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 | 0.2030 | 0.0000 |
298.15 | 0.2218 | 0.0297 |
298.15 | 0.2388 | 0.0460 |
298.15 | 0.2562 | 0.0624 |
298.15 | 0.2704 | 0.0766 |
298.15 | 0.2853 | 0.0841 |
298.15 | 0.3032 | 0.0947 |
298.15 | 0.3240 | 0.1066 |
298.15 | 0.3397 | 0.1144 |
298.15 | 0.3591 | 0.1203 |
298.15 | 0.3711 | 0.1245 |
298.15 | 0.3744 | 0.1278 |
298.15 | 0.4017 | 0.1337 |
298.15 | 0.4085 | 0.1335 |
298.15 | 0.4236 | 0.1376 |
298.15 | 0.4305 | 0.1380 |
298.15 | 0.4399 | 0.1396 |
298.15 | 0.4531 | 0.1414 |
298.15 | 0.4595 | 0.1423 |
298.15 | 0.4694 | 0.1427 |
298.15 | 0.4815 | 0.1444 |
298.15 | 0.5159 | 0.1460 |
298.15 | 0.5355 | 0.1466 |
298.15 | 0.5614 | 0.1483 |
298.15 | 0.5833 | 0.1471 |
298.15 | 0.6045 | 0.1471 |
298.15 | 0.6272 | 0.1465 |
298.15 | 0.6566 | 0.1453 |
298.15 | 0.6877 | 0.1439 |
298.15 | 0.7189 | 0.1398 |
298.15 | 0.7547 | 0.1309 |
298.15 | 0.7901 | 0.1156 |
298.15 | 0.9200 | 0.0000 |
308.15 | 0.2110 | 0.0000 |
308.15 | 0.2215 | 0.0200 |
308.15 | 0.2535 | 0.0521 |
308.15 | 0.2876 | 0.0664 |
308.15 | 0.3057 | 0.0893 |
308.15 | 0.3348 | 0.1058 |
308.15 | 0.3888 | 0.1254 |
308.15 | 0.4377 | 0.1321 |
308.15 | 0.4646 | 0.1346 |
308.15 | 0.4918 | 0.1360 |
308.15 | 0.4975 | 0.1354 |
308.15 | 0.5211 | 0.1368 |
308.15 | 0.5494 | 0.1376 |
308.15 | 0.5789 | 0.1370 |
308.15 | 0.6343 | 0.1357 |
308.15 | 0.6647 | 0.1345 |
308.15 | 0.7032 | 0.1310 |
308.15 | 0.7376 | 0.1257 |
308.15 | 0.7688 | 0.1175 |
308.15 | 0.8432 | 0.0788 |
308.15 | 0.9305 | 0.0000 |
318.15 | 0.2242 | 0.0000 |
318.15 | 0.2338 | 0.0227 |
318.15 | 0.2601 | 0.0475 |
318.15 | 0.2905 | 0.0729 |
318.15 | 0.3123 | 0.0844 |
318.15 | 0.3418 | 0.0978 |
318.15 | 0.3692 | 0.1087 |
318.15 | 0.3932 | 0.1140 |
318.15 | 0.4164 | 0.1194 |
318.15 | 0.4181 | 0.1219 |
318.15 | 0.4379 | 0.1219 |
318.15 | 0.4544 | 0.1249 |
318.15 | 0.4580 | 0.1246 |
318.15 | 0.4711 | 0.1253 |
318.15 | 0.4751 | 0.1263 |
318.15 | 0.4909 | 0.1268 |
318.15 | 0.4954 | 0.1268 |
318.15 | 0.5092 | 0.1272 |
318.15 | 0.5228 | 0.1278 |
318.15 | 0.5504 | 0.1286 |
318.15 | 0.5789 | 0.1282 |
318.15 | 0.6165 | 0.1268 |
318.15 | 0.6593 | 0.1246 |
318.15 | 0.6890 | 0.1219 |
318.15 | 0.7216 | 0.1183 |
318.15 | 0.7453 | 0.1144 |
318.15 | 0.7708 | 0.1082 |
318.15 | 0.7906 | 0.1019 |
318.15 | 0.8377 | 0.0789 |
318.15 | 0.9320 | 0.0000 |
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 | Mass fraction of 2,3-Butanediol (2) - Liquid mixture 2 | Mass fraction of Water (3) - Liquid mixture 2 |
298.15 | 0.2521 | 0.0489 | 0.0683 | 0.8380 |
298.15 | 0.2173 | 0.0210 | 0.0289 | 0.8813 |
298.15 | 0.3418 | 0.1070 | 0.1284 | 0.7450 |
298.15 | 0.3957 | 0.1196 | 0.1353 | 0.6766 |
298.15 | 0.2697 | 0.0658 | 0.0877 | 0.8212 |
298.15 | 0.2324 | 0.0349 | 0.0467 | 0.8573 |
308.15 | 0.3288 | 0.0859 | 0.0940 | 0.8100 |
308.15 | 0.2591 | 0.0518 | 0.0593 | 0.8587 |
308.15 | 0.2888 | 0.0688 | 0.0760 | 0.8392 |
308.15 | 0.2234 | 0.0221 | 0.0279 | 0.8970 |
308.15 | 0.3651 | 0.1112 | 0.1170 | 0.7488 |
308.15 | 0.4318 | 0.1244 | 0.1321 | 0.6901 |
318.15 | 0.3317 | 0.0907 | 0.0912 | 0.7990 |
318.15 | 0.2536 | 0.0390 | 0.0426 | 0.8751 |
318.15 | 0.2725 | 0.0533 | 0.0543 | 0.8596 |
318.15 | 0.3103 | 0.0724 | 0.0747 | 0.8347 |
318.15 | 0.2357 | 0.0239 | 0.0254 | 0.8979 |
318.15 | 0.3964 | 0.1117 | 0.1162 | 0.7022 |
318.15 | 0.4740 | 0.1241 | 0.1309 | 0.6137 |
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 | 0.2030 | 0.0000 |
298.15 | 0.2218 | 0.0297 |
298.15 | 0.2388 | 0.0460 |
298.15 | 0.2562 | 0.0624 |
298.15 | 0.2704 | 0.0766 |
298.15 | 0.2853 | 0.0841 |
298.15 | 0.3032 | 0.0947 |
298.15 | 0.3240 | 0.1066 |
298.15 | 0.3397 | 0.1144 |
298.15 | 0.3591 | 0.1203 |
298.15 | 0.3711 | 0.1245 |
298.15 | 0.3744 | 0.1278 |
298.15 | 0.4017 | 0.1337 |
298.15 | 0.4085 | 0.1335 |
298.15 | 0.4236 | 0.1376 |
298.15 | 0.4305 | 0.1380 |
298.15 | 0.4399 | 0.1396 |
298.15 | 0.4531 | 0.1414 |
298.15 | 0.4595 | 0.1423 |
298.15 | 0.4694 | 0.1427 |
298.15 | 0.4815 | 0.1444 |
298.15 | 0.5159 | 0.1460 |
298.15 | 0.5355 | 0.1466 |
298.15 | 0.5614 | 0.1483 |
298.15 | 0.5833 | 0.1471 |
298.15 | 0.6045 | 0.1471 |
298.15 | 0.6272 | 0.1465 |
298.15 | 0.6566 | 0.1453 |
298.15 | 0.6877 | 0.1439 |
298.15 | 0.7189 | 0.1398 |
298.15 | 0.7547 | 0.1309 |
298.15 | 0.7901 | 0.1156 |
298.15 | 0.9200 | 0.0000 |
308.15 | 0.2110 | 0.0000 |
308.15 | 0.2215 | 0.0200 |
308.15 | 0.2535 | 0.0521 |
308.15 | 0.2876 | 0.0664 |
308.15 | 0.3057 | 0.0893 |
308.15 | 0.3348 | 0.1058 |
308.15 | 0.3888 | 0.1254 |
308.15 | 0.4377 | 0.1321 |
308.15 | 0.4646 | 0.1346 |
308.15 | 0.4918 | 0.1360 |
308.15 | 0.4975 | 0.1354 |
308.15 | 0.5211 | 0.1368 |
308.15 | 0.5494 | 0.1376 |
308.15 | 0.5789 | 0.1370 |
308.15 | 0.6343 | 0.1357 |
308.15 | 0.6647 | 0.1345 |
308.15 | 0.7032 | 0.1310 |
308.15 | 0.7376 | 0.1257 |
308.15 | 0.7688 | 0.1175 |
308.15 | 0.8432 | 0.0788 |
308.15 | 0.9305 | 0.0000 |
318.15 | 0.2242 | 0.0000 |
318.15 | 0.2338 | 0.0227 |
318.15 | 0.2601 | 0.0475 |
318.15 | 0.2905 | 0.0729 |
318.15 | 0.3123 | 0.0844 |
318.15 | 0.3418 | 0.0978 |
318.15 | 0.3692 | 0.1087 |
318.15 | 0.3932 | 0.1140 |
318.15 | 0.4164 | 0.1194 |
318.15 | 0.4181 | 0.1219 |
318.15 | 0.4379 | 0.1219 |
318.15 | 0.4544 | 0.1249 |
318.15 | 0.4580 | 0.1246 |
318.15 | 0.4711 | 0.1253 |
318.15 | 0.4751 | 0.1263 |
318.15 | 0.4909 | 0.1268 |
318.15 | 0.4954 | 0.1268 |
318.15 | 0.5092 | 0.1272 |
318.15 | 0.5228 | 0.1278 |
318.15 | 0.5504 | 0.1286 |
318.15 | 0.5789 | 0.1282 |
318.15 | 0.6165 | 0.1268 |
318.15 | 0.6593 | 0.1246 |
318.15 | 0.6890 | 0.1219 |
318.15 | 0.7216 | 0.1183 |
318.15 | 0.7453 | 0.1144 |
318.15 | 0.7708 | 0.1082 |
318.15 | 0.7906 | 0.1019 |
318.15 | 0.8377 | 0.0789 |
318.15 | 0.9320 | 0.0000 |
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 | Mass fraction of 2,3-Butanediol (2) - Liquid mixture 2 | Mass fraction of Water (3) - Liquid mixture 2 |
298.15 | 0.2521 | 0.0489 | 0.0683 | 0.8380 |
298.15 | 0.2173 | 0.0210 | 0.0289 | 0.8813 |
298.15 | 0.3418 | 0.1070 | 0.1284 | 0.7450 |
298.15 | 0.3957 | 0.1196 | 0.1353 | 0.6766 |
298.15 | 0.2697 | 0.0658 | 0.0877 | 0.8212 |
298.15 | 0.2324 | 0.0349 | 0.0467 | 0.8573 |
308.15 | 0.3288 | 0.0859 | 0.0940 | 0.8100 |
308.15 | 0.2591 | 0.0518 | 0.0593 | 0.8587 |
308.15 | 0.2888 | 0.0688 | 0.0760 | 0.8392 |
308.15 | 0.2234 | 0.0221 | 0.0279 | 0.8970 |
308.15 | 0.3651 | 0.1112 | 0.1170 | 0.7488 |
308.15 | 0.4318 | 0.1244 | 0.1321 | 0.6901 |
318.15 | 0.3317 | 0.0907 | 0.0912 | 0.7990 |
318.15 | 0.2536 | 0.0390 | 0.0426 | 0.8751 |
318.15 | 0.2725 | 0.0533 | 0.0543 | 0.8596 |
318.15 | 0.3103 | 0.0724 | 0.0747 | 0.8347 |
318.15 | 0.2357 | 0.0239 | 0.0254 | 0.8979 |
318.15 | 0.3964 | 0.1117 | 0.1162 | 0.7022 |
318.15 | 0.4740 | 0.1241 | 0.1309 | 0.6137 |