 0.5100 | 1169.01 |
| 0.5600 | 1165.22 |
| 0.6090 | 1162.97 |
| 0.6590 | 1160.41 |
| 0.7080 | 1158.25 |
| 0.7570 | 1155.32 |
| 0.8060 | 1152.79 |
| 0.8550 | 1150.1 |
| 0.9040 | 1147.39 |
| 0.9520 | 1144.67 |
Operational condition: Pressure, kPa = 101 (Gas)
| Mole fraction of Ethyl Acetate (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0160 | 379.96 |
| 0.0480 | 377.93 |
| 0.0830 | 375.96 |
| 0.1100 | 374.37 |
| 0.1590 | 371.87 |
| 0.2130 | 369.40 |
| 0.2810 | 366.75 |
| 0.3570 | 364.08 |
| 0.4030 | 362.67 |
| 0.4460 | 361.47 |
| 0.4890 | 360.19 |
| 0.5280 | 359.24 |
| 0.5710 | 358.30 |
| 0.6140 | 357.26 |
| 0.6520 | 356.99 |
| 0.6950 | 355.59 |
| 0.7410 | 354.72 |
| 0.7810 | 353.95 |
| 0.8180 | 353.29 |
| 0.8490 | 352.73 |
| 0.8790 | 352.20 |
Operational condition: Pressure, kPa = 101 (Gas)
| Mole fraction of Ethyl Acetate (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0160 | 379.96 |
| 0.0480 | 377.93 |
| 0.0830 | 375.96 |
| 0.1100 | 374.37 |
| 0.1590 | 371.87 |
| 0.2130 | 369.40 |
| 0.2810 | 366.75 |
| 0.3570 | 364.08 |
| 0.4030 | 362.67 |
| 0.4460 | 361.47 |
| 0.4890 | 360.19 |
| 0.5280 | 359.24 |
| 0.5710 | 358.30 |
| 0.6140 | 357.26 |
| 0.6520 | 356.99 |
| 0.6950 | 355.59 |
| 0.7410 | 354.72 |
| 0.7810 | 353.95 |
| 0.8180 | 353.29 |
| 0.8490 | 352.73 |
| 0.8790 | 352.20 |