Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid mixture 1 | Mass fraction of Water (3) - Liquid mixture 1 | Mass fraction of 2,3-Butanediol (2) - Liquid mixture 1 |
298.15 | 0.9184 | 0.0000 |
298.15 | 0.8400 | 0.0734 |
298.15 | 0.8300 | 0.0808 |
298.15 | 0.8063 | 0.1013 |
298.15 | 0.7726 | 0.1243 |
298.15 | 0.7561 | 0.1317 |
298.15 | 0.7429 | 0.1400 |
298.15 | 0.7247 | 0.1448 |
298.15 | 0.7109 | 0.1528 |
308.15 | 0.9208 | 0.0000 |
308.15 | 0.8704 | 0.0466 |
308.15 | 0.8521 | 0.0590 |
308.15 | 0.8153 | 0.0918 |
308.15 | 0.7995 | 0.1001 |
308.15 | 0.7710 | 0.1166 |
308.15 | 0.7563 | 0.1227 |
308.15 | 0.7186 | 0.1375 |
318.15 | 0.9138 | 0.0000 |
318.15 | 0.8624 | 0.0466 |
318.15 | 0.8431 | 0.0610 |
318.15 | 0.8177 | 0.0818 |
318.15 | 0.7814 | 0.1001 |
318.15 | 0.7413 | 0.1171 |
318.15 | 0.7053 | 0.1279 |
318.15 | 0.6536 | 0.1357 |
298.15 | 0.6915 | 0.1575 |
298.15 | 0.6612 | 0.1621 |
298.15 | 0.6306 | 0.1632 |
298.15 | 0.5983 | 0.1660 |
298.15 | 0.5611 | 0.1650 |
298.15 | 0.5128 | 0.1659 |
298.15 | 0.4536 | 0.1622 |
298.15 | 0.4255 | 0.1621 |
298.15 | 0.3518 | 0.1529 |
308.15 | 0.6958 | 0.1416 |
308.15 | 0.6605 | 0.1487 |
308.15 | 0.6282 | 0.1503 |
308.15 | 0.5576 | 0.1556 |
308.15 | 0.5168 | 0.1543 |
308.15 | 0.4742 | 0.1531 |
308.15 | 0.4018 | 0.1494 |
308.15 | 0.3754 | 0.1438 |
318.15 | 0.6106 | 0.1386 |
318.15 | 0.5736 | 0.1396 |
318.15 | 0.5489 | 0.1396 |
318.15 | 0.5188 | 0.1403 |
318.15 | 0.4990 | 0.1413 |
318.15 | 0.4790 | 0.1423 |
318.15 | 0.4456 | 0.1395 |
318.15 | 0.4164 | 0.1375 |
298.15 | 0.3336 | 0.1481 |
298.15 | 0.2923 | 0.1309 |
298.15 | 0.2708 | 0.1203 |
298.15 | 0.2561 | 0.1035 |
298.15 | 0.2369 | 0.0873 |
298.15 | 0.2150 | 0.0690 |
298.15 | 0.1889 | 0.0466 |
298.15 | 0.1745 | 0.0300 |
308.15 | 0.1566 | 0.0000 |
308.15 | 0.3491 | 0.1392 |
308.15 | 0.3169 | 0.1305 |
308.15 | 0.2876 | 0.1179 |
308.15 | 0.2608 | 0.0967 |
308.15 | 0.2389 | 0.0776 |
308.15 | 0.2111 | 0.0517 |
308.15 | 0.1919 | 0.0316 |
308.15 | 0.1788 | 0.0000 |
318.15 | 0.3787 | 0.1305 |
318.15 | 0.3456 | 0.1228 |
318.15 | 0.3067 | 0.1077 |
318.15 | 0.2796 | 0.0938 |
318.15 | 0.2563 | 0.0768 |
318.15 | 0.2344 | 0.0560 |
318.15 | 0.2152 | 0.0336 |
318.15 | 0.1932 | 0.0000 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mass fraction of Water (3) - Liquid mixture 2 | Mass fraction of 2,3-Butanediol (2) - Liquid mixture 2 | Mass fraction of 2,3-Butanediol (2) - Liquid mixture 1 | Mass fraction of Water (3) - Liquid mixture 1 |
298.15 | 0.7405 | 0.1418 | 0.1189 | 0.2738 |
308.15 | 0.8103 | 0.0933 | 0.0685 | 0.2282 |
308.15 | 0.7648 | 0.1186 | 0.0910 | 0.2550 |
308.15 | 0.6977 | 0.1405 | 0.1086 | 0.2735 |
308.15 | 0.7463 | 0.1278 | 0.0960 | 0.2601 |
318.15 | 0.8601 | 0.0467 | 0.0389 | 0.2200 |
318.15 | 0.8346 | 0.0680 | 0.0524 | 0.2275 |
318.15 | 0.7989 | 0.0907 | 0.0662 | 0.2503 |
318.15 | 0.7683 | 0.1080 | 0.0795 | 0.2623 |
318.15 | 0.7335 | 0.1187 | 0.0954 | 0.2798 |
318.15 | 0.6996 | 0.1289 | 0.1074 | 0.3047 |
298.15 | 0.8001 | 0.1061 | 0.0814 | 0.2352 |
318.15 | 0.6576 | 0.1388 | 0.1201 | 0.3302 |
298.15 | 0.8291 | 0.0847 | 0.0584 | 0.2096 |
298.15 | 0.8399 | 0.0734 | 0.0475 | 0.1968 |
298.15 | 0.8565 | 0.0593 | 0.0383 | 0.1897 |
298.15 | 0.8209 | 0.0931 | 0.0655 | 0.2179 |
308.15 | 0.8675 | 0.0503 | 0.0443 | 0.2051 |
308.15 | 0.8451 | 0.0651 | 0.0518 | 0.2111 |
308.15 | 0.8276 | 0.0809 | 0.0632 | 0.2247 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid mixture 1 | Mass fraction of Water (3) - Liquid mixture 1 | Mass fraction of 2,3-Butanediol (2) - Liquid mixture 1 |
298.15 | 0.9184 | 0.0000 |
298.15 | 0.8400 | 0.0734 |
298.15 | 0.8300 | 0.0808 |
298.15 | 0.8063 | 0.1013 |
298.15 | 0.7726 | 0.1243 |
298.15 | 0.7561 | 0.1317 |
298.15 | 0.7429 | 0.1400 |
298.15 | 0.7247 | 0.1448 |
298.15 | 0.7109 | 0.1528 |
308.15 | 0.9208 | 0.0000 |
308.15 | 0.8704 | 0.0466 |
308.15 | 0.8521 | 0.0590 |
308.15 | 0.8153 | 0.0918 |
308.15 | 0.7995 | 0.1001 |
308.15 | 0.7710 | 0.1166 |
308.15 | 0.7563 | 0.1227 |
308.15 | 0.7186 | 0.1375 |
318.15 | 0.9138 | 0.0000 |
318.15 | 0.8624 | 0.0466 |
318.15 | 0.8431 | 0.0610 |
318.15 | 0.8177 | 0.0818 |
318.15 | 0.7814 | 0.1001 |
318.15 | 0.7413 | 0.1171 |
318.15 | 0.7053 | 0.1279 |
318.15 | 0.6536 | 0.1357 |
298.15 | 0.6915 | 0.1575 |
298.15 | 0.6612 | 0.1621 |
298.15 | 0.6306 | 0.1632 |
298.15 | 0.5983 | 0.1660 |
298.15 | 0.5611 | 0.1650 |
298.15 | 0.5128 | 0.1659 |
298.15 | 0.4536 | 0.1622 |
298.15 | 0.4255 | 0.1621 |
298.15 | 0.3518 | 0.1529 |
308.15 | 0.6958 | 0.1416 |
308.15 | 0.6605 | 0.1487 |
308.15 | 0.6282 | 0.1503 |
308.15 | 0.5576 | 0.1556 |
308.15 | 0.5168 | 0.1543 |
308.15 | 0.4742 | 0.1531 |
308.15 | 0.4018 | 0.1494 |
308.15 | 0.3754 | 0.1438 |
318.15 | 0.6106 | 0.1386 |
318.15 | 0.5736 | 0.1396 |
318.15 | 0.5489 | 0.1396 |
318.15 | 0.5188 | 0.1403 |
318.15 | 0.4990 | 0.1413 |
318.15 | 0.4790 | 0.1423 |
318.15 | 0.4456 | 0.1395 |
318.15 | 0.4164 | 0.1375 |
298.15 | 0.3336 | 0.1481 |
298.15 | 0.2923 | 0.1309 |
298.15 | 0.2708 | 0.1203 |
298.15 | 0.2561 | 0.1035 |
298.15 | 0.2369 | 0.0873 |
298.15 | 0.2150 | 0.0690 |
298.15 | 0.1889 | 0.0466 |
298.15 | 0.1745 | 0.0300 |
308.15 | 0.1566 | 0.0000 |
308.15 | 0.3491 | 0.1392 |
308.15 | 0.3169 | 0.1305 |
308.15 | 0.2876 | 0.1179 |
308.15 | 0.2608 | 0.0967 |
308.15 | 0.2389 | 0.0776 |
308.15 | 0.2111 | 0.0517 |
308.15 | 0.1919 | 0.0316 |
308.15 | 0.1788 | 0.0000 |
318.15 | 0.3787 | 0.1305 |
318.15 | 0.3456 | 0.1228 |
318.15 | 0.3067 | 0.1077 |
318.15 | 0.2796 | 0.0938 |
318.15 | 0.2563 | 0.0768 |
318.15 | 0.2344 | 0.0560 |
318.15 | 0.2152 | 0.0336 |
318.15 | 0.1932 | 0.0000 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mass fraction of Water (3) - Liquid mixture 2 | Mass fraction of 2,3-Butanediol (2) - Liquid mixture 2 | Mass fraction of 2,3-Butanediol (2) - Liquid mixture 1 | Mass fraction of Water (3) - Liquid mixture 1 |
298.15 | 0.7405 | 0.1418 | 0.1189 | 0.2738 |
308.15 | 0.8103 | 0.0933 | 0.0685 | 0.2282 |
308.15 | 0.7648 | 0.1186 | 0.0910 | 0.2550 |
308.15 | 0.6977 | 0.1405 | 0.1086 | 0.2735 |
308.15 | 0.7463 | 0.1278 | 0.0960 | 0.2601 |
318.15 | 0.8601 | 0.0467 | 0.0389 | 0.2200 |
318.15 | 0.8346 | 0.0680 | 0.0524 | 0.2275 |
318.15 | 0.7989 | 0.0907 | 0.0662 | 0.2503 |
318.15 | 0.7683 | 0.1080 | 0.0795 | 0.2623 |
318.15 | 0.7335 | 0.1187 | 0.0954 | 0.2798 |
318.15 | 0.6996 | 0.1289 | 0.1074 | 0.3047 |
298.15 | 0.8001 | 0.1061 | 0.0814 | 0.2352 |
318.15 | 0.6576 | 0.1388 | 0.1201 | 0.3302 |
298.15 | 0.8291 | 0.0847 | 0.0584 | 0.2096 |
298.15 | 0.8399 | 0.0734 | 0.0475 | 0.1968 |
298.15 | 0.8565 | 0.0593 | 0.0383 | 0.1897 |
298.15 | 0.8209 | 0.0931 | 0.0655 | 0.2179 |
308.15 | 0.8675 | 0.0503 | 0.0443 | 0.2051 |
308.15 | 0.8451 | 0.0651 | 0.0518 | 0.2111 |
308.15 | 0.8276 | 0.0809 | 0.0632 | 0.2247 |