Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 2 | Mole fraction of 1-Butanol (1) - Liquid mixture 2 | Mole fraction of 1-Butanol (1) - Liquid mixture 1 | Mole fraction of Water (3) - Liquid mixture 1 |
288.15 | 0.9970 | 0.0000 | 0.0000 | 0.0593 |
288.15 | 0.9903 | 0.0018 | 0.0680 | 0.1156 |
288.15 | 0.9884 | 0.0037 | 0.1061 | 0.1382 |
288.15 | 0.9878 | 0.0043 | 0.1836 | 0.2018 |
288.15 | 0.9873 | 0.0047 | 0.2494 | 0.2545 |
288.15 | 0.9864 | 0.0056 | 0.2888 | 0.2748 |
288.15 | 0.9851 | 0.0068 | 0.3249 | 0.3296 |
288.15 | 0.9851 | 0.0068 | 0.3481 | 0.3522 |
288.15 | 0.9837 | 0.0080 | 0.3942 | 0.3873 |
288.15 | 0.9829 | 0.0087 | 0.4123 | 0.4255 |
288.15 | 0.9802 | 0.0198 | 0.5018 | 0.4982 |
318.15 | 0.9972 | 0.0000 | 0.0000 | 0.0752 |
318.15 | 0.9911 | 0.0010 | 0.0669 | 0.1275 |
318.15 | 0.9906 | 0.0015 | 0.1071 | 0.1522 |
318.15 | 0.9893 | 0.0027 | 0.1866 | 0.2174 |
318.15 | 0.9888 | 0.0031 | 0.2427 | 0.2706 |
318.15 | 0.9880 | 0.0040 | 0.2761 | 0.2963 |
318.15 | 0.9878 | 0.0041 | 0.3168 | 0.3395 |
318.15 | 0.9877 | 0.0041 | 0.3479 | 0.3752 |
318.15 | 0.9853 | 0.0065 | 0.3773 | 0.4077 |
318.15 | 0.9841 | 0.0076 | 0.3981 | 0.4347 |
318.15 | 0.9834 | 0.0166 | 0.4769 | 0.5231 |
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 2 | Mole fraction of 1-Butanol (1) - Liquid mixture 2 | Mole fraction of 1-Butanol (1) - Liquid mixture 1 | Mole fraction of Water (3) - Liquid mixture 1 |
288.15 | 0.9970 | 0.0000 | 0.0000 | 0.0593 |
288.15 | 0.9903 | 0.0018 | 0.0680 | 0.1156 |
288.15 | 0.9884 | 0.0037 | 0.1061 | 0.1382 |
288.15 | 0.9878 | 0.0043 | 0.1836 | 0.2018 |
288.15 | 0.9873 | 0.0047 | 0.2494 | 0.2545 |
288.15 | 0.9864 | 0.0056 | 0.2888 | 0.2748 |
288.15 | 0.9851 | 0.0068 | 0.3249 | 0.3296 |
288.15 | 0.9851 | 0.0068 | 0.3481 | 0.3522 |
288.15 | 0.9837 | 0.0080 | 0.3942 | 0.3873 |
288.15 | 0.9829 | 0.0087 | 0.4123 | 0.4255 |
288.15 | 0.9802 | 0.0198 | 0.5018 | 0.4982 |
318.15 | 0.9972 | 0.0000 | 0.0000 | 0.0752 |
318.15 | 0.9911 | 0.0010 | 0.0669 | 0.1275 |
318.15 | 0.9906 | 0.0015 | 0.1071 | 0.1522 |
318.15 | 0.9893 | 0.0027 | 0.1866 | 0.2174 |
318.15 | 0.9888 | 0.0031 | 0.2427 | 0.2706 |
318.15 | 0.9880 | 0.0040 | 0.2761 | 0.2963 |
318.15 | 0.9878 | 0.0041 | 0.3168 | 0.3395 |
318.15 | 0.9877 | 0.0041 | 0.3479 | 0.3752 |
318.15 | 0.9853 | 0.0065 | 0.3773 | 0.4077 |
318.15 | 0.9841 | 0.0076 | 0.3981 | 0.4347 |
318.15 | 0.9834 | 0.0166 | 0.4769 | 0.5231 |