Operational condition: Pressure, kPa = 100 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Ethanol (1) - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 1 | Mole fraction of Ethanol (1) - Liquid mixture 1 |
298.15 | 0.0000 | 0.0072 | 0.9999 | 0.0000 |
303.15 | 0.0000 | 0.0099 | 0.9998 | 0.0000 |
308.15 | 0.0000 | 0.0122 | 0.9997 | 0.0000 |
293.15 | 0.0000 | 0.0063 | 0.9999 | 0.0000 |
293.15 | 0.0064 | 0.0000 | 0.9822 | 0.0178 |
293.15 | 0.0259 | 0.0101 | 0.9351 | 0.0649 |
293.15 | 0.0540 | 0.0163 | 0.8917 | 0.1083 |
293.15 | 0.1023 | 0.0250 | 0.8364 | 0.1636 |
293.15 | 0.1522 | 0.0348 | 0.7814 | 0.2178 |
293.15 | 0.1962 | 0.0520 | 0.7342 | 0.2627 |
293.15 | 0.2364 | 0.0641 | 0.6982 | 0.2959 |
293.15 | 0.2728 | 0.0796 | 0.6506 | 0.3390 |
298.15 | 0.0074 | 0.0000 | 0.9827 | 0.0173 |
298.15 | 0.0290 | 0.0122 | 0.9303 | 0.0697 |
298.15 | 0.0599 | 0.0171 | 0.8911 | 0.1089 |
298.15 | 0.1106 | 0.0258 | 0.8366 | 0.1634 |
298.15 | 0.1568 | 0.0385 | 0.7945 | 0.2050 |
298.15 | 0.1959 | 0.0502 | 0.7480 | 0.2492 |
298.15 | 0.2386 | 0.0633 | 0.7087 | 0.2872 |
298.15 | 0.2743 | 0.0779 | 0.6698 | 0.3230 |
303.15 | 0.0086 | 0.0106 | 0.9822 | 0.0178 |
303.15 | 0.0374 | 0.0161 | 0.9283 | 0.0717 |
303.15 | 0.0743 | 0.0207 | 0.8794 | 0.1206 |
303.15 | 0.1111 | 0.0294 | 0.8430 | 0.1570 |
303.15 | 0.1467 | 0.0370 | 0.8138 | 0.1862 |
303.15 | 0.1744 | 0.0476 | 0.7772 | 0.2228 |
303.15 | 0.2008 | 0.0548 | 0.7523 | 0.2456 |
303.15 | 0.2329 | 0.0639 | 0.7163 | 0.2787 |
303.15 | 0.2615 | 0.0763 | 0.6783 | 0.3142 |
308.15 | 0.0079 | 0.0000 | 0.9824 | 0.0176 |
308.15 | 0.0347 | 0.0103 | 0.9358 | 0.0642 |
308.15 | 0.0661 | 0.0171 | 0.8916 | 0.1084 |
308.15 | 0.1186 | 0.0299 | 0.8424 | 0.1576 |
308.15 | 0.1653 | 0.0414 | 0.7933 | 0.2067 |
308.15 | 0.2139 | 0.0608 | 0.7430 | 0.2538 |
308.15 | 0.2542 | 0.0754 | 0.6933 | 0.3003 |
308.15 | 0.2938 | 0.0906 | 0.6607 | 0.3317 |
Operational conditions:
Fixed | Measured | ||
---|---|---|---|
Mole fraction of n-Butyl ether (2) - Liquid mixture 1 | Mole fraction of Ethanol (1) - Liquid mixture 1 | Mole fraction of n-Butyl ether (2) - Liquid mixture 2 | Mole fraction of Ethanol (1) - Liquid mixture 2 |
0.9542 | 0.0098 | 0.0003 | 0.0162 |
0.9146 | 0.0288 | 0.0001 | 0.0582 |
0.8523 | 0.0758 | 0.0002 | 0.1199 |
0.7715 | 0.1392 | 0.0010 | 0.1798 |
0.6962 | 0.2047 | 0.0026 | 0.2414 |
0.6048 | 0.2605 | 0.0069 | 0.3031 |
0.4999 | 0.3354 | 0.0198 | 0.3725 |
0.3558 | 0.4118 | 0.0493 | 0.4362 |
0.2703 | 0.4503 | 0.0870 | 0.4596 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Ethanol (1) - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 1 | Mole fraction of Ethanol (1) - Liquid mixture 1 |
298.15 | 0.0000 | 0.0072 | 0.9999 | 0.0000 |
303.15 | 0.0000 | 0.0099 | 0.9998 | 0.0000 |
308.15 | 0.0000 | 0.0122 | 0.9997 | 0.0000 |
293.15 | 0.0000 | 0.0063 | 0.9999 | 0.0000 |
293.15 | 0.0064 | 0.0000 | 0.9822 | 0.0178 |
293.15 | 0.0259 | 0.0101 | 0.9351 | 0.0649 |
293.15 | 0.0540 | 0.0163 | 0.8917 | 0.1083 |
293.15 | 0.1023 | 0.0250 | 0.8364 | 0.1636 |
293.15 | 0.1522 | 0.0348 | 0.7814 | 0.2178 |
293.15 | 0.1962 | 0.0520 | 0.7342 | 0.2627 |
293.15 | 0.2364 | 0.0641 | 0.6982 | 0.2959 |
293.15 | 0.2728 | 0.0796 | 0.6506 | 0.3390 |
298.15 | 0.0074 | 0.0000 | 0.9827 | 0.0173 |
298.15 | 0.0290 | 0.0122 | 0.9303 | 0.0697 |
298.15 | 0.0599 | 0.0171 | 0.8911 | 0.1089 |
298.15 | 0.1106 | 0.0258 | 0.8366 | 0.1634 |
298.15 | 0.1568 | 0.0385 | 0.7945 | 0.2050 |
298.15 | 0.1959 | 0.0502 | 0.7480 | 0.2492 |
298.15 | 0.2386 | 0.0633 | 0.7087 | 0.2872 |
298.15 | 0.2743 | 0.0779 | 0.6698 | 0.3230 |
303.15 | 0.0086 | 0.0106 | 0.9822 | 0.0178 |
303.15 | 0.0374 | 0.0161 | 0.9283 | 0.0717 |
303.15 | 0.0743 | 0.0207 | 0.8794 | 0.1206 |
303.15 | 0.1111 | 0.0294 | 0.8430 | 0.1570 |
303.15 | 0.1467 | 0.0370 | 0.8138 | 0.1862 |
303.15 | 0.1744 | 0.0476 | 0.7772 | 0.2228 |
303.15 | 0.2008 | 0.0548 | 0.7523 | 0.2456 |
303.15 | 0.2329 | 0.0639 | 0.7163 | 0.2787 |
303.15 | 0.2615 | 0.0763 | 0.6783 | 0.3142 |
308.15 | 0.0079 | 0.0000 | 0.9824 | 0.0176 |
308.15 | 0.0347 | 0.0103 | 0.9358 | 0.0642 |
308.15 | 0.0661 | 0.0171 | 0.8916 | 0.1084 |
308.15 | 0.1186 | 0.0299 | 0.8424 | 0.1576 |
308.15 | 0.1653 | 0.0414 | 0.7933 | 0.2067 |
308.15 | 0.2139 | 0.0608 | 0.7430 | 0.2538 |
308.15 | 0.2542 | 0.0754 | 0.6933 | 0.3003 |
308.15 | 0.2938 | 0.0906 | 0.6607 | 0.3317 |
Operational conditions:
Fixed | Measured | ||
---|---|---|---|
Mole fraction of n-Butyl ether (2) - Liquid mixture 1 | Mole fraction of Ethanol (1) - Liquid mixture 1 | Mole fraction of n-Butyl ether (2) - Liquid mixture 2 | Mole fraction of Ethanol (1) - Liquid mixture 2 |
0.9542 | 0.0098 | 0.0003 | 0.0162 |
0.9146 | 0.0288 | 0.0001 | 0.0582 |
0.8523 | 0.0758 | 0.0002 | 0.1199 |
0.7715 | 0.1392 | 0.0010 | 0.1798 |
0.6962 | 0.2047 | 0.0026 | 0.2414 |
0.6048 | 0.2605 | 0.0069 | 0.3031 |
0.4999 | 0.3354 | 0.0198 | 0.3725 |
0.3558 | 0.4118 | 0.0493 | 0.4362 |
0.2703 | 0.4503 | 0.0870 | 0.4596 |