Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 2 | Mole fraction of n-Hexane (2) - Liquid mixture 1 | Mole fraction of Benzene (1) - Liquid mixture 1 | Mole fraction of Benzene (1) - Liquid mixture 2 | Mole fraction of n-Hexane (2) - Liquid mixture 2 |
298.15 | 0.7965 | 0.0938 | 0.0615 | 0.0773 |
298.15 | 0.7102 | 0.1607 | 0.1132 | 0.0929 |
298.15 | 0.6378 | 0.2141 | 0.1514 | 0.1133 |
298.15 | 0.5693 | 0.2655 | 0.2092 | 0.1025 |
298.15 | 0.4923 | 0.3037 | 0.2521 | 0.1278 |
298.15 | 0.4491 | 0.3341 | 0.2708 | 0.1588 |
298.15 | 0.3967 | 0.3551 | 0.3109 | 0.1722 |
298.15 | 0.3385 | 0.3605 | 0.3375 | 0.1991 |
308.15 | 0.7802 | 0.0963 | 0.0679 | 0.0735 |
308.15 | 0.7121 | 0.1538 | 0.1154 | 0.0997 |
308.15 | 0.6223 | 0.2178 | 0.1645 | 0.1086 |
308.15 | 0.5529 | 0.2557 | 0.1988 | 0.1257 |
308.15 | 0.4909 | 0.2912 | 0.2371 | 0.1492 |
308.15 | 0.4326 | 0.3177 | 0.2708 | 0.1708 |
308.15 | 0.3786 | 0.3354 | 0.2998 | 0.1966 |
308.15 | 0.3259 | 0.3440 | 0.3240 | 0.2295 |
318.15 | 0.7789 | 0.0876 | 0.0601 | 0.0997 |
318.15 | 0.6932 | 0.1508 | 0.1085 | 0.1134 |
318.15 | 0.6159 | 0.2031 | 0.1532 | 0.1291 |
318.15 | 0.5456 | 0.2454 | 0.1939 | 0.1472 |
318.15 | 0.4818 | 0.2711 | 0.2303 | 0.1682 |
318.15 | 0.4232 | 0.3013 | 0.2619 | 0.1929 |
318.15 | 0.3632 | 0.3155 | 0.2886 | 0.2231 |
318.15 | 0.3172 | 0.3193 | 0.3081 | 0.2596 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 2 | Mole fraction of n-Hexane (2) - Liquid mixture 1 | Mole fraction of Benzene (1) - Liquid mixture 1 | Mole fraction of Benzene (1) - Liquid mixture 2 | Mole fraction of n-Hexane (2) - Liquid mixture 2 |
298.15 | 0.7965 | 0.0938 | 0.0615 | 0.0773 |
298.15 | 0.7102 | 0.1607 | 0.1132 | 0.0929 |
298.15 | 0.6378 | 0.2141 | 0.1514 | 0.1133 |
298.15 | 0.5693 | 0.2655 | 0.2092 | 0.1025 |
298.15 | 0.4923 | 0.3037 | 0.2521 | 0.1278 |
298.15 | 0.4491 | 0.3341 | 0.2708 | 0.1588 |
298.15 | 0.3967 | 0.3551 | 0.3109 | 0.1722 |
298.15 | 0.3385 | 0.3605 | 0.3375 | 0.1991 |
308.15 | 0.7802 | 0.0963 | 0.0679 | 0.0735 |
308.15 | 0.7121 | 0.1538 | 0.1154 | 0.0997 |
308.15 | 0.6223 | 0.2178 | 0.1645 | 0.1086 |
308.15 | 0.5529 | 0.2557 | 0.1988 | 0.1257 |
308.15 | 0.4909 | 0.2912 | 0.2371 | 0.1492 |
308.15 | 0.4326 | 0.3177 | 0.2708 | 0.1708 |
308.15 | 0.3786 | 0.3354 | 0.2998 | 0.1966 |
308.15 | 0.3259 | 0.3440 | 0.3240 | 0.2295 |
318.15 | 0.7789 | 0.0876 | 0.0601 | 0.0997 |
318.15 | 0.6932 | 0.1508 | 0.1085 | 0.1134 |
318.15 | 0.6159 | 0.2031 | 0.1532 | 0.1291 |
318.15 | 0.5456 | 0.2454 | 0.1939 | 0.1472 |
318.15 | 0.4818 | 0.2711 | 0.2303 | 0.1682 |
318.15 | 0.4232 | 0.3013 | 0.2619 | 0.1929 |
318.15 | 0.3632 | 0.3155 | 0.2886 | 0.2231 |
318.15 | 0.3172 | 0.3193 | 0.3081 | 0.2596 |