Operational condition: Pressure, kPa = 101.2 (Liquid mixture 1)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Water (3) - Liquid mixture 1 | Temperature, K - Liquid mixture 1 | Mole fraction of Isopropyl Alcohol (1) - Liquid mixture 1 |
| 0.0460 | 288.15 | 0.1781 |
| 0.0486 | 298.15 | 0.1759 |
| 0.0693 | 308.15 | 0.0801 |
| 0.0754 | 298.15 | 0.2199 |
| 0.0795 | 288.15 | 0.2635 |
| 0.0912 | 308.15 | 0.1378 |
| 0.1042 | 288.15 | 0.2839 |
| 0.1075 | 288.15 | 0.2912 |
| 0.1148 | 298.15 | 0.2698 |
| 0.1178 | 308.15 | 0.2162 |
| 0.1203 | 308.15 | 0.2290 |
| 0.1405 | 308.15 | 0.2500 |
| 0.1520 | 288.15 | 0.3355 |
| 0.1648 | 298.15 | 0.3173 |
| 0.1675 | 308.15 | 0.2675 |
| 0.1897 | 288.15 | 0.3621 |
| 0.1903 | 308.15 | 0.2805 |
| 0.2206 | 298.15 | 0.3489 |
| 0.2235 | 288.15 | 0.3744 |
| 0.2241 | 308.15 | 0.2929 |
| 0.2707 | 288.15 | 0.3870 |
| 0.2712 | 308.15 | 0.3107 |
| 0.2933 | 298.15 | 0.3671 |
| 0.3093 | 288.15 | 0.3962 |
| 0.3317 | 308.15 | 0.3144 |
| 0.3335 | 298.15 | 0.3680 |
| 0.3562 | 288.15 | 0.3893 |
| 0.3726 | 298.15 | 0.3630 |
| 0.3901 | 308.15 | 0.3043 |
| 0.3945 | 288.15 | 0.3835 |
| 0.4137 | 298.15 | 0.3540 |
| 0.4367 | 288.15 | 0.3741 |
| 0.4510 | 298.15 | 0.3434 |
| 0.4592 | 308.15 | 0.2864 |
| 0.4802 | 288.15 | 0.3601 |
| 0.4922 | 298.15 | 0.3277 |
| 0.5297 | 288.15 | 0.3412 |
| 0.5358 | 298.15 | 0.3104 |
| 0.5380 | 308.15 | 0.2573 |
| 0.5811 | 298.15 | 0.2902 |
| 0.5903 | 288.15 | 0.3105 |
| 0.6157 | 308.15 | 0.2235 |
| 0.6328 | 298.15 | 0.2623 |
| 0.6507 | 288.15 | 0.2762 |
| 0.6883 | 298.15 | 0.2323 |
| 0.6914 | 308.15 | 0.1841 |
| 0.6989 | 288.15 | 0.2475 |
| 0.7405 | 288.15 | 0.2220 |
| 0.7415 | 298.15 | 0.2036 |
| 0.7585 | 288.15 | 0.2151 |
| 0.7604 | 308.15 | 0.1462 |
| 0.7837 | 298.15 | 0.1793 |
| 0.7906 | 288.15 | 0.1917 |
| 0.8151 | 298.15 | 0.1605 |
| 0.8170 | 308.15 | 0.1143 |
| 0.8358 | 298.15 | 0.1481 |
| 0.8795 | 308.15 | 0.0768 |
| 0.9058 | 308.15 | 0.0617 |
Operational condition: Pressure, kPa = 101.2 (Liquid mixture 1)
| Fixed | Measured | |||
|---|---|---|---|---|
| Temperature, K - Liquid mixture 1 | Mole fraction of Water (3) - Liquid mixture 1 | Mole fraction of Isopropyl Alcohol (1) - Liquid mixture 1 | Mole fraction of Isopropyl Alcohol (1) - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 2 |
| 288.15 | 0.8265 | 0.1636 | 0.3929 | 0.3079 |
| 288.15 | 0.7684 | 0.2030 | 0.3890 | 0.3623 |
| 288.15 | 0.8850 | 0.1073 | 0.3812 | 0.2476 |
| 288.15 | 0.9200 | 0.0780 | 0.3691 | 0.1972 |
| 288.15 | 0.9562 | 0.0428 | 0.3218 | 0.1347 |
| 288.15 | 0.9785 | 0.0215 | 0.2660 | 0.0768 |
| 288.15 | 0.9858 | 0.0142 | 0.1813 | 0.0270 |
| 288.15 | 0.5147 | 0.3504 | 0.3504 | 0.5147 |
| 298.15 | 0.8456 | 0.1408 | 0.3642 | 0.3692 |
| 298.15 | 0.8856 | 0.1052 | 0.3697 | 0.3291 |
| 298.15 | 0.9197 | 0.0730 | 0.3692 | 0.2876 |
| 298.15 | 0.9415 | 0.0528 | 0.3652 | 0.2496 |
| 298.15 | 0.9616 | 0.0349 | 0.3506 | 0.2164 |
| 298.15 | 0.9732 | 0.0268 | 0.3038 | 0.1401 |
| 298.15 | 0.9800 | 0.0200 | 0.2751 | 0.1053 |
| 298.15 | 0.9831 | 0.0169 | 0.0765 | 0.0136 |
| 298.15 | 0.5479 | 0.3038 | 0.3038 | 0.5479 |
| 308.15 | 0.7259 | 0.1600 | 0.3175 | 0.2965 |
| 308.15 | 0.7847 | 0.1323 | 0.3008 | 0.2442 |
| 308.15 | 0.8430 | 0.0999 | 0.2730 | 0.1715 |
| 308.15 | 0.8650 | 0.0848 | 0.2501 | 0.1480 |
| 308.15 | 0.9251 | 0.0456 | 0.1610 | 0.0900 |
| 308.15 | 0.9500 | 0.0300 | 0.1191 | 0.0699 |
| 308.15 | 0.5287 | 0.2618 | 0.2618 | 0.5287 |
Operational condition: Pressure, kPa = 101.2 (Liquid mixture 1)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Water (3) - Liquid mixture 1 | Temperature, K - Liquid mixture 1 | Mole fraction of Isopropyl Alcohol (1) - Liquid mixture 1 |
| 0.0460 | 288.15 | 0.1781 |
| 0.0486 | 298.15 | 0.1759 |
| 0.0693 | 308.15 | 0.0801 |
| 0.0754 | 298.15 | 0.2199 |
| 0.0795 | 288.15 | 0.2635 |
| 0.0912 | 308.15 | 0.1378 |
| 0.1042 | 288.15 | 0.2839 |
| 0.1075 | 288.15 | 0.2912 |
| 0.1148 | 298.15 | 0.2698 |
| 0.1178 | 308.15 | 0.2162 |
| 0.1203 | 308.15 | 0.2290 |
| 0.1405 | 308.15 | 0.2500 |
| 0.1520 | 288.15 | 0.3355 |
| 0.1648 | 298.15 | 0.3173 |
| 0.1675 | 308.15 | 0.2675 |
| 0.1897 | 288.15 | 0.3621 |
| 0.1903 | 308.15 | 0.2805 |
| 0.2206 | 298.15 | 0.3489 |
| 0.2235 | 288.15 | 0.3744 |
| 0.2241 | 308.15 | 0.2929 |
| 0.2707 | 288.15 | 0.3870 |
| 0.2712 | 308.15 | 0.3107 |
| 0.2933 | 298.15 | 0.3671 |
| 0.3093 | 288.15 | 0.3962 |
| 0.3317 | 308.15 | 0.3144 |
| 0.3335 | 298.15 | 0.3680 |
| 0.3562 | 288.15 | 0.3893 |
| 0.3726 | 298.15 | 0.3630 |
| 0.3901 | 308.15 | 0.3043 |
| 0.3945 | 288.15 | 0.3835 |
| 0.4137 | 298.15 | 0.3540 |
| 0.4367 | 288.15 | 0.3741 |
| 0.4510 | 298.15 | 0.3434 |
| 0.4592 | 308.15 | 0.2864 |
| 0.4802 | 288.15 | 0.3601 |
| 0.4922 | 298.15 | 0.3277 |
| 0.5297 | 288.15 | 0.3412 |
| 0.5358 | 298.15 | 0.3104 |
| 0.5380 | 308.15 | 0.2573 |
| 0.5811 | 298.15 | 0.2902 |
| 0.5903 | 288.15 | 0.3105 |
| 0.6157 | 308.15 | 0.2235 |
| 0.6328 | 298.15 | 0.2623 |
| 0.6507 | 288.15 | 0.2762 |
| 0.6883 | 298.15 | 0.2323 |
| 0.6914 | 308.15 | 0.1841 |
| 0.6989 | 288.15 | 0.2475 |
| 0.7405 | 288.15 | 0.2220 |
| 0.7415 | 298.15 | 0.2036 |
| 0.7585 | 288.15 | 0.2151 |
| 0.7604 | 308.15 | 0.1462 |
| 0.7837 | 298.15 | 0.1793 |
| 0.7906 | 288.15 | 0.1917 |
| 0.8151 | 298.15 | 0.1605 |
| 0.8170 | 308.15 | 0.1143 |
| 0.8358 | 298.15 | 0.1481 |
| 0.8795 | 308.15 | 0.0768 |
| 0.9058 | 308.15 | 0.0617 |
Operational condition: Pressure, kPa = 101.2 (Liquid mixture 1)
| Fixed | Measured | |||
|---|---|---|---|---|
| Temperature, K - Liquid mixture 1 | Mole fraction of Water (3) - Liquid mixture 1 | Mole fraction of Isopropyl Alcohol (1) - Liquid mixture 1 | Mole fraction of Isopropyl Alcohol (1) - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 2 |
| 288.15 | 0.8265 | 0.1636 | 0.3929 | 0.3079 |
| 288.15 | 0.7684 | 0.2030 | 0.3890 | 0.3623 |
| 288.15 | 0.8850 | 0.1073 | 0.3812 | 0.2476 |
| 288.15 | 0.9200 | 0.0780 | 0.3691 | 0.1972 |
| 288.15 | 0.9562 | 0.0428 | 0.3218 | 0.1347 |
| 288.15 | 0.9785 | 0.0215 | 0.2660 | 0.0768 |
| 288.15 | 0.9858 | 0.0142 | 0.1813 | 0.0270 |
| 288.15 | 0.5147 | 0.3504 | 0.3504 | 0.5147 |
| 298.15 | 0.8456 | 0.1408 | 0.3642 | 0.3692 |
| 298.15 | 0.8856 | 0.1052 | 0.3697 | 0.3291 |
| 298.15 | 0.9197 | 0.0730 | 0.3692 | 0.2876 |
| 298.15 | 0.9415 | 0.0528 | 0.3652 | 0.2496 |
| 298.15 | 0.9616 | 0.0349 | 0.3506 | 0.2164 |
| 298.15 | 0.9732 | 0.0268 | 0.3038 | 0.1401 |
| 298.15 | 0.9800 | 0.0200 | 0.2751 | 0.1053 |
| 298.15 | 0.9831 | 0.0169 | 0.0765 | 0.0136 |
| 298.15 | 0.5479 | 0.3038 | 0.3038 | 0.5479 |
| 308.15 | 0.7259 | 0.1600 | 0.3175 | 0.2965 |
| 308.15 | 0.7847 | 0.1323 | 0.3008 | 0.2442 |
| 308.15 | 0.8430 | 0.0999 | 0.2730 | 0.1715 |
| 308.15 | 0.8650 | 0.0848 | 0.2501 | 0.1480 |
| 308.15 | 0.9251 | 0.0456 | 0.1610 | 0.0900 |
| 308.15 | 0.9500 | 0.0300 | 0.1191 | 0.0699 |
| 308.15 | 0.5287 | 0.2618 | 0.2618 | 0.5287 |